Porous Flow Requirements Traceability Matrix

This template follows Idaho National Laboratory (INL) template TEM-214, "IT System Requirements Traceability Matrix."

note

This document serves as an addendum to Framework Requirements Traceability Matrix and captures information for Requirement Traceability Matrix (RTM) specific to the Porous Flow application.

Framework Requirements Traceability Matrix

Introduction

Minimum System Requirements

In general, the following is required for MOOSE-based development:

GCC/Clang C++17 compliant compiler (GCC @ 7.5.0, Clang @ 5.0.2 or greater)
- Note: Intel compilers are not supported.
Memory: 16 GBs (debug builds)
Processor: 64-bit x86
Disk: 30GB

System Purpose

The Multiphysics Object Oriented Simulation Environment (MOOSE) is a tool for solving complex coupled Multiphysics equations using the finite element method. MOOSE uses an object-oriented design to abstract data structure management, parallelism, threading and compiling while providing an easy to use interface targeted at engineers that may not have a lot of software development experience. MOOSE will require extreme scalability and flexibility when compared to other FEM frameworks. For instance, MOOSE needs the ability to run extremely complex material models, or even third-party applications within a parallel simulation without sacrificing parallelism. This capability is in contrast to what is often seen in commercial packages, where custom material models can limit the parallel scalability, forcing serial runs in the most severe cases. When comparing high-end capabilities, many MOOSE competitors target modest-sized clusters with just a few thousand processing cores. MOOSE, however, will be required to routinely executed on much larger clusters with scalability to clusters available in the top 500 systems (top500.org). MOOSE will also be targeted at smaller systems such as high-end laptop computers.

The design goal of MOOSE is to give developers ultimate control over their physical models and applications. Designing new models or solving completely new classes of problems will be accomplished by writing standard C++ source code within the framework's class hierarchy. Scientists and engineers will be free to implement completely new algorithms using pieces of the framework where possible, and extending the framework's capabilities where it makes sense to do so. Commercial applications do not have this capability, and instead opt for either a more rigid parameter system or a limited application-specific metalanguage.

System Scope

MOOSE's scope is to provide a set of interfaces for building Finite Element Method (FEM) simulations. Abstractions to all underlying libraries are provided.

Solving coupled problems where competing physical phenomena impact one and other in a significant nonlinear fashion represents a serious challenge to several solution strategies. Small perturbations in strongly-coupled parameters often have very large adverse effects on convergence behavior. These adverse effects are compounded as additional physics are added to a model. To overcome these challenges, MOOSE employs three distinct yet compatible systems for solving these types of problems.

First, an advanced numerical technique called the Jacobian-Free Newton-Krylov (JFNK) method is employed to solve the most fully-coupled physics in an accurate, consistent way. An example of this would be the effect of temperature on the expansion or contraction of a material. While the JFNK numerical method is very effective at solving fully-coupled equations, it can also be computationally expensive. Plus, not all physical phenomena in a given model are truly coupled to one another. For instance, in a reactor, the speed of the coolant flow may not have any direct effect on the complex chemical reactions taking place inside the fuel rods. We call such models "loosely-coupled". A robust, scalable system must strike the proper balance between the various modeling strategies to avoid performing unnecessary computations or incorrectly predicting behavior in situations such as these.

MOOSE's Multiapp system will allow modelers to group physics into logical categories where MOOSE can solve some groups fully-coupled and others loosely-coupled. The Multiapp system goes even further by also supporting a "tightly-coupled" strategy, which falls somewhere between the "fully-coupled" and "loosely-coupled" approaches. Several sets of physics can then be linked together into logical hierarchies using any one of these coupling strategies, allowing for several potential solution strategies. For instance, a complex nuclear reactor model might consist of several tightly-coupled systems of fully-coupled equations.

Finally, MOOSE's Transfers system ties all of the physics groups contained within the Multiapp system together and allows for full control over the flow of information among the various groups. This capability bridges physical phenomena from several different complementary scales simultaneously. When these three MOOSE systems are combined, myriad coupling combinations are possible. In all cases, the MOOSE framework handles the parallel communication, input, output and execution of the underlying simulation. By handling these computer science tasks, the MOOSE framework keeps modelers focused on doing research.

MOOSE innovates by building advanced simulation capabilities on top of the very best available software technologies in a way that makes them widely accessible for innovative research. MOOSE is equally capable of solving small models on common laptops and the very biggest FEM models ever attempted—all without any major changes to configuration or source code. Since its inception, the MOOSE project has focused on both developer and computational efficiency. Improved developer efficiency is achieved by leveraging existing algorithms and technologies from several leading open-source packages. Additionally, MOOSE uses several complementary parallel technologies (both the distributed-memory message passing paradigm and shared-memory thread-based approaches are used) to lay an efficient computational foundation for development. Using existing open technologies in this manner helps the developers reduce the scope of the project and keeps the size of the MOOSE code base maintainable. This approach provides users with state-of-the-art finite element and solver technology as a basis for the advanced coupling and solution strategies mentioned previously.

MOOSE's developers work openly with other package developers to make sure that cutting-edge technologies are available through MOOSE, providing researchers with competitive research opportunities. MOOSE maintains a set of objects that hide parallel interfaces while exposing advanced spatial and temporal coupling algorithms in the framework. This accessible approach places developmental technology into the hands of scientists and engineers, which can speed the pace of scientific discovery.

Assumptions and Dependencies

The Porous Flow application is developed using MOOSE and is based on various modules, as such the RTM for Porous Flow is dependent upon the files listed at the beginning of this document.

Pre-test Instructions/Environment/Setup

Ideally all testing should be performed on a clean test machine following one of the supported configurations setup by the test system engineer. Testing may be performed on local workstations and cluster systems containing supported operating systems.

The repository should be clean prior to building and testing. When using "git" this can be done by doing a force clean in the main repository and each one of the submodules:


git clean -xfd
git submodule foreach 'git clean -xfd'

All tests must pass in accordance with the type of test being performed. This list can be found in the Software Test Plan.

System Requirements Traceability

Functional Requirements

porous_flow: Actions
16.1.1The system shall calculate proper density, viscosity, enthalpy and internal energy with the PorousFlowBrine material when using PorousFlowFullySaturated Action.
Specification(s): fullsat_brine
Design: Brine and carbon dioxide
Issue(s): #10093
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.1.2The system shall produce an error when attempting to use a PorousFlowBrine Material without any NaCl variable
Specification(s): fullsat_brine_except1
Design: Brine and carbon dioxide
Issue(s): #10093 #16841
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.1.3The system shall produce an error when attempting to use a PorousFlowBrine Material at the same time as a PorousFlowSimpleFluidProperties Material
Specification(s): fullsat_brine_except2
Design: Brine and carbon dioxide
Issue(s): #10093 #16841
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.1.4The system shall produce an error when attempting to use a PorousFlowSingleComponentFluid Material at the same time as a PorousFlowBrine Material
Specification(s): fullsat_brine_except3
Design: Brine and carbon dioxide
Issue(s): #10093 #16841
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.1.5The system shall produce an error when attempting to use a PorousFlowSingleComponentFluid Material without a fluid-properties UserObject
Specification(s): fullsat_brine_except4
Design: PorousFlowFullySaturated
Issue(s): #16841
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.1.6The system shall produce an error when attempting to use a non-standard pressure unit choice with PorousFlowBrine
Specification(s): fullsat_brine_except5
Design: PorousFlowFullySaturated
Issue(s): #16841
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.1.7The system shall produce an error when attempting to use a non-standard time unit choice with PorousFlowBrine
Specification(s): fullsat_brine_except6
Design: PorousFlowFullySaturated
Issue(s): #16841
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.1.8The system shall produce an error if PorousFlowUnsaturated is used with no stabilization.
Specification(s): unsat_except1
Design: PorousFlowUnsaturated
Issue(s): #16841
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.1.9The system shall produce an error if the number of variables to save fluid-component rates-of-change into is not equal to the number of fluid components
Specification(s): unsat_except2
Design: PorousFlowUnsaturated
Issue(s): #16841
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.1.10The system shall produce a warning when attempting to add materials to the simulation when using the PorousFlowFullySaturated Action.
Specification(s): addjoiner
Design: PorousFlowAddMaterialJoiner
Issue(s): #10093
Collection(s): FUNCTIONAL
Type(s): RunApp
31
16.1.11The system shall handle adding materials properly when the add_nodes parameter and the at_nodes=true parameters are both active in the PorousFlowFullySaturated Action.
Specification(s): addmaterials
Design: PorousFlowAddMaterialAction
Issue(s): #10093
Collection(s): FUNCTIONAL
Type(s): RunApp
31
16.1.12The system shall handle adding materials properly when the add_nodes parameter is supplied in the PorousFlowFullySaturated Action.
Specification(s): addmaterials2
Design: PorousFlowAddMaterialAction
Issue(s): #10093
Collection(s): FUNCTIONAL
Type(s): RunApp
31
16.1.13The system shall add all required objects when using PorousFlowBasicTHM Action with coupling_type = Hydro.
Specification(s): basicthm_h
Design: PorousFlowBasicTHM
Issue(s): #8574
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.1.14The system shall add all required objects when using PorousFlowBasicTHM Action with coupling_type = ThermoHydro.
Specification(s): basicthm_th
Design: PorousFlowBasicTHM
Issue(s): #8574
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.1.15The system shall add all required objects when using PorousFlowBasicTHM Action with coupling_type = HydroMechanical.
Specification(s): basicthm_hm
Design: PorousFlowBasicTHM
Issue(s): #8574
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.1.16The system shall add all required objects when using PorousFlowBasicTHM Action with coupling_type = ThermoHydroMechanical.
Specification(s): basicthm_thm
Design: PorousFlowBasicTHM
Issue(s): #8574
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.1.17The system shall handle adding materials properly when materials are block restricted
Specification(s): block_restricted
Design: PorousFlowAddMaterialJoiner PorousFlowAddMaterialAction
Issue(s): #10093
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.1.18The system shall add all required objects when using PorousFlowBasicTHM Action to allow boreholes to be used
Specification(s): basicthm_bh
Design: PorousFlowBasicTHM
Issue(s): #17025
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.1.19The system shall add all required objects when using PorousFlowFullySaturated Action to allow boreholes to be used
Specification(s): fullsat_bh
Design: PorousFlowFullySaturated
Issue(s): #17025
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.1.20PorousFlow shall be able to be block-restricted, specifically so that a model's physics is governed by PorousFlow only on part of the mesh
Specification(s): multiblock
Design: PorousFlowAddMaterialJoiner
Issue(s): #20260
Collection(s): FUNCTIONAL
Type(s): CSVDiff
7
16.1.21PorousFlow shall be able to be block-restricted, and Joiners shall work even when one PorousFlow material is block-restricted for one phase and non block-restricted for another
Specification(s): block_restricted_and_not
Design: PorousFlowAddMaterialJoiner
Issue(s): #20260
Collection(s): FUNCTIONAL
Type(s): RunApp
31

porous_flow: Adaptivity
16.2.1The system shall work when using mesh adaptivity with TRI3 elements
Specification(s): tri
Design: Mass lumping
Issue(s): #14428
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.2.2The system shall work when using mesh adaptivity with QUAD elements
Specification(s): quad
Design: Mass lumping
Issue(s): #14428
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.2.3The system shall work when using mesh adaptivity with TET4 elements
Specification(s): tet
Design: Mass lumping
Issue(s): #14428
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.2.4The system shall work when using mesh adaptivity with HEX elements
Specification(s): hex
Design: Mass lumping
Issue(s): #14428
Collection(s): FUNCTIONAL
Type(s): Exodiff
31

porous_flow: Aux Kernels
16.3.1PorousFlow shall be able to calculate the Darcy flow velocity vector for a fully-saturated case
Specification(s): darcy_velocity
Design: PorousFlowDarcyVelocityComponent
Issue(s): #17159
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.3.2PorousFlow shall be able to populate AuxVariables corresponding to capillary pressure, saturation, fluid density, etc
Specification(s): properties
Design: PorousFlowPropertyAux
Issue(s): #17159
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.3.3PorousFlow shall be able to calculate the Darcy flow velocity vector on 2D fracture embedded inside a 3D matrix
Specification(s): darcy_velocity_lower
Design: PorousFlowDarcyVelocityComponentLowerDimensional
Issue(s): #17159
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.3.4PorousFlow shall be able to calculate the Darcy flow velocity vector on 2D fracture embedded inside a 3D matrix, including the case with triangular and tetrahedral elements
Specification(s): darcy_velocity_lower_tets
Design: PorousFlowDarcyVelocityComponentLowerDimensional
Issue(s): #17159
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.3.3
31
16.3.5PorousFlow shall be able to calculate the Darcy flow velocity vector on 1D fracture embedded inside a 2D matrix
Specification(s): darcy_velocity_lower_2D
Design: PorousFlowDarcyVelocityComponentLowerDimensional
Issue(s): #17159
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.3.6An error shall be produced if PorousFlow is asked to calculate the Darcy flow velocity vector on a lower-dimensional fracture, but the variables are not defined only on the lower-dimensional elements
Specification(s): darcy_velocity_lower_except
Design: PorousFlowDarcyVelocityComponentLowerDimensional
Issue(s): #17159
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.3.7PorousFlow shall be able to calculate a measure of element length in a given direction, and shall produce an error if a nodal variable is used to store the results
Specification(s): element_length_except1
Design: PorousFlowElementLength
Issue(s): #18232
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.3.8PorousFlow shall be able to calculate a measure of element length in a given direction, and shall produce an error if the direction is incorrectly specified
Specification(s): element_length_except2
Design: PorousFlowElementLength
Issue(s): #18232
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.3.9PorousFlow shall be able to calculate a measure of element length in a given direction, in 2D
Specification(s): element_length_2D
Design: PorousFlowElementLength
Issue(s): #18232
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.3.10PorousFlow shall be able to calculate a measure of element length in a given direction, in 3D
Specification(s): element_length_3D
Design: PorousFlowElementLength
Issue(s): #18232
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.3.11PorousFlow shall be able to calculate element normal, and shall produce an error if a nodal variable is used to store the result
Specification(s): element_normal_except1
Design: PorousFlowElementNormal
Issue(s): #18232
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.3.12PorousFlow shall be able to calculate element normal for 1D elements if provided with a perpendicular vector, and shall produce an error if the perpendicular vector is incorrectly specified
Specification(s): element_normal_except2
Design: PorousFlowElementNormal
Issue(s): #18232
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.3.13PorousFlow shall be able to calculate element normals for meshes containing 3D elements if provided with a default value for the 3D elements, but shall produce an error if that default value is incorrectly specified
Specification(s): element_normal_except3
Design: PorousFlowElementNormal
Issue(s): #18232
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.3.14PorousFlow shall be able to calculate element normals for 1D and 2D elements, if provided with a perpendicular vector for the 1D elements
Specification(s): element_normal_1D_2D
Design: PorousFlowElementNormal
Issue(s): #18232
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.3.15PorousFlow shall be able to calculate element normals for 2D and 3D elements, if provided with a default value for the 3D elements
Specification(s): element_normal_2D_3D
Design: PorousFlowElementNormal
Issue(s): #18232
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Basic Advection
16.4.1
Specification(s): except1
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.4.2
Specification(s): except2
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.4.3
Specification(s): 1phase
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.4.4
Specification(s): 2phase
Collection(s): FUNCTIONAL
Type(s): Exodiff
31

porous_flow: Buckley Leverett
16.5.1PorousFlow shall be able to simulate a Buckley-Leverett problem
Specification(s): bl01
Design: Injection ala Buckley and Leverett
Issue(s): #13155 #16953
Collection(s): FUNCTIONAL
Type(s): Exodiff
58
16.5.2PorousFlow shall be able to simulate a Buckley-Leverett problem with small saturation
Specification(s): bl01_heavy
Design: Injection ala Buckley and Leverett
Issue(s): #13155 #16953
Collection(s): FUNCTIONAL
Type(s): CSVDiff
1

porous_flow: Capillary Pressure
16.6.1
Specification(s): brookscorey1
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.6.2
Specification(s): brookscorey2
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.6.3
Specification(s): vangenuchten1
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.6.4
Specification(s): vangenuchten2
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.6.5
Specification(s): vangenuchten3
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Chemistry
16.7.1
Specification(s): except1
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.2
Specification(s): except2
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.3
Specification(s): except3
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.4
Specification(s): except5
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.5
Specification(s): except6
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.6
Specification(s): except7
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.7
Specification(s): except8
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.8
Specification(s): except9
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.9
Specification(s): except10
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.10
Specification(s): except11
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.11
Specification(s): except12
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.12
Specification(s): except13
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.13
Specification(s): except14
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.14
Specification(s): except15
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.15
Specification(s): except16
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.16
Specification(s): except17
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.17
Specification(s): except18
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.18
Specification(s): except19
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.19
Specification(s): except20
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.20
Specification(s): except21
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.21
Specification(s): except22
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.7.22
Specification(s): precipitation
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.7.23
Specification(s): precipitation_porosity_change
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.7.24
Specification(s): dissolution
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.7.25
Specification(s): dissolution_limited
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.7.26
Specification(s): 2species_equilibrium
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.7.27
Specification(s): 2species_predis
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.7.28
Specification(s): precipitation_2phase
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.7.29
Specification(s): dissolution_limited_2phase
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.7.30
Specification(s): 2species_equilibrium_2phase
Collection(s): FUNCTIONAL
Type(s): Exodiff
31

porous_flow: Density
16.8.1
Specification(s): GravDensity01
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Desorption
16.9.1
Specification(s): desorption01
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.9.2
Specification(s): desorption02
Collection(s): FUNCTIONAL
Type(s): Exodiff
31

porous_flow: Dirackernels
16.10.1PorousFlowSquarePulsePointSource shall provide a constant mass point source/sink between two specified times
Specification(s): squarepules
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowSquarePulsePointSource
Issue(s): #6990
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.2The system shall provide a mass point source/sink computed by a postprocessor
Specification(s): frompps
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPointSourceFromPostprocessor
Issue(s): #15132
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.3The system shall provide an enthalphy point source computed by a postprocessor
Specification(s): hfrompps
Design: Point and line sources/sinks PorousFlowPointEnthalpySourceFromPostprocessor
Issue(s): #15742
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.4PorousFlowSquarePulsePointSource shall provide a constant mass point sink between two specified times
Specification(s): theis1
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowSquarePulsePointSource
Issue(s): #6990
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.5PorousFlow shall be able to accurately simulate drawdown in 2D groundwater systems, to agree with the Theis solution
Specification(s): theis_rz
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowSquarePulsePointSource
Issue(s): #6990 #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.6PorousFlowSquarePulsePointSource shall provide a constant mass point sink between two specified times
Specification(s): theis2
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowSquarePulsePointSource
Issue(s): #6990
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.7PorousFlowSquarePulsePointSource shall provide a constant mass point source of a specified fluid phase
Specification(s): theis3
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowSquarePulsePointSource
Issue(s): #7677
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.8PorousFlowPeacemanBorehole shall throw an error if the fluid phase is larger than the number of phases in the system
Specification(s): bh_except01
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.9PorousFlowPeacemanBorehole shall throw an error if the fluid component is larger than the number of fluid components in the system
Specification(s): bh_except02
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.10PorousFlowPeacemanBorehole shall throw an error if flux is a function of porepressure but no porepressure material exists
Specification(s): bh_except03
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.11PorousFlowPeacemanBorehole shall throw an error if flux is a function of temperature but no temperature material exists
Specification(s): bh_except04
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.12PorousFlowPeacemanBorehole shall throw an error if flux is restricted to a specific fluid component but no mass fraction material exists
Specification(s): bh_except05
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.13PorousFlowPeacemanBorehole shall throw an error if flux is to be multiplied by mobility but no nodal fluid density material exists
Specification(s): bh_except06
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.14PorousFlowPeacemanBorehole shall throw an error if flux is to be multiplied by mobility but no nodal relative permeability material exists
Specification(s): bh_except07
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.15PorousFlowPeacemanBorehole shall throw an error if flux is to be multiplied by mobility but no nodal fluid density material exists
Specification(s): bh_except08
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.16PorousFlowPeacemanBorehole shall throw an error if flux is to be multiplied by enthalpy but no fluid enthalpy material exists
Specification(s): bh_except09
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.17PorousFlowPeacemanBorehole shall throw an error if flux is to be multiplied by internal energy but no fluid internal energy material exists
Specification(s): bh_except10
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.18PorousFlowPeacemanBorehole shall throw an error if flux is to be multiplied by relative permeability but no nodal relative permeability material exists
Specification(s): bh_except11
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.19PorousFlowPeacemanBorehole shall throw an error if the given point file does not exist
Specification(s): bh_except12
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.20PorousFlowPeacemanBorehole shall throw an error if two points in the point file are coincident
Specification(s): bh_except13
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.21PorousFlowPeacemanBorehole shall throw an error if the element containing the dirac kernel is not larger than the specified borehole radius
Specification(s): bh_except14
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.22PorousFlowPeacemanBorehole shall throw an error if flux is a function of porepressure but no permeability material exists
Specification(s): bh_except15
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.23PorousFlowPeacemanBorehole shall throw an error if flux is a function of temperature but no thermal conductivity material exists
Specification(s): bh_except16
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.24PorousFlowPolyLineSink shall extract fluid at the specified rate
Specification(s): pls01_00
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPolyLineSink
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.25PorousFlowPolyLineSink shall extract fluid at the specified rate when using the line_base parameter
Specification(s): pls01_line_base
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPolyLineSink
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.26PorousFlowPolyLineSink shall abort with an error if the line base, direction, and length cause the line to exit the mesh domain."
Specification(s): pls01_line_base_bounds
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPolyLineSink
Issue(s): #7992 #8139
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.27PorousFlowPolyLineSink shall extract fluid at the specified rate
Specification(s): pls01_01
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPolyLineSink
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.28PorousFlowPolyLineSink shall extract fluid at the specified rate
Specification(s): pls01_20
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPolyLineSink
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.29PorousFlowPolyLineSink shall extract fluid at the specified rate
Specification(s): pls01_21
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPolyLineSink
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.30PorousFlowPolyLineSink shall extract fluid at the specified rate
Specification(s): pls02
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPolyLineSink
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.31PorousFlowPolyLineSink shall be able to dynamically create dirac points automatically in response to changing mesh geometry.
Specification(s): pls02_autopoints
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPolyLineSink
Issue(s): #15528 #15547
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.32PorousFlowPolyLineSink shall extract fluid at the specified rate
Specification(s): pls03_00
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPolyLineSink
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.33PorousFlowPolyLineSink shall extract fluid at the specified rate
Specification(s): pls03_01
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPolyLineSink
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.34PorousFlowPolyLineSink shall extract fluid at the specified rate
Specification(s): pls03_20
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPolyLineSink
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.35PorousFlowPolyLineSink shall extract fluid at the specified rate
Specification(s): pls03_21
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPolyLineSink
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.36PorousFlowPolyLineSink shall extract fluid at the specified rate
Specification(s): pls03_action
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPolyLineSink
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.37PorousFlowPolyLineSink shall extract fluid at the specified rate getting the coordinates from a reporter
Specification(s): pls02reporter
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPolyLineSink
Issue(s): #20018
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.38PorousFlowPolyLineSink shall abort with an error if the reporter containing the coordinates is not the same size as the reporter containing weights
Specification(s): pls02reporter_wrongSize
Design: PorousFlowPolyLineSink
Issue(s): #20506
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.39PorousFlowPolyLineSink shall abort with an error if the coordinates reporter is empty
Specification(s): pls02reporter_empty
Design: PorousFlowPolyLineSink
Issue(s): #20506
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.10.40PorousFlowPeacemanBorehole shall extract fluid at the specified rate in a fully-saturated system
Specification(s): bh02
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.41PorousFlowPeacemanBorehole shall inject fluid at the specified rate in a fully-saturated system
Specification(s): bh03
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139 #20452
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.42PorousFlowPeacemanBorehole shall extract fluid at the specified rate in a fully-saturated system
Specification(s): bh04
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.43PorousFlowPeacemanBorehole shall inject fluid at the specified rate in an unsaturated system
Specification(s): bh05
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): CSVDiff
7
16.10.44PorousFlowPeacemanBorehole shall extract fluid at the specified rate in a cylindrical model
Specification(s): bh07
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.45PorousFlowPeacemanBorehole shall extract fluid at the specified rate in a cylindrical model
Specification(s): bh07_exo
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.10.46PorousFlowPeacemanBorehole shall extract fluid at the specified rate in a fully-saturated system using reporter for input
Specification(s): bh02reporter
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #20018
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.10.47Multiple PorousFlowPeacemanBorehole objects shall be able to inject and extract fluid in different locations
Specification(s): injection_production
Design: Point and line sources and sinks Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #7992 #8139
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.10.48If the strain at the nearest quadpoint is used when evaluating PorousFlowPorosity that is coupled to solid mechanics, all PorousFlow DiracKernels shall be usable
Specification(s): strain_at_nearest_qp
Design: Point and line sources and sinks Point and line sources/sinks
Issue(s): #12541
Collection(s): FUNCTIONAL
Type(s): RunApp
31
16.10.49It shall be possible to use PorousFlow DiracKernels in simulations involving plastic deformation
Specification(s): injection_with_plasticity
Design: Point and line sources/sinks PorousFlowPeacemanBorehole
Issue(s): #12962
Collection(s): FUNCTIONAL
Type(s): Exodiff
31

porous_flow: Dispersion
16.11.1PorousFlow shall correctly simulate the molecular diffusion
Specification(s): diff01
Design: Diffusion and hydrodynamic dispersion Tests
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.11.2PorousFlow shall correctly simulate the molecular diffusion when using an action
Specification(s): diff01_action
Design: Diffusion and hydrodynamic dispersion Tests
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.11.3PorousFlow shall correctly simulate the hydrodynamic dispersion
Specification(s): disp01
Design: Diffusion and hydrodynamic dispersion Tests
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.11.4PorousFlow shall correctly simulate the hydrodynamic dispersion in a high-resolution setting
Specification(s): disp01_heavy
Design: Diffusion and hydrodynamic dispersion Tests
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
1

porous_flow: Energy Conservation
16.12.1PorousFlow shall produce an error if the user specifies a phase number that is too large for the simulation according to the PorousFlowDictator
Specification(s): except01
Design: PorousFlowHeatEnergy PorousFlowHeatVolumetricExpansion PorousFlowEnergyTimeDerivative PorousFlowFullySaturatedHeatAdvection PorousFlowHeatAdvection PorousFlowHeatConduction PorousFlowPlasticHeatEnergy
Issue(s): #8123
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.12.2PorousFlow shall produce an error if the user specifies a porous-flow variable that is too large for the simulation according to the PorousFlowDictator
Specification(s): except02
Design: PorousFlowHeatEnergy PorousFlowHeatVolumetricExpansion PorousFlowEnergyTimeDerivative PorousFlowFullySaturatedHeatAdvection PorousFlowHeatAdvection PorousFlowHeatConduction PorousFlowPlasticHeatEnergy
Issue(s): #8123
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.12.3PorousFlow shall correctly calculate the heat energy using the heat-energy postprocessor when there are no fluids and constant porosity
Specification(s): heat01
Design: PorousFlowHeatEnergy PorousFlowHeatVolumetricExpansion PorousFlowEnergyTimeDerivative PorousFlowFullySaturatedHeatAdvection PorousFlowHeatAdvection PorousFlowHeatConduction PorousFlowPlasticHeatEnergy
Issue(s): #8123
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.12.4PorousFlow shall correctly calculate the heat energy using the heat-energy postprocessor when there is 1 fluid phase and constant porosity
Specification(s): heat02
Design: PorousFlowHeatEnergy PorousFlowHeatVolumetricExpansion PorousFlowEnergyTimeDerivative PorousFlowFullySaturatedHeatAdvection PorousFlowHeatAdvection PorousFlowHeatConduction PorousFlowPlasticHeatEnergy
Issue(s): #8123
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.12.5PorousFlow shall correctly conserve heat energy in a THM simulation when the model is squashed mechanically
Specification(s): heat03
Design: PorousFlowHeatEnergy PorousFlowHeatVolumetricExpansion PorousFlowEnergyTimeDerivative PorousFlowFullySaturatedHeatAdvection PorousFlowHeatAdvection PorousFlowHeatConduction PorousFlowPlasticHeatEnergy
Issue(s): #8123
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.12.6PorousFlow shall correctly conserve heat energy in a THM simulation when the model is squashed mechanically, in RZ coordinates
Specification(s): heat03_rz
Design: PorousFlowHeatEnergy PorousFlowHeatVolumetricExpansion PorousFlowEnergyTimeDerivative PorousFlowFullySaturatedHeatAdvection PorousFlowHeatAdvection PorousFlowHeatConduction PorousFlowPlasticHeatEnergy
Issue(s): #18324
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.12.7PorousFlow shall correctly calculate time-varying temperature, porepressure, stress and porosity in a model containing a source of heat energy
Specification(s): heat04
Design: PorousFlowHeatEnergy PorousFlowHeatVolumetricExpansion PorousFlowEnergyTimeDerivative PorousFlowFullySaturatedHeatAdvection PorousFlowHeatAdvection PorousFlowHeatConduction PorousFlowPlasticHeatEnergy
Issue(s): #8123
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.12.8PorousFlow shall correctly calculate time-varying temperature, porepressure, stress and porosity in a model containing a source of heat energy and fluid, in RZ coordinates
Specification(s): heat04_rz
Design: PorousFlowHeatEnergy PorousFlowHeatVolumetricExpansion PorousFlowEnergyTimeDerivative PorousFlowFullySaturatedHeatAdvection PorousFlowHeatAdvection PorousFlowHeatConduction PorousFlowPlasticHeatEnergy
Issue(s): #8123
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.12.9PorousFlow shall correctly calculate time-varying temperature, porepressure, stress and porosity in a model containing a source of heat energy, when using the PorousFlowUnsaturated Action
Specification(s): heat04_action
Design: PorousFlowHeatEnergy PorousFlowHeatVolumetricExpansion PorousFlowEnergyTimeDerivative PorousFlowFullySaturatedHeatAdvection PorousFlowHeatAdvection PorousFlowHeatConduction PorousFlowPlasticHeatEnergy
Issue(s): #18324
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.12.10PorousFlow shall correctly calculate time-varying temperature, porepressure, stress and porosity in a model containing a source of heat energy, when using the PorousFlowFullySaturated Action
Specification(s): heat04_fullysat_action
Design: PorousFlowHeatEnergy PorousFlowHeatVolumetricExpansion PorousFlowEnergyTimeDerivative PorousFlowFullySaturatedHeatAdvection PorousFlowHeatAdvection PorousFlowHeatConduction PorousFlowPlasticHeatEnergy
Issue(s): #8123
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.12.11PorousFlow shall correctly calculate time-varying temperature, porepressure, stress and porosity in a model containing a source of heat energy, when using the PorousFlowUnsaturated Action with Kuzmin-Turek stabilization
Specification(s): heat04_action_KT
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations PorousFlowHeatEnergy PorousFlowHeatVolumetricExpansion PorousFlowEnergyTimeDerivative PorousFlowFullySaturatedHeatAdvection PorousFlowHeatAdvection PorousFlowHeatConduction PorousFlowPlasticHeatEnergy
Issue(s): #8123 #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.12.9
31
16.12.12In fully-coupled THM situations, PorousFlow shall correctly initialize the porosity when it depends on all Variables
Specification(s): heat05
Design: PorousFlowHeatEnergy PorousFlowHeatVolumetricExpansion PorousFlowEnergyTimeDerivative PorousFlowFullySaturatedHeatAdvection PorousFlowHeatAdvection PorousFlowHeatConduction PorousFlowPlasticHeatEnergy
Issue(s): #8123
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Fluids
16.13.1PorousFlow shall be able to use high-precision equations of state for water from the FluidProperties module
Specification(s): h2o
Design: PorousFlowSingleComponentFluid
Issue(s): #11716
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.13.2PorousFlow shall be able to use high-precision equations of state for methane from the FluidProperties module
Specification(s): methane
Design: PorousFlowSingleComponentFluid
Issue(s): #11716
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.13.3PorousFlow shall be able to use equations of state for an ideal gas from the FluidProperties module
Specification(s): ideal_gas
Design: PorousFlowSingleComponentFluid
Issue(s): #11716
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.13.4PorousFlow shall be able to use high-precision equations of state for brine from the FluidProperties module
Specification(s): brine1
Design: PorousFlowBrine
Issue(s): #11716
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.13.5PorousFlow shall be able to use a given UserObject for water properties
Specification(s): brine1_tab
Design: PorousFlowBrine
Issue(s): #11716 #13882
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.13.4
31
16.13.6PorousFlow shall be able to use high-precision equations of state for CO2 from the FluidProperties module
Specification(s): co2
Design: PorousFlowSingleComponentFluid
Issue(s): #11716
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.13.7PorousFlow shall be able to use equations of state from the FluidProperties module for a single-component fluid and specify the temperature unit in Kelvin
Specification(s): simple_fluid
Design: PorousFlowSingleComponentFluid
Issue(s): #13154
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.13.8PorousFlow shall be able to use equations of state from the FluidProperties module for a single-component fluid and specify the pressure unit in MPa
Specification(s): simple_fluid_MPa
Design: PorousFlowSingleComponentFluid
Issue(s): #13154
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.13.9PorousFlow shall be able to use equations of state from the FluidProperties module for a single-component fluid and specify the time unit in days
Specification(s): simple_fluid_dy
Design: PorousFlowSingleComponentFluid
Issue(s): #13154
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.13.10PorousFlow shall be able to use equations of state from the FluidProperties module for a single-component fluid and specify the time unit in hours
Specification(s): simple_fluid_hr
Design: PorousFlowSingleComponentFluid
Issue(s): #13154
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.13.11PorousFlow shall be able to use equations of state from the FluidProperties module for a single-component fluid and specify the time unit in years
Specification(s): simple_fluid_yr
Design: PorousFlowSingleComponentFluid
Issue(s): #13154
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.13.12PorousFlow shall be able to use equations of state from the FluidProperties module for a single-component fluid and specify the time unit in years, the pressure unit in MPa and the temperature unit in Celsius
Specification(s): simple_fluid_yr_MPa_C
Design: PorousFlowSingleComponentFluid
Issue(s): #13154
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.13.13PorousFlow shall be able to use equations of state from the FluidProperties module for a single-component fluid and specify the time unit in years, the pressure unit in MPa and the temperature unit in Celsius, and this functionality shall be available through the PorousFlowActions
Specification(s): simple_fluid_yr_MPa_C_action
Design: PorousFlowSingleComponentFluid PorousFlowFullySaturated
Issue(s): #13154 #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.13.12
7

porous_flow: Fluidstate
16.14.1PorousFlow shall calculate the properties of the liquid phase in a water and NCG system
Specification(s): waterncg_liquid
Design: PorousFlowWaterNCG
Issue(s): #8818
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.14.2PorousFlow shall calculate the solubilities and properties of both the gas and liquid phase in a water and NCG system
Specification(s): waterncg_twophase
Design: PorousFlowWaterNCG
Issue(s): #8818
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.14.3PorousFlow shall calculate the properties of the gas phase in a water and NCG system
Specification(s): waterncg_gas
Design: PorousFlowWaterNCG
Issue(s): #8818
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.14.4PorousFlow shall evolve a gas phase as a gas component is added in a water and NCG system
Specification(s): theis
Design: PorousFlowWaterNCG
Issue(s): #8818
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.14.5PorousFlow shall evolve a gas phase as a gas component is added in a water and NCG system
Specification(s): theis_tabulated
Design: PorousFlowWaterNCG
Issue(s): #8818
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.14.6PorousFlow shall evolve a gas phase as a gas component is added in a nonisothermal water and NCG system
Specification(s): theis_nonisothermal
Design: PorousFlowWaterNCG
Issue(s): #8818 #10167
Collection(s): FUNCTIONAL
Type(s): CSVDiff
7
16.14.7PorousFlow shall calculate the solubilities and properties of both the gas and liquid phase in a brine and CO2 system
Specification(s): brineco2
Design: PorousFlowBrineCO2
Issue(s): #8818
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.14.8PorousFlow shall evolve a gas phase as CO2 is added to a liquid brine phase
Specification(s): brineco2_2
Design: PorousFlowBrineCO2
Issue(s): #8818
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.14.9PorousFlow shall evolve a gas phase as CO2 is added to a liquid brine phase in the high temperature regime
Specification(s): brineco2_hightemp
Design: PorousFlowBrineCO2
Issue(s): #8818 #11359
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.14.10PorousFlow shall evolve a gas phase as CO2 is added to a liquid brine phase
Specification(s): theis_brineco2
Design: PorousFlowBrineCO2
Issue(s): #8818
Collection(s): FUNCTIONAL
Type(s): CSVDiff
1
16.14.11PorousFlow shall evolve a gas phase as CO2 is added to a liquid brine phase in a nonisothermal model
Specification(s): theis_brineco2_nonisothermal
Design: PorousFlowBrineCO2
Issue(s): #8818 #10167
Collection(s): FUNCTIONAL
Type(s): CSVDiff
7
16.14.12PorousFlow shall calculate the initial value of total mass fraction corresponding to the specified gas saturation in a water and NCG system
Specification(s): waterncg_ic
Design: PorousFlowFluidStateWaterNCGIC
Issue(s): #9377
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.14.13PorousFlow shall calculate the initial value of total mass fraction corresponding to the specified gas saturation in a brine and CO2 system
Specification(s): brineco2_ic
Design: PorousFlowFluidStateBrineCO2IC
Issue(s): #9377
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.14.14PorousFlow shall calculate the properties of both the gas and liquid phase in a water-steam system
Specification(s): water_vapor_2phase
Design: PorousFlowWaterVapor
Issue(s): #13108
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.14.15PorousFlow shall calculate the liquid properties in a saturated liquid system
Specification(s): water_vapor_liquid
Design: PorousFlowWaterVapor
Issue(s): #13108
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.14.16PorousFlow shall calculate the gas properties in a saturated gas system
Specification(s): water_vapor_gas
Design: PorousFlowWaterVapor
Issue(s): #13108
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.14.17PorousFlow shall evolve a vapor phase as conditions enter the two phase region
Specification(s): water_vapor_phase_change
Design: PorousFlowWaterVapor
Issue(s): #13108
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.14.18PorousFlow shall calculate the temperature profile in a 1D Avdonin problem
Specification(s): geothermal_1d
Design: PorousFlowWaterVapor
Issue(s): #13108
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.14.19PorousFlow shall calculate the temperature profile in a 1D radial Avdonin problem
Specification(s): geothermal_1d_radial
Design: PorousFlowWaterVapor
Issue(s): #13108
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Flux Limited Tvd Advection
16.15.1PorousFlow shall implement Kuzmin-Turek stabilization, and shall error-out if the flux-limiting computations are not evaluated on linear
Specification(s): except_01
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.15.2PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries when there is no antidiffusion
Specification(s): jacobian_01
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
1
16.15.3PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries when the flux limiter is minmod
Specification(s): jacobian_02_minmod
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.15.4PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries when the flux limiter is vanleer
Specification(s): jacobian_02_vanleer
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.15.5PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries when the flux limiter is mc
Specification(s): jacobian_02_mc
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.15.6PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries when the flux limiter is superbee
Specification(s): jacobian_02_superbee
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.15.7PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries, for more than 1 thread
Specification(s): jacobian_02_vanleer_threads
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
Prerequisite(s): 16.15.4
26
16.15.8PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries when the flux limiter is vanleer, when the variable is such that the flux limiter is 1
Specification(s): jacobian_03_vanleer
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.15.9PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries when the flux limiter is mc, when the variable is such that the flux limiter is 1
Specification(s): jacobian_03_mc
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.15.10PorousFlow shall implement Kuzmin-Turek stabilization in 1D
Specification(s): fltvd_1D
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.15.11PorousFlow shall implement Kuzmin-Turek stabilization in 1D with more than 1 thread
Specification(s): fltvd_1D_threads
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.15.10
30
16.15.12PorousFlow shall implement Kuzmin-Turek stabilization in 2D
Specification(s): fltvd_2D
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.15.13PorousFlow shall implement Kuzmin-Turek stabilization in 2D with more than 1 thread
Specification(s): fltvd_2D_threads
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.15.11 16.15.12
30
16.15.14PorousFlow shall implement Kuzmin-Turek stabilization in 3D
Specification(s): fltvd_3D
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
1
16.15.15PorousFlow shall implement Kuzmin-Turek stabilization in 2D when the velocity is not aligned with the mesh
Specification(s): fltvd_2D_angle
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.15.16PorousFlow shall implement Kuzmin-Turek stabilization in 2D when using triangular mesh elements
Specification(s): fltvd_2D_trimesh
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
1
16.15.17PorousFlow shall implement Kuzmin-Turek stabilization in 2D when using triangular mesh elements and with more than 1 thread
Specification(s): fltvd_2D_trimesh_threads
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.15.16
1
16.15.18PorousFlow shall implement Kuzmin-Turek stabilization in 2D when the advection is block limited
Specification(s): fltvd_2D_blocks
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.15.19PorousFlow shall implement Kuzmin-Turek stabilization in 2D when the advection is block limited, and when more than 1 thread is used
Specification(s): fltvd_2D_blocks_threads
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.15.11 16.15.18
30
16.15.20PorousFlow shall implement Kuzmin-Turek stabilization in 1D when mesh adaptivity is used
Specification(s): fltvd_1D_adaptivity
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.15.21PorousFlow shall implement Kuzmin-Turek stabilization in 1D when mesh adaptivity is used, and when more than 1 thread is used
Specification(s): fltvd_1D_adaptivity_threads
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.15.11 16.15.20
30

porous_flow: Flux Limited Tvd Pflow
16.16.1PorousFlow shall error-out if the specified phase number >= number of phases in the model, when using Kuzmin-Turek stabilization
Specification(s): except01
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.16.2PorousFlow shall error-out if the specified fluid component number >= number of fluid components in the model, when using Kuzmin-Turek stabilization
Specification(s): except02
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.16.3PorousFlow shall error-out if the fe_family is specified but not fe_order, when using Kuzmin-Turek stabilization
Specification(s): except03
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.16.4PorousFlow error-out if the fe_order is specified but not fe_family, when using Kuzmin-Turek stabilization
Specification(s): except04
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.16.5PorousFlow shall error-out if the PorousFlowDictator cannot determine a consistent FE type to use and if no FE type is specified, when using Kuzmin-Turek stabilization
Specification(s): except05
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.16.6PorousFlow shall compute all Jacobian entries when there is no antidiffusion in Kuzmin-Turek stabilized PorousFlow simulations involving full saturation of 1 phase and 1 component
Specification(s): jacobian_01
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
1
16.16.7PorousFlow shall compute all Jacobian entries when there is no antidiffusion in Kuzmin-Turek stabilized PorousFlow simulations involving full saturation of 1 phase and 1 component, when using more than 1 thread
Specification(s): jacobian_01_threads
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
Prerequisite(s): 16.16.6
1
16.16.8PorousFlow shall compute all Jacobian entries when there is no antidiffusion in Kuzmin-Turek stabilized PorousFlow simulations involving 1 unsaturated fluid phase with multiple components
Specification(s): jacobian_02
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.16.9PorousFlow shall compute all Jacobian entries when there is no antidiffusion in Kuzmin-Turek stabilized PorousFlow simulations involving multiple fluid phases and multiple fluid components
Specification(s): jacobian_03
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
1
16.16.10PorousFlow shall compute all Jacobian entries when there is no antidiffusion in Kuzmin-Turek stabilized PorousFlow simulations involving multiple fluid phases and multiple fluid components, when using more than 1 thread
Specification(s): jacobian_03_threads
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
Prerequisite(s): 16.16.9
1
16.16.11PorousFlow shall compute all Jacobian entries when the flux limiter is minmod in Kuzmin-Turek stabilized PorousFlow simulations involving full saturation of 1 phase and 1 component
Specification(s): jacobian_04_minmod
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
1
16.16.12PorousFlow shall compute all Jacobian entries when the flux limiter is vanleer in Kuzmin-Turek stabilized PorousFlow simulations involving full saturation of 1 phase and 1 component
Specification(s): jacobian_04_vanleer
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
1
16.16.13PorousFlow shall compute all Jacobian entries when the flux limiter is mc in Kuzmin-Turek stabilized PorousFlow simulations involving full saturation of 1 phase and 1 component
Specification(s): jacobian_04_mc
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
1
16.16.14PorousFlow shall compute all Jacobian entries when the flux limiter is superbee in Kuzmin-Turek stabilized PorousFlow simulations involving full saturation of 1 phase and 1 component
Specification(s): jacobian_04_superbee
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
1
16.16.15PorousFlow shall compute all Jacobian entries when the flux limiter is vanleer in Kuzmin-Turek stabilized PorousFlow simulations involving full saturation of 1 phase and 1 component, when using more than 1 thread
Specification(s): jacobian_04_vanleer_threads
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
Prerequisite(s): 16.16.12
1
16.16.16PorousFlow shall compute all Jacobian entries when using any non-trivial flux limiter in Kuzmin-Turek stabilized PorousFlow simulations involving multiple phases and multiple components
Specification(s): jacobian_05
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.16.17PorousFlow shall compute all Jacobian entries when using any non-trivial flux limiter in Kuzmin-Turek stabilized PorousFlow simulations involving multiple phases and multiple components, when using more than 1 thread
Specification(s): jacobian_05_threads
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
Prerequisite(s): 16.16.16
26
16.16.18PorousFlow shall implement Kuzmin-Turek stabilization in 1D for PorousFlow simulations
Specification(s): pffltvd_1D
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.16.19PorousFlow shall implement Kuzmin-Turek stabilization in 1D for PorousFlow simulations, for more than 1 thread
Specification(s): pffltvd_1D_threads
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.16.18
30
16.16.20PorousFlow shall implement Kuzmin-Turek stabilization in 2D for PorousFlow simulations
Specification(s): pffltvd_2D
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.16.21PorousFlow shall implement Kuzmin-Turek stabilization in 2D for PorousFlow simulations, for more than 1 thread
Specification(s): pffltvd_2D_threads
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.16.19 16.16.20
30
16.16.22PorousFlow shall issue a warning if the memory is inefficiently used for multi-processor simulations involving Kuzmin-Turek stablization
Specification(s): memory_inefficiency
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #13078
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
Prerequisite(s): 16.16.19 16.16.20 16.16.21
30
16.16.23PorousFlow shall implement Kuzmin-Turek stabilization in 2D for PorousFlow simulations
Specification(s): pffltvd_3D
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
1
16.16.24PorousFlow shall implement Kuzmin-Turek stabilization in 2D for PorousFlow simulations, when the Darcy velocity is not aligned with the mesh
Specification(s): pffltvd_2D_angle
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.16.25PorousFlow shall implement Kuzmin-Turek stabilization in 2D for PorousFlow simulations, when using triangular mesh elements
Specification(s): pffltvd_2D_trimesh
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
1
16.16.26PorousFlow shall implement Kuzmin-Turek stabilization in 2D for PorousFlow simulations, when using triangular mesh elements, and more than 1 thread
Specification(s): pffltvd_2D_trimesh_threads
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.16.25
1
16.16.27PorousFlow shall implement Kuzmin-Turek stabilization in 1D for PorousFlow simulations when mesh adaptivity is used
Specification(s): pffltvd_1D_adaptivity
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Functions
16.17.1
Specification(s): mpf_except1
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.17.2
Specification(s): mpf1
Collection(s): FUNCTIONAL
Type(s): Exodiff
31

porous_flow: Gravity
16.18.1PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations
Specification(s): grav01a
Design: Governing equations Establishment of gravitational head in 1D
Issue(s): #6845 #7677 #8073 #8585 #8574 #9537
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.18.2PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations
Specification(s): grav01b
Design: Governing equations Establishment of gravitational head in 1D
Issue(s): #6845 #7677 #8073 #8585 #8574 #9537
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.18.3PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations
Specification(s): grav01c
Design: Governing equations Establishment of gravitational head in 1D
Issue(s): #6845 #7677 #8073 #8585 #8574 #9537
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.18.4PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations
Specification(s): grav01c_action
Design: Governing equations Establishment of gravitational head in 1D
Issue(s): #6845 #7677 #8073 #8585 #8574 #9537
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.18.5PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations
Specification(s): grav02a
Design: Governing equations Establishment of gravitational head in 1D
Issue(s): #6845 #7677 #8073 #8585 #8574 #9537
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.18.6PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations
Specification(s): grav02b
Design: Governing equations Establishment of gravitational head in 1D
Issue(s): #6845 #7677 #8073 #8585 #8574 #9537
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.18.7PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations
Specification(s): grav02c
Design: Governing equations Establishment of gravitational head in 1D
Issue(s): #6845 #7677 #8073 #8585 #8574 #9537
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.18.8PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations
Specification(s): grav02d
Design: Governing equations Establishment of gravitational head in 1D
Issue(s): #6845 #7677 #8073 #8585 #8574 #9537
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.18.9PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations
Specification(s): grav02e
Design: Governing equations Establishment of gravitational head in 1D
Issue(s): #6845 #7677 #8073 #8585 #8574 #9537
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.18.10PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations
Specification(s): grav02f
Design: Governing equations Establishment of gravitational head in 1D
Issue(s): #6845 #7677 #8073 #8585 #8574 #9537
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.18.11PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations
Specification(s): grav02g
Design: Governing equations Establishment of gravitational head in 1D
Issue(s): #6845 #7677 #8073 #8585 #8574 #9537
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.18.12PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations
Specification(s): fully_saturated_grav01a
Design: Governing equations Establishment of gravitational head in 1D
Issue(s): #6845 #7677 #8073 #8585 #8574 #9537
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.18.13PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations
Specification(s): fully_saturated_grav01b
Design: Governing equations Establishment of gravitational head in 1D
Issue(s): #6845 #7677 #8073 #8585 #8574 #9537
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.18.14PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations
Specification(s): fully_saturated_grav01c
Design: Governing equations Establishment of gravitational head in 1D
Issue(s): #6845 #7677 #8073 #8585 #8574 #9537 #12505
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.18.15PorousFlow shall be able to find steady-state porepressure for single-phase, fully-saturated, multicomponent systems
Specification(s): fully_saturated_upwinded_grav01c
Design: PorousFlowFullySaturatedAdvectiveFlux Establishment of gravitational head in 1D
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.18.16PorousFlow shall be able to find steady-state porepressure for single-phase, fully-saturated, multicomponent systems, if the Darcy flow is expressed in terms of fluid volumes
Specification(s): fully_saturated_upwinded_nodens_grav01c
Design: PorousFlowFullySaturatedAdvectiveFlux Establishment of gravitational head in 1D
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.18.15
31
16.18.17PorousFlow shall be able to find steady-state porepressure for single-phase, fully-saturated, multicomponent systems, when using an action
Specification(s): fully_saturated_upwinded_grav01c_action
Design: PorousFlowFullySaturated Establishment of gravitational head in 1D
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.18.16
31
16.18.18PorousFlow shall be able to find steady-state porepressure for single-phase, fully-saturated, multicomponent systems, when using an action and a fluid-volume calculation
Specification(s): fully_saturated_upwinded_nodens_grav01c_action
Design: PorousFlowFullySaturated Establishment of gravitational head in 1D
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.18.17
31
16.18.19PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero, when the simulation contains more than one domain, with each domain having its own capillary pressure and relative permeability function
Specification(s): grav01d
Design: Governing equations Establishment of gravitational head in 1D
Issue(s): #13116
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Heat Advection
16.19.1PorousFlow shall produce an error when the kernel describing heat advection by a single-phase fluid is used in a multi-phase situation
Specification(s): except1
Design: PorousFlowFullySaturatedUpwindHeatAdvection
Issue(s): #16841
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.19.2PorousFlow shall correctly advect heat energy with a moving fluid, using no numerical stabilization
Specification(s): heat_advection_1d_fully_saturated
Design: PorousFlowHeatAdvection PorousFlowEnergyTimeDerivative Heat advection in a 1D bar
Issue(s): #7984
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.19.3PorousFlow shall correctly advect heat energy with a moving fluid, using no numerical stabilization, and the user should be able to activiate this stabilization using the PorousFlow Action system
Specification(s): heat_advection_1d_fully_saturated_action_none
Design: PorousFlowFullySaturated Numerical diffusion Worked example of Kuzmin-Turek stabilization Heat advection in a 1D bar
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.19.2
31
16.19.4PorousFlow shall correctly advect heat energy with a moving fluid, using full-upwinding for numerical stabilization
Specification(s): heat_advection_1d
Design: PorousFlowHeatAdvection PorousFlowEnergyTimeDerivative Heat advection in a 1D bar
Issue(s): #7984
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.19.5PorousFlow shall correctly advect heat energy with a moving fluid, using full-upwinding for numerical stabilization, in fully-saturated single-phase systems
Specification(s): heat_advection_1d_fullsat
Design: PorousFlowFullySaturatedUpwindHeatAdvection PorousFlowEnergyTimeDerivative Heat advection in a 1D bar
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.19.4
31
16.19.6PorousFlow shall correctly advect heat energy with a moving fluid, using full-upwinding for numerical stabilization, in fully-saturated single-phase systems, and the user should be able to activiate this stabilization using the PorousFlow Action system
Specification(s): heat_advection_1d_fully_saturated_action_full
Design: PorousFlowFullySaturated PorousFlowEnergyTimeDerivative Heat advection in a 1D bar
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.19.5
31
16.19.7PorousFlow shall correctly advect heat energy with a moving fluid, using the Kuzmin-Turek for numerical stabilization
Specification(s): heat_advection_1d_KT
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization Heat advection in a 1D bar
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.19.8PorousFlow shall implement Kuzmin-Turek stabilization for PorousFlow simulations involving the advection of heat energy in a moving fluid, and the user should be able to activiate this stabilization using the PorousFlow Action system
Specification(s): heat_advection_1d_fully_saturated_action_KT
Design: PorousFlowFullySaturated Numerical diffusion Worked example of Kuzmin-Turek stabilization Heat advection in a 1D bar
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.19.7
31
16.19.9PorousFlow shall implement Kuzmin-Turek stabilization for PorousFlow simulations involving the advection of heat energy in a moving fluid
Specification(s): heat_advection_1d_KT_threads
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization Heat advection in a 1D bar
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
30

porous_flow: Heat Conduction
16.20.1PorousFlow shall be able to simulate heat conduction in a fluid-free environment
Specification(s): no_fluid
Design: Heat conduction tests descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.20.2PorousFlow shall be able to simulate heat conduction for systems containing multi-phase fluids
Specification(s): two_phase
Design: Heat conduction tests descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Heat Mass Transfer
16.21.1PorousFlow shall be able to transfer heat or mass from one Variable to another when the transfer coefficient is a constant.
Specification(s): testvariable_transfer_0D
Design: PorousFlowHeatMassTransfer
Issue(s): #11050
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.21.2PorousFlow shall be able to transfer heat or mass from one Variable to another when the transfer coefficient is a variable.
Specification(s): testvariable_transfer_variable_0D
Design: PorousFlowHeatMassTransfer
Issue(s): #11050
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Heterogeneous Materials
16.22.1The system shall allow the assignment of porosity and permeability from an AuxVariable field.
Specification(s): constant_poroperm
Design: PorousFlowPorosity
Issue(s): #8062
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.22.2The system shall allow the assignment of porosity and permeability from an AuxVariable field with binlinear relationships.
Specification(s): constant_poroperm2
Design: PorousFlowPorosity
Issue(s): #8062
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.22.3The system shall allow the assignment of porosity and permeability from an AuxVariable read from a mesh
Specification(s): constant_poroperm3
Design: PorousFlowPorosity
Issue(s): #13478
Collection(s): FUNCTIONAL
Type(s): Exodiff
Prerequisite(s): 16.22.2
31
16.22.4The system shall calculate permeability from a changing porosity.
Specification(s): vol_expansion_poroperm
Design: PorousFlowPorosity
Issue(s): #8062
Collection(s): FUNCTIONAL
Type(s): Exodiff
31

porous_flow: Hysteresis
16.23.1If the liquid phase number exceeds the number of phases in the system, PorousFlow shall produce an appropriate error message and exit
Specification(s): except01
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.2The maximum order for hysteretic relative permeabilities and capillary pressures is 3 and if the user specifies an initial order greater than this amount, an error shall be thrown
Specification(s): except02
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.3An error shall be thrown if the initial order of hysteresis is incommensurate with previous_turning_points
Specification(s): except03
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.4An error shall be thrown if the hysteretic turning points do not lie in the range [0, 1]
Specification(s): except04
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.5An error shall be thrown if the hysteretic turning points do not lie in the range [0, 1]
Specification(s): except05
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.6An error shall be thrown if the turning points are incorrectly ordered
Specification(s): except06
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.7An error shall be thrown if the turning points are incorrectly ordered
Specification(s): except07
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.8An error shall be thrown if the turning points are incorrectly ordered
Specification(s): except08
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.9An error shall be thrown if the hysteresis turning-point information is requested for the Nth turning point, when N exceeds the maximum number of turning points
Specification(s): except09
Design: PorousFlowHysteresisOrder PorousFlowPropertyAux
Issue(s): #16021
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.10An error shall be thrown if the maximum gas residual saturation is greater than 1 - minimum_liquid_saturation in hysteretic problems
Specification(s): except10
Design: Hysteresis in PorousFlow
Issue(s): #16129
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.11An error shall be thrown if parameters are chosen such that the high and low extension regions of the hysteretic capillary pressure overlap
Specification(s): except11
Design: Hysteresis in PorousFlow
Issue(s): #16129
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.12A warning shall be produced if the residual saturation is not greater than the minimum saturation in hysteretic simulations
Specification(s): except12
Design: Hysteresis in PorousFlow
Issue(s): #16129
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.13An exception shall be thrown if a single-phase hysteretic capillary-pressure Material is used in situations with more than one fluid phase
Specification(s): except13
Design: PorousFlow1PhaseHysP
Issue(s): #16129
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.14An exception shall be thrown if a two-phase PP hysteretic capillary-pressure Material is used in models that do not have exactly 2 phases
Specification(s): except14
Design: PorousFlow2PhaseHysPP
Issue(s): #16260
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.15An exception shall be thrown if a two-phase PS hysteretic capillary-pressure Material is used in models that do not have exactly 2 phases
Specification(s): except15
Design: PorousFlow2PhaseHysPS
Issue(s): #16260
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.16When using hysteretic relative permeabilities, an exception shall be thrown if the gas residual saturation is not less than 1 - liquid_residual_saturation
Specification(s): except16
Design: PorousFlowHystereticRelativePermeabilityLiquid PorousFlowHystereticRelativePermeabilityGas
Issue(s): #16324
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.23.17PorousFlow shall be able to calculate the hysteresis order
Specification(s): hys_order_01
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.18PorousFlow shall be able to calculate the hysteresis order
Specification(s): hys_order_02
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.19PorousFlow shall be able to calculate the hysteresis order
Specification(s): hys_order_03
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.20PorousFlow shall be able to calculate the hysteresis order and hysteresis order shall be able to be initialized to a nonzero value
Specification(s): hys_order_04
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.21PorousFlow shall be able to calculate the hysteresis order and hysteresis order shall be able to be initialized to a nonzero value
Specification(s): hys_order_05
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.22PorousFlow shall be able to calculate the hysteresis order and hysteresis order shall be able to be initialized to a nonzero value
Specification(s): hys_order_06
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.23PorousFlow shall be able to calculate the hysteresis order and hysteresis order shall be able to be initialized to a nonzero value
Specification(s): hys_order_07
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.24PorousFlow shall be able to calculate the hysteresis order and hysteresis order shall be able to be initialized to a nonzero value, and jumps of greater than 2 in hysteresis order shall be allowed within one time-step
Specification(s): hys_order_08
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.25PorousFlow shall be able to calculate the hysteresis order and hysteresis order shall be able to be initialized to a nonzero value, and jumps of greater than 2 in hysteresis order shall be allowed within one time-step, and turning points shall be correctly identified in such situations
Specification(s): hys_order_09
Design: PorousFlowHysteresisOrder
Issue(s): #16021
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.26PorousFlow shall be able to compute saturation according to the primary drying curve in hysteretic problems, using no low extension
Specification(s): hys_sat_01
Design: PorousFlow1PhaseHysP
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.27PorousFlow shall be able to compute saturation according to the primary drying curve in hysteretic problems, using quadratic low extension
Specification(s): hys_sat_02
Design: PorousFlow1PhaseHysP
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.28PorousFlow shall be able to compute saturation according to the primary drying curve in hysteretic problems, using exponential low extension
Specification(s): hys_sat_03
Design: PorousFlow1PhaseHysP
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.29PorousFlow shall be able to compute capillary pressure according to the primary drying curve in hysteretic problems, using no low extension
Specification(s): hys_pc_01
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.30PorousFlow shall be able to compute capillary pressure according to the primary drying curve in hysteretic problems, using quadratic low extension
Specification(s): hys_pc_02
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.31PorousFlow shall be able to compute capillary pressure according to the primary drying curve in hysteretic problems, using exponential low extension
Specification(s): hys_pc_03
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.32PorousFlow shall be able to compute capillary pressure according to the primary wetting curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_pc_1_w_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.33PorousFlow shall be able to compute capillary pressure according to the primary wetting curve in hysteretic problems, using no low extension and power high extension
Specification(s): hys_pc_1_w_none_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.34PorousFlow shall be able to compute capillary pressure according to the primary wetting curve in hysteretic problems, using quadratic low extension and no high extension
Specification(s): hys_pc_1_w_quadratic_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.35PorousFlow shall be able to compute capillary pressure according to the primary wetting curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_pc_1_w_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.36PorousFlow shall be able to compute capillary pressure according to the primary wetting curve in hysteretic problems, using exponential low extension and no high extension
Specification(s): hys_pc_1_w_exponential_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.37PorousFlow shall be able to compute capillary pressure according to the primary wetting curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_pc_1_w_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.38PorousFlow shall be able to compute capillary pressure according to the first-order wetting curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_pc_1_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.39PorousFlow shall be able to compute capillary pressure according to the first-order wetting curve in hysteretic problems, using no low extension and power high extension
Specification(s): hys_pc_1_none_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.40PorousFlow shall be able to compute capillary pressure according to the first-order wetting curve in hysteretic problems, using quadratic low extension and no high extension
Specification(s): hys_pc_1_quadratic_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.41PorousFlow shall be able to compute capillary pressure according to the first-order wetting curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_pc_1_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.42PorousFlow shall be able to compute capillary pressure according to the first-order wetting curve in hysteretic problems, using exponential low extension and no high extension
Specification(s): hys_pc_1_exponential_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.43PorousFlow shall be able to compute capillary pressure according to the first-order wetting curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_pc_1_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.44PorousFlow shall be able to compute capillary pressure according to the second-order drying curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_pc_2_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.45PorousFlow shall be able to compute capillary pressure according to the second-order drying curve in hysteretic problems, using no low extension and power high extension
Specification(s): hys_pc_2_none_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.46PorousFlow shall be able to compute capillary pressure according to the second-order drying curve in hysteretic problems, using quadratic low extension and no high extension
Specification(s): hys_pc_2_quadratic_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.47PorousFlow shall be able to compute capillary pressure according to the second-order drying curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_pc_2_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.48PorousFlow shall be able to compute capillary pressure according to the second-order drying curve in hysteretic problems, using exponential low extension and no high extension
Specification(s): hys_pc_2_exponential_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.49PorousFlow shall be able to compute capillary pressure according to the second-order drying curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_pc_2_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.50PorousFlow shall be able to compute capillary pressure according to the third-order wetting curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_pc_3_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.51PorousFlow shall be able to compute capillary pressure according to the third-order wetting curve in hysteretic problems, using no low extension and power high extension
Specification(s): hys_pc_3_none_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.52PorousFlow shall be able to compute capillary pressure according to the third-order wetting curve in hysteretic problems, using quadratic low extension and no high extension
Specification(s): hys_pc_3_quadratic_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.53PorousFlow shall be able to compute capillary pressure according to the third-order wetting curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_pc_3_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.54PorousFlow shall be able to compute capillary pressure according to the third-order wetting curve in hysteretic problems, using exponential low extension and no high extension
Specification(s): hys_pc_3_exponential_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.55PorousFlow shall be able to compute capillary pressure according to the third-order wetting curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_pc_3_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.56PorousFlow shall be able to compute saturation from capillary pressure according to the primary drying curve in hysteretic problems, using no low extension
Specification(s): hys_sat_prim_01
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.57PorousFlow shall be able to compute saturation from capillary pressure according to the primary drying curve in hysteretic problems, using quadratic low extension
Specification(s): hys_sat_prim_02
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.58PorousFlow shall be able to compute saturation from capillary pressure according to the primary drying curve in hysteretic problems, using exponential low extension
Specification(s): hys_sat_prim_03
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.59PorousFlow shall be able to compute liquid saturation according to the primary wetting curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_sat_1_w_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.60PorousFlow shall be able to compute liquid saturation according to the primary wetting curve in hysteretic problems, using no low extension and power high extension
Specification(s): hys_sat_1_w_none_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.61PorousFlow shall be able to compute liquid saturation according to the primary wetting curve in hysteretic problems, using quadratic low extension and no high extension
Specification(s): hys_sat_1_w_quadratic_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.62PorousFlow shall be able to compute liquid saturation according to the primary wetting curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_sat_1_w_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.63PorousFlow shall be able to compute liquid saturation according to the primary wetting curve in hysteretic problems, using exponential low extension and no high extension
Specification(s): hys_sat_1_w_exponential_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.64PorousFlow shall be able to compute liquid saturation according to the primary wetting curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_sat_1_w_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.65PorousFlow shall be able to compute liquid saturation according to the second-order drying curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_sat_2_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.66PorousFlow shall be able to compute liquid saturation according to the second-order drying curve in hysteretic problems, using no low extension and power high extension
Specification(s): hys_sat_2_none_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.67PorousFlow shall be able to compute liquid saturation according to the second-order drying curve in hysteretic problems, using quadratic low extension and no high extension
Specification(s): hys_sat_2_quadratic_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.68PorousFlow shall be able to compute liquid saturation according to the second-order drying curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_sat_2_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.69PorousFlow shall be able to compute liquid saturation according to the second-order drying curve in hysteretic problems, using exponential low extension and no high extension
Specification(s): hys_sat_2_exponential_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.70PorousFlow shall be able to compute liquid saturation according to the second-order drying curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_sat_2_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.71PorousFlow shall be able to compute liquid saturation according to the third-order wetting curve in hysteretic problems, using no low extension and power high extension
Specification(s): hys_sat_3_none_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.72PorousFlow shall be able to compute liquid saturation according to the third-order wetting curve in hysteretic problems, using quadratic low extension and no high extension
Specification(s): hys_sat_3_quadratic_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.73PorousFlow shall be able to compute liquid saturation according to the third-order wetting curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_sat_3_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.74PorousFlow shall be able to compute liquid saturation according to the third-order wetting curve in hysteretic problems, using exponential low extension and no high extension
Specification(s): hys_sat_3_exponential_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.75PorousFlow shall be able to compute liquid saturation according to the third-order wetting curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_sat_3_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.76PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along to the primary drying curve in hysteretic problems, using no low extension
Specification(s): hys_dpc_prim_01
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.77PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along to the primary drying curve in hysteretic problems, using quadratic low extension
Specification(s): hys_dpc_prim_02
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.78PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along to the primary drying curve in hysteretic problems, using exponential low extension
Specification(s): hys_dpc_prim_03
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.79PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along the first-order wetting curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_dpc_1_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.80PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along the first-order wetting curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_dpc_1_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.81PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along the first-order wetting curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_dpc_1_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.82PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along the second-order drying curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_dpc_2_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.83PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along the second-order drying curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_dpc_2_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.84PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along the second-order drying curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_dpc_2_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.85PorousFlow shall be able to compute the derivative of the capillary pressure with respect to the liquid saturation along the third-order wetting curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_dpc_3_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.86PorousFlow shall be able to compute the derivative of the capillary pressure with respect to the liquid saturation along the third-order wetting curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_dpc_3_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.87PorousFlow shall be able to compute the derivative of the capillary pressure with respect to the liquid saturation along the third-order wetting curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_dpc_3_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.88PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along to the primary drying curve in hysteretic problems, using no low extension
Specification(s): hys_d2pc_prim_01
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.89PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along to the primary drying curve in hysteretic problems, using quadratic low extension
Specification(s): hys_d2pc_prim_02
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.90PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along to the primary drying curve in hysteretic problems, using exponential low extension
Specification(s): hys_d2pc_prim_03
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.91PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along the first-order wetting curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_d2pc_1_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.92PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along the first-order wetting curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_d2pc_1_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.93PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along the first-order wetting curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_d2pc_1_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.94PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along the second-order drying curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_d2pc_2_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.95PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along the second-order drying curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_d2pc_2_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.96PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along the second-order drying curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_d2pc_2_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.97PorousFlow shall be able to compute the second derivative of the capillary pressure with respect to the liquid saturation along the third-order wetting curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_d2pc_3_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.98PorousFlow shall be able to compute the second derivative of the capillary pressure with respect to the liquid saturation along the third-order wetting curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_d2pc_3_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.99PorousFlow shall be able to compute the second derivative of the capillary pressure with respect to the liquid saturation along the third-order wetting curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_d2pc_3_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.100PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along to the primary drying curve in hysteretic problems, using no low extension
Specification(s): hys_dsat_prim_01
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.101PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along to the primary drying curve in hysteretic problems, using quadratic low extension
Specification(s): hys_dsat_prim_02
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.102PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along to the primary drying curve in hysteretic problems, using exponential low extension
Specification(s): hys_dsat_prim_03
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.103PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along the first-order wetting curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_dsat_1_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.104PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along the first-order wetting curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_dsat_1_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.105PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along the first-order wetting curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_dsat_1_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.106PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along the second-order drying curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_dsat_2_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.107PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along the second-order drying curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_dsat_2_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.108PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along the second-order drying curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_dsat_2_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.109PorousFlow shall be able to compute the derivative of the liquid saturation with respect to capillary pressure along the third-order wetting curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_dsat_3_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.110PorousFlow shall be able to compute the derivative of the liquid saturation with respect to capillary pressure along the third-order wetting curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_dsat_3_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.111PorousFlow shall be able to compute the derivative of the liquid saturation with respect to capillary pressure along the third-order wetting curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_dsat_3_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.112PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along to the primary drying curve in hysteretic problems, using no low extension
Specification(s): hys_d2sat_prim_01
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.113PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along to the primary drying curve in hysteretic problems, using quadratic low extension
Specification(s): hys_d2sat_prim_02
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.114PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along to the primary drying curve in hysteretic problems, using exponential low extension
Specification(s): hys_d2sat_prim_03
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.115PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along the first-order wetting curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_d2sat_1_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.116PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along the first-order wetting curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_d2sat_1_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.117PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along the first-order wetting curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_d2sat_1_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.118PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along the second-order drying curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_d2sat_2_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.119PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along the second-order drying curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_d2sat_2_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.120PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along the second-order drying curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_d2sat_2_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.121PorousFlow shall be able to compute the second derivative of the liquid saturation with respect to capillary pressure along the third-order wetting curve in hysteretic problems, using no low extension and no high extension
Specification(s): hys_d2sat_3_none_none
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.122PorousFlow shall be able to compute the second derivative of the liquid saturation with respect to capillary pressure along the third-order wetting curve in hysteretic problems, using quadratic low extension and power high extension
Specification(s): hys_d2sat_3_quadratic_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.123PorousFlow shall be able to compute the second derivative of the liquid saturation with respect to capillary pressure along the third-order wetting curve in hysteretic problems, using exponential low extension and power high extension
Specification(s): hys_d2sat_3_exponential_power
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.124PorousFlow shall be able to compute capillary pressure as a function of saturation in hysteretic time-dependent problems, along the primary drying curve
Specification(s): vary_sat_1a
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.125PorousFlow shall be able to compute capillary pressure as a function of saturation in hysteretic time-dependent problems, along the primary drying curve and then the primary wetting curve
Specification(s): vary_sat_1b
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.126PorousFlow shall be able to compute capillary pressure as a function of saturation in hysteretic time-dependent problems, along the primary drying curve and then the first-order wetting
Specification(s): vary_sat_1c
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.127PorousFlow shall be able to compute capillary pressure as a function of saturation in hysteretic time-dependent problems, along the primary drying curve, then first-order wetting, and then second-order drying
Specification(s): vary_sat_1d
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.128PorousFlow shall be able to compute capillary pressure as a function of saturation in hysteretic time-dependent problems, along the primary drying curve, then first-order wetting, and then second-order drying, and then third-order
Specification(s): vary_sat_1e
Design: PorousFlowHystereticInfo
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.129PorousFlow shall be able to compute saturation in 1-phase hysteretic systems, as the system evolves in time along the primary drying curve and then along a first-order wetting curve
Specification(s): 1phase
Design: PorousFlow1PhaseHysP
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.130PorousFlow shall be able to compute saturation in 1-phase hysteretic systems, as the system evolves in time along the primary drying curve and then along first, second and third order curves
Specification(s): 1phase_3rd
Design: PorousFlow1PhaseHysP
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.131PorousFlow shall be able to compute the full Jacobian entries in 2-phase hysteretic systems when using a PP formulation
Specification(s): 2phasePP_jacobian
Design: PorousFlow2PhaseHysPP
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.23.132PorousFlow shall be able to compute saturations and porepressures in 2-phase hysteretic systems when using a PP formulation, as the system evolves in time along the primary drying curve and then along a first-order curve
Specification(s): 2phasePP_1
Design: PorousFlow2PhaseHysPP
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.133PorousFlow shall be able to compute saturations and porepressures in 2-phase hysteretic systems when using a PP formulation, as the system evolves in time along the primary drying curve and then along a first-order curve and then along a second-order drying curve until it meets the primary drying curve
Specification(s): 2phasePP_2
Design: PorousFlow2PhaseHysPP
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.134PorousFlow shall be able to compute the full Jacobian entries in 2-phase hysteretic systems when using a PS formulation
Specification(s): 2phasePS_jacobian
Design: PorousFlow2PhaseHysPS
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.23.135PorousFlow shall be able to compute saturations and porepressures in 2-phase hysteretic systems when using a PS formulation, as the system evolves in time along the primary drying curve and then along a first-order curve
Specification(s): 2phasePS_1
Design: PorousFlow2PhaseHysPS
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.136PorousFlow shall be able to compute saturations and porepressures in 2-phase hysteretic systems when using a PS formulation, as the system evolves in time along the primary drying curve and then along a first-order curve and then along a second-order drying curve until it meets the primary drying curve
Specification(s): 2phasePS_2
Design: PorousFlow2PhaseHysPS
Issue(s): #16129
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.137PorousFlow shall be able to compute hysteretic relative permeability in 1-phase systems as the system evolves in time along the primary drying curve and then along a first-order wetting curve
Specification(s): 1phase_relperm
Design: PorousFlowHystereticRelativePermeabilityLiquid
Issue(s): #16324
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.138PorousFlow shall be able to compute hysteretic relative permeability in 1-phase systems as the saturation cycles between high and low values, including going below the residual saturation
Specification(s): 1phase_relperm_2
Design: PorousFlowHystereticRelativePermeabilityLiquid
Issue(s): #16324
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.139PorousFlow shall be able to compute hysteretic liquid and gas relative permeabilities in 2-phase systems as the system evolves in time along the primary drying curve and then along first-order wetting curves
Specification(s): 2phasePS_relperm
Design: PorousFlowHystereticRelativePermeabilityLiquid PorousFlowHystereticRelativePermeabilityGas
Issue(s): #16324
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.140PorousFlow shall be able to compute hysteretic liquid and gas relative permeabilities in 2-phase systems as the system dries and then re-wets, and the gas relative permeability is extended to low saturations using a linear-like extension
Specification(s): 2phasePS_relperm_2_linear_like
Design: PorousFlowHystereticRelativePermeabilityLiquid PorousFlowHystereticRelativePermeabilityGas
Issue(s): #16324
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.141PorousFlow shall be able to compute hysteretic liquid and gas relative permeabilities in 2-phase systems as the system dries and then re-wets, and the gas relative permeability is extended to low saturations using a cubic extension
Specification(s): 2phasePS_relperm_2_cubic
Design: PorousFlowHystereticRelativePermeabilityLiquid PorousFlowHystereticRelativePermeabilityGas
Issue(s): #16324
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.142PorousFlow shall be able to compute hysteretic liquid and gas relative permeabilities in 2-phase systems as the system dries and then re-wets, and the gas relative permeability is extended to low saturations by assuming is is unity
Specification(s): 2phasePS_relperm_2_none
Design: PorousFlowHystereticRelativePermeabilityLiquid PorousFlowHystereticRelativePermeabilityGas
Issue(s): #16324
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.23.143PorousFlow shall be able to compute the full Jacobian entries when using hysteretic relative permeabilities, as the system evolves along a zeroth order curve
Specification(s): relperm_jac
Design: PorousFlowHystereticRelativePermeabilityLiquid PorousFlowHystereticRelativePermeabilityGas
Issue(s): #16324
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.23.144PorousFlow shall be able to compute the full Jacobian entries when using hysteretic relative permeabilities, as the system evolves along a first-order curve
Specification(s): relperm_jac_1
Design: PorousFlowHystereticRelativePermeabilityLiquid PorousFlowHystereticRelativePermeabilityGas
Issue(s): #16324
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26

porous_flow: Ics
16.24.1PorousFlow shall calculate an initial condition for a fluid property given pressure and temperature
Specification(s): fluidpropic
Design: PorousFlowFluidPropertyIC
Issue(s): #13108
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.24.2PorousFlow shall calculate an initial condition for a fluid property given pressure and temperature (in C)
Specification(s): fluidpropic_celsius
Design: PorousFlowFluidPropertyIC
Issue(s): #13108
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.24.1
31

porous_flow: Infiltration And Drainage
16.25.1PorousFlow shall be able to model 2-phase infiltration and agree with the analytic solution
Specification(s): bw01
Design: Infiltration and drainage test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): Exodiff
1
16.25.2PorousFlow shall be able to model 2-phase infiltration on a coarse mesh and agree with the analytic solution
Specification(s): bw02
Design: Infiltration and drainage test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.25.3PorousFlow shall be able to model 2-phase drainage and agree with the analytic solution
Specification(s): wli01
Design: Infiltration and drainage test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): Exodiff
1
16.25.4PorousFlow shall be able to model 2-phase drainage on a coarse mesh and agree with the analytic solution
Specification(s): wli02
Design: Infiltration and drainage test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.25.5PorousFlow shall be able to model single-phase infiltration and agree with the analytic solution
Specification(s): rd01
Design: Infiltration and drainage test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): Exodiff
1
16.25.6PorousFlow shall be able to model single-phase short-term drainage and agree with the analytic solution
Specification(s): rd02
Design: Infiltration and drainage test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): Exodiff
1
16.25.7PorousFlow shall be able to model single-phase long-term drainage and agree with the analytic solution
Specification(s): rd03
Design: Infiltration and drainage test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.25.8PorousFlow shall be able to model water infiltration into a 2-phase and agree with the analytic solution
Specification(s): rsc01
Design: Infiltration and drainage test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): Exodiff
1
16.25.9PorousFlow shall be able to model water infiltration into a 2-phase and agree with the analytic solution in a high-resolution test
Specification(s): rsc02
Design: Infiltration and drainage test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): Exodiff
31

porous_flow: Jacobian
16.26.1PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1phase, constant-bulk density, constant porosity, 1-component, fully saturated
Specification(s): mass01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.2PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1phase, constant-bulk density, constant porosity, 1-component, fully saturated, in a volume approach
Specification(s): mass01_nodens
Design: PorousFlowMassTimeDerivative Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.3PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1phase, constant-bulk density, constant porosity, 1-component, unsaturated
Specification(s): mass02
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.4PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1phase, constant-bulk density, constant porosity, multi-component, unsaturated
Specification(s): mass03
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.5PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 2-phase, constant-bulk density, constant porosity, 2-component
Specification(s): mass04
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.6PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 2-phase, constant-bulk density, constant porosity, multi-component
Specification(s): mass05
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.7PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 2-phase, constant-bulk density, constant porosity, multi-component, in a volume formulation
Specification(s): mass05_nodens
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.8PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1-phase, constant-bulk density, constant porosity, 1-component, in a log(mass-density) formulation
Specification(s): mass06
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.9PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1-phase, constant-bulk density, constant porosity, 1-component, in a log(mass-density), volumetric formulation
Specification(s): mass07
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.10PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1-phase, constant-bulk density, HMporosity, 1-component, unsaturated
Specification(s): mass08
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.11PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 2-phase, constant-bulk density, 2-component, PS-formulation
Specification(s): mass09
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.12PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1-phase, constant-bulk density, HM-porosity, 1-component, unsaturated
Specification(s): mass10
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.13PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1-phase, constant-bulk density, HM-porosity, 1-component, unsaturated, with a volumetric formulation
Specification(s): mass10_nodens
Design: PorousFlowMassTimeDerivative Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.14PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1-phase, with a fully-saturated formulation
Specification(s): mass01_fully_saturated
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.15PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 1-component, unsaturated, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability
Specification(s): fflux01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.16PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 3-component, unsaturated, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability
Specification(s): fflux02
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.17PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 2-phase, 2-component, PS formulation, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability
Specification(s): fflux03
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.18PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 2-phase, 3-component, PP formulation, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability
Specification(s): fflux04
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.19PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, log-mass-density formulation, fully-saturated, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability
Specification(s): fflux05
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.20PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, log-mass-density formulation, unsaturated, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability
Specification(s): fflux06
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.21PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 2-phase, 2-component with components in both phases, PS formulation, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability
Specification(s): fflux07
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.22PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 1-component, constant viscosity, Kozeny-Carman permeability, constant fluid-bulk modulus, Corey-relative permeability
Specification(s): fflux08
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.23PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 2-phase, 3-component, PP formulation, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability, with RSC capilarity
Specification(s): fflux09
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.24PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 3-component, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability, with BW capilarity
Specification(s): fflux10
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.25PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 3-component, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability, with VG capilarity with a cubic extension
Specification(s): fflux11
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.26PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 3-component, constant viscosity, constant permeability, constant fluid-bulk modulus, FLAC-relative permeability
Specification(s): fflux12
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.27PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 2-phase, 3-component, PP-formulation, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability, with a harmonic-mean mobility
Specification(s): fflux13
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.28PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 3-components, constant viscosity, constant permeability, constant fluid-bulk modulus, fully-saturated formulation
Specification(s): fflux01_fully_saturated
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.29PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 3-components, constant viscosity, constant permeability, constant fluid-bulk modulus, fully-saturated formulation with strong advection
Specification(s): fflux02_fully_saturated
Design: PorousFlowFullySaturated PorousFlowFullySaturatedAdvectiveFlux Nonlinear convergence problems PorousFlowDictator
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.30PorousFlow shall compute all Jacobian entries of Kernels for the effective stress, with 2-phase, 2-component, PP formulation
Specification(s): eff_stress01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.31PorousFlow shall compute all Jacobian entries of Kernels for the effective stress, with 2-phase, 2-component, PS formulation
Specification(s): eff_stress02
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.32PorousFlow shall compute all Jacobian entries of Kernels for the effective stress, with 2-phase, 2-component, PP formulation, in RZ coordinates
Specification(s): eff_stress03
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.33PorousFlow shall compute all Jacobian entries of Kernels for the effective stress, with 2-phase, 2-component, PS formulation, in RZ coordinates
Specification(s): eff_stress04
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845 #12506
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.34PorousFlow shall compute all Jacobian entries of Kernels for the mass volumetric expansion, with constant bulk modulus, constant porosity and VG capilarity
Specification(s): mass_vol_exp01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.35PorousFlow shall compute all Jacobian entries of Kernels for the mass volumetric expansion, with constant bulk modulus, HM porosity and VG capilarity
Specification(s): mass_vol_exp02
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.36PorousFlow shall compute all Jacobian entries of Kernels for the mass volumetric expansion, with constant bulk modulus, HM porosity and VG capilarity, in a volumetric formulation
Specification(s): mass_vol_exp03
Design: PorousFlowMassVolumetricExpansion Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.37PorousFlow shall compute all Jacobian entries of Kernels for the piecewise linear sink, with 1-phase and 1-component
Specification(s): pls01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.38PorousFlow shall compute all Jacobian entries of Kernels for the piecewise linear sink, with 2-phase and 2-components
Specification(s): pls02
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.39PorousFlow shall compute all Jacobian entries of Kernels for the piecewise linear sink, with 2-phase and 3-components
Specification(s): pls03
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.40PorousFlow shall compute all Jacobian entries of Kernels for the piecewise linear sink, with 2-phase and 3-components, with enthalpy, internal energy and thermal conductivity
Specification(s): pls04
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.41PorousFlow shall compute all Jacobian entries of Kernels for the half-gaussian sink
Specification(s): hgs01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.42PorousFlow shall compute all Jacobian entries of Kernels for the half-cubic sink of fluid
Specification(s): hcs01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.43PorousFlow shall compute all Jacobian entries of Kernels for the half-cubic sink of heat
Specification(s): hcs02
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.44PorousFlow shall compute all Jacobian entries of Kernels for the heat conduction, with 0 phases
Specification(s): hcond01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.45PorousFlow shall compute all Jacobian entries of Kernels for the heat conduction, with 2 phases
Specification(s): hcond02
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.46PorousFlow shall compute all Jacobian entries of Kernels for the energy-density time derivative, with 0 phases
Specification(s): denergy01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.47PorousFlow shall compute all Jacobian entries of Kernels for the energy-density time derivative, with 2-phase, 1-component, with solid displacements
Specification(s): denergy02
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.48PorousFlow shall compute all Jacobian entries of Kernels for the energy-density time derivative, with 2-phase, 1-component, with solid displacements, and TM porosity
Specification(s): denergy03
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.49PorousFlow shall compute all Jacobian entries of Kernels for the energy-density time derivative, with 2-phase, 1-component, with solid displacements, and THM porosity
Specification(s): denergy04
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.50PorousFlow shall compute all Jacobian entries of Kernels for the energy-density time derivative, with 2-phase, 1-component, with solid displacements, and THM porosity, compressive strains and ensuring porosity remains positivie
Specification(s): denergy05
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.51PorousFlow shall compute all Jacobian entries of Kernels for the heat advection, with 1 phase, unsaturated
Specification(s): heat_advection01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.52PorousFlow shall compute all Jacobian entries of Kernels for the heat advection, with 2 phase, unsaturated
Specification(s): heat_advection02
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.53PorousFlow shall compute all Jacobian entries of Kernels for the heat advection, with 1 phase, fully-saturated formulation
Specification(s): heat_advection01_fully_saturated
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.54PorousFlow shall compute all Jacobian entries of Kernels for the heat advection, with 1 phase, fully-saturated, fully-upwinded formulation
Specification(s): heat_advection01_fullsat_upwind
Design: PorousFlowFullySaturatedUpwindHeatAdvection Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.55PorousFlow shall compute all Jacobian entries of Kernels for the diffusion
Specification(s): diff01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.56PorousFlow shall compute all Jacobian entries of Kernels for the diffusion with constant tortuousity and diffusivity
Specification(s): diff02
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.57PorousFlow shall compute all Jacobian entries of Kernels for the diffusion with 2-phases, with saturation-dependent tortuousity and MQ diffusion coefficients
Specification(s): diff03
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.58PorousFlow shall compute all Jacobian entries of Kernels for the transverse dispersion
Specification(s): disp01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.59PorousFlow shall compute all Jacobian entries of Kernels for the transverse dispersion and diffusion
Specification(s): disp02
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.60PorousFlow shall compute all Jacobian entries of Kernels for the transverse and longitudinal dispersion
Specification(s): disp03
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.61PorousFlow shall compute all Jacobian entries of Kernels for the transverse and longitudinal dispersion and diffusion
Specification(s): disp04
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.62PorousFlow shall compute all Jacobian entries of Kernels for the heat volumetric expansion, 1phase with constant bulk modulus, VG capilarity and THM porosity
Specification(s): heat_vol_exp01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.63PorousFlow shall compute all Jacobian entries of Kernels for the plastic heat energy
Specification(s): phe01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
50
16.26.64PorousFlow shall compute all Jacobian entries of Kernels for the a peaceman line sink, with 2-phase, 3-components, with enthalpy, internal energy and thermal conductivity
Specification(s): line_sink01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.65PorousFlow shall compute all Jacobian entries of Kernels for the a poly-line sink, with 2-phase, 3-components, with enthalpy, internal energy and thermal conductivity
Specification(s): line_sink02
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.66PorousFlow shall compute all Jacobian entries of Kernels for the a peaceman sink, with 2-phase, 3-components, with enthalpy, internal energy and thermal conductivity, and with many points within each element
Specification(s): line_sink03
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845 #10471 #16255
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.67PorousFlow shall compute all Jacobian entries of Kernels for the a peaceman sink, with 2-phase, 3-components, with enthalpy, internal energy and thermal conductivity, and with 5 points within each element
Specification(s): line_sink01_5
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.68PorousFlow shall compute all Jacobian entries of Kernels for the a poly-line sink, with 2-phase, 3-components, with enthalpy, internal energy and thermal conductivity, and with 5 points within each element
Specification(s): line_sink02_5
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.69PorousFlow shall compute all Jacobian entries of Kernels for the a poly-line sink, with 2-phase, 3-components, with enthalpy, internal energy and thermal conductivity, and with 1 point within each element
Specification(s): line_sink04
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845 #10471
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.70PorousFlow shall compute all Jacobian entries of Kernels for the desorbed mass
Specification(s): desorped_mass01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.71PorousFlow shall compute all Jacobian entries of Kernels for the volumetric expansion of desorbed mass
Specification(s): desorped_mass_vol_exp01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.72PorousFlow shall compute all Jacobian entries of Kernels for the non-condensible gas version of water, 2 phase
Specification(s): waterncg_twophase
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.73PorousFlow shall compute all Jacobian entries of Kernels for the non-condensible gas version of water, 1 liquid phase
Specification(s): waterncg_liqiud
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.74PorousFlow shall compute all Jacobian entries of Kernels for the non-condensible gas version of water, 1 gas phase
Specification(s): waterncg_gas
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.75PorousFlow shall compute all Jacobian entries of Kernels for the non-condensible gas version of water, 2 phase, nonisothermal
Specification(s): waterncg_twophase_nonisothermal
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845 #10167
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.76PorousFlow shall compute all Jacobian entries of Kernels for the brine equation of state, 2 phase
Specification(s): brineco2_twophase
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.77PorousFlow shall compute all Jacobian entries of Kernels for the brine equation of state, 1 liquid phase
Specification(s): brineco2_liquid
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.78PorousFlow shall compute all Jacobian entries of Kernels for the brine equation of state, 1 gas phase
Specification(s): brineco2_gas
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.79PorousFlow shall compute all Jacobian entries of Kernels for the brine equation of state, 2 phase, nonisothermal
Specification(s): brineco2_twophase_nonisothermal
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845 #10167
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.80PorousFlow shall compute all Jacobian entries of Kernels for the brine equation of state, 1 phase with salt fraction as a variable
Specification(s): brineco2_liquid_2
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.81PorousFlow shall compute all Jacobian entries of Kernels for the exponential decay
Specification(s): exponential_decay
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.82PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissoluation not depending on temperature
Specification(s): chem01
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.83PorousFlow shall compute all Jacobian entries of Kernels for the chemical precipitation not depending on temperature
Specification(s): chem02
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.84PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution depending on temperature
Specification(s): chem03
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.85PorousFlow shall compute all Jacobian entries of Kernels for the chemical precipitation not depending on temperature
Specification(s): chem04
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.86PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution not depending on temperature where one concentration is initialized to zero, and the stoichiometry is > 1
Specification(s): chem05
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.87PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution not depending on temperature where one concentration is initialized to zero, and the stoichiometry is = 1
Specification(s): chem06
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.88PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution not depending on temperature where the concentrations are initialized to zero
Specification(s): chem07
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.89PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution depending on temperature where one concentration is initialized to zero, and the stoichiometry is > 1
Specification(s): chem08
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.90PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution depending on temperature where one concentration is initialized to zero, and the stoichiometry is = 1
Specification(s): chem09
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.91PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution depending on temperature where concentrations are initialized to zero
Specification(s): chem10
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.92PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution depending on temperature with 3 primary variables and 4 reactions
Specification(s): chem11
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.93PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution depending on temperature with 3 primary variables and 4 reactions, with negative initial concentrations
Specification(s): chem12
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.94PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution depending on temperature with 3 primary variables and 4 reactions, with some zero initial concentrations
Specification(s): chem13
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.95PorousFlow shall compute all Jacobian entries of Kernels for the porosity depending on chemical concentrations
Specification(s): chem14
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.96PorousFlow shall compute all Jacobian entries of Kernels for the mass-fractions that depend on chemical concentrations
Specification(s): chem15
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.97PorousFlow shall compute all Jacobian entries of Kernels for the basic advection with a pre-defined velocity vector, in the 0-phase, no temperature case
Specification(s): basic_advection1
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.98PorousFlow shall compute all Jacobian entries of Kernels for the basic advection with a Darcy velocity vector in the fully-saturated, constant permeability, constant viscosity case
Specification(s): basic_advection2
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.99PorousFlow shall compute all Jacobian entries of Kernels for the basic advection with a Darcy velocity vector in the unsaturated, constant permeability, constant viscosity case
Specification(s): basic_advection3
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.100PorousFlow shall compute all Jacobian entries of Kernels for the basic advection with a Darcy velocity vector in the unsaturated, non-isothermal, constant permeability, constant viscosity case
Specification(s): basic_advection4
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.101PorousFlow shall compute all Jacobian entries of Kernels for the basic advection with a Darcy velocity vector in the unsaturated case
Specification(s): basic_advection5
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.102PorousFlow shall compute all Jacobian entries of Kernels for the basic advection with a Darcy velocity vector in the 2-phase PP case
Specification(s): basic_advection6
Design: Porous Flow Tutorial Page 09. An overview of the PorousFlow architecture Porous Flow Tutorial Page 02. Numerical issues Preconditioners and linear solvers Nonlinear convergence problems PorousFlowDictator
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.103PorousFlow shall compute all Jacobian entries of Kernels for the enthalpy sink, where porepressure is specified
Specification(s): esbc01
Design: PorousFlowEnthalpySink
Issue(s): #15742
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.104PorousFlow shall compute all Jacobian entries of Kernels for the enthalpy sink, where external pressure is specified
Specification(s): esbc02
Design: PorousFlowEnthalpySink
Issue(s): #15742
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.105PorousFlow shall compute all Jacobian entries of Kernels for the enthalpy source
Specification(s): hfrompps
Design: PorousFlowPointEnthalpySourceFromPostprocessor
Issue(s): #15742
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.106PorousFlow shall compute all Jacobian entries of Kernels for the outflow boundary condition, 1-phase, 1-component
Specification(s): outflowbc01
Design: Sinks test descriptions Boundary conditions PorousFlowOutflowBC
Issue(s): #18037
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.107PorousFlow shall compute all Jacobian entries of Kernels for the outflow heat boundary condition, 1-phase, 1-component
Specification(s): outflowbc02
Design: Sinks test descriptions Boundary conditions PorousFlowOutflowBC
Issue(s): #18037
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.108PorousFlow shall compute all Jacobian entries of Kernels for the outflow fluid and heat boundary conditions, 1-phase, multi-component
Specification(s): outflowbc03
Design: Sinks test descriptions Boundary conditions PorousFlowOutflowBC
Issue(s): #18037
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.109PorousFlow shall compute all Jacobian entries of Kernels for the outflow fluid boundary conditions, multi-phase, multi-component
Specification(s): outflowbc04
Design: Sinks test descriptions Boundary conditions PorousFlowOutflowBC
Issue(s): #18037
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26
16.26.110PorousFlow shall be able to calculate the analytic Jacobian of systems that include a porosity that is a linear function of effective porepressure, temperature and volumetric strain
Specification(s): linear_por
Design: Porosity PorousFlowPorosityLinear
Issue(s): #18079
Collection(s): FUNCTIONAL
Type(s): PetscJacobianTester
26

porous_flow: Mass Conservation
16.27.1PorousFlow shall correctly compuate the total fluid mass in a single-phase, single-component fluid
Specification(s): mass01
Design: Mass computation and conservation PorousFlowFluidMass
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.27.2PorousFlow shall correctly compuate the total fluid masses in a single-phase, multi-component fluid
Specification(s): mass02
Design: Mass computation and conservation PorousFlowFluidMass
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.27.3PorousFlow shall correctly compuate the evolution of fluid mass when there is a source of fluid
Specification(s): mass03
Design: Mass computation and conservation PorousFlowFluidMass
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.27.4PorousFlow shall conserve mass in a material with impermeable boundaries that is compressed mechanically
Specification(s): mass04
Design: Mass computation and conservation PorousFlowFluidMass
Issue(s): #13155 #18324
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.27.5PorousFlow shall correctly compuate the total fluid masses in a multi-phase, multi-component fluid
Specification(s): mass05
Design: Mass computation and conservation PorousFlowFluidMass
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.27.6PorousFlow shall correctly compuate the component and phase fluid masses in a multi-phase, multi-component fluid, at all saturations, and above a saturation threshold
Specification(s): mass06
Design: Mass computation and conservation PorousFlowFluidMass
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.27.7If the phase number exceeds the number of phases in the system, PorousFlow shall produce an appropriate error message and exit
Specification(s): mass07
Design: Mass computation and conservation PorousFlowFluidMass
Issue(s): #13155
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.27.8If the phase index exceeds the number of phases in the system, PorousFlow shall produce an appropriate error message and exit
Specification(s): mass08
Design: Mass computation and conservation PorousFlowFluidMass
Issue(s): #13155
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.27.9If a saturation threshold is used in computing the fluid mass, and a phase index is not provided, PorousFlow shall produce an appropriate error message and exit
Specification(s): mass09
Design: Mass computation and conservation PorousFlowFluidMass
Issue(s): #13155
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.27.10If the user enters a PorousFlow variable number that is not less than the number of PorousFlow variables, PorousFlow shall produce an appropriate error message and exit
Specification(s): mass10
Design: Mass computation and conservation PorousFlowFluidMass
Issue(s): #13155
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.27.11PorousFlow shall conserve mass in a material with impermeable boundaries that is allowed to expand mechanically while being injected with fluid
Specification(s): mass11
Design: Mass computation and conservation PorousFlowFluidMass
Issue(s): #18324
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.27.12PorousFlow shall conserve mass in an annular material with impermeable boundaries that is compressed verticaly
Specification(s): mass12
Design: Mass computation and conservation PorousFlowFluidMass
Issue(s): #18324
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.27.13PorousFlow shall conserve mass in an annular material with impermeable boundaries that is compressed radially
Specification(s): mass13
Design: Mass computation and conservation PorousFlowFluidMass
Issue(s): #18324
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Newton Cooling
16.28.1PorousFlow shall be able to model transient newton cooling acting on the fluid mass and agree with the analytic solution
Specification(s): nc01
Design: Heat and fluid responses in 1D bars
Issue(s): #13155 #16953
Collection(s): FUNCTIONAL
Type(s): CSVDiff
2
16.28.2PorousFlow shall be able to model steady-state newton cooling acting on the fluid mass and agree with the analytic solution
Specification(s): nc02
Design: Heat and fluid responses in 1D bars
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
58
16.28.3PorousFlow shall be able to model steady-state newton cooling acting on the temperature and agree with the analytic solution
Specification(s): nc04
Design: Heat and fluid responses in 1D bars
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.28.4PorousFlow shall be able to model newton cooling acting on the porepressure and at the same time extracting heat along with the extracted fluid and agree with the analytic solution
Specification(s): nc06
Design: Heat and fluid responses in 1D bars
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.28.5PorousFlow shall be able to model newton cooling acting on the porepressure of an ideal gas and at the same time extracting heat along with the extracted gas and agree with the analytic solution
Specification(s): nc08
Design: Heat and fluid responses in 1D bars
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Numerical Diffusion
16.29.1The system shall be able to solve the advection equation
Specification(s): framework
Design: Numerical diffusion
Issue(s): #12346
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.29.2PorousFlow shall be able to solve the advection of fluid species, using mass lumping and no upwinding, employing an Action
Specification(s): fully_saturated_action
Design: Numerical diffusion
Issue(s): #11013
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.29.3PorousFlow shall be able to solve the advection of fluid species, using mass lumping and full upwinding, without employing an action
Specification(s): no_action
Design: Numerical diffusion
Issue(s): #11013
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.29.4PorousFlow shall be able to solve the advection of fluid species in a fully-saturated single-phase situation, using mass lumping and full upwinding, via employing an action
Specification(s): fully_saturated_upwinded
Design: Numerical diffusion
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.29.3
31
16.29.5PorousFlow shall be able to solve the advection of fluid species in a fully-saturated single-phase situation, using mass lumping and KT upwinding, via employing an action
Specification(s): fully_saturated_KT
Design: Numerical diffusion
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
1
16.29.6PorousFlow shall implement Kuzmin-Turek stabilization, but be able to use no antidiffusion
Specification(s): fltvd_no_antidiffusion
Design: Numerical diffusion
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.29.7PorousFlow shall implement Kuzmin-Turek stabilization
Specification(s): fltvd
Design: Numerical diffusion
Issue(s): #12370 #12118 #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.29.8PorousFlow shall implement Kuzmin-Turek stabilization for PorousFlow simulations. The advection via the Darcy velocity shall have the correct velocity. With no flux-limiter the results should be the same as full upwinding. The results for simulations involving PorousFlow Kernels and UserObjects when the Darcy velocity is constant shall be the same as the constant-velocity, non-PorousFlow case.
Specification(s): pffltvd
Design: Numerical diffusion How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
1
16.29.9PorousFlow shall implement Kuzmin-Turek stabilization for PorousFlow simulations and the user shall be able to use the PorousFlow Action system to choose the Kuzmin-Turek stabilization for single-phase, multi-component fluid flow
Specification(s): pffltvd_action
Design: Numerical diffusion How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.29.8
1

porous_flow: Plastic Heating
16.30.1PorousFlow shall model heat generated from plastic deformation, including tensile failure
Specification(s): tensile01
Design: Heat energy produced by plastic deformation PorousFlowPlasticHeatEnergy
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.30.2PorousFlow shall model heat generated from plastic deformation, including compressive failure
Specification(s): compressive01
Design: Heat energy produced by plastic deformation PorousFlowPlasticHeatEnergy
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.30.3PorousFlow shall model heat generated from plastic deformation, including shear failure
Specification(s): shear01
Design: Heat energy produced by plastic deformation PorousFlowPlasticHeatEnergy
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Poro Elasticity
16.31.1PorousFlow shall be able to model standard poroelasticity in the situation where increasing porepressure leads to volumetric expansion
Specification(s): vol_expansion
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.31.2PorousFlow shall be able to model standard poroelasticity and be able to simulate an undrained oedometer test
Specification(s): undrained_oedometer
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.3PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-constrained solid
Specification(s): pp_generation
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.4PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-constrained solid, using PorousFlow Actions
Specification(s): pp_generation_action
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.5PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-constrained solid, using a fully-saturated formulation
Specification(s): pp_generation_fullysat_action
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.6PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-unconstrained solid
Specification(s): pp_generation_unconfined
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.7PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-unconstrained solid, using a constant Biot modulus
Specification(s): pp_generation_unconfined_constM
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.8PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-unconstrained solid, using a constant Biot modulus, and be able to simulate this using an Action
Specification(s): pp_generation_unconfined_constM_action
Design: PorousFlowFullySaturated Poroelasticity test descriptions
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.31.7
31
16.31.9PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-unconstrained solid, using a fully-saturated formulation
Specification(s): pp_generation_unconfined_fully_saturated
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.10PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-unconstrained solid, using a fully-saturated formulation, based on fluid volumes instead of fluid masses
Specification(s): pp_generation_unconfined_fully_saturated_volume
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.11PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-unconstrained solid, using a Actions
Specification(s): pp_generation_unconfined_basicthm
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.12PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Mandel consolidation of a drained medium
Specification(s): mandel
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.13PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Mandel consolidation of a drained medium, using a constant Biot modulus
Specification(s): mandel_constM
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.14PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Mandel consolidation of a drained medium, using a fully-saturated formalism
Specification(s): mandel_fully_saturated
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.15PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Mandel consolidation of a drained medium, using a fully-saturated formalism based on fluid volume instaed of the usual fluid mass
Specification(s): mandel_fully_saturated_volume
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.16PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Mandel consolidation of a drained medium, using Actions
Specification(s): mandel_basicthm
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.17PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Terzaghi consolidation of a drained medium
Specification(s): terzaghi
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.18PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Terzaghi consolidation of a drained medium, using a constant Biot modulus
Specification(s): terzaghi_constM
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.19PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Terzaghi consolidation of a drained medium, using a fully-saturated formalism
Specification(s): terzaghi_fully_saturated_volume
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.20PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Terzaghi consolidation of a drained medium, using Actions
Specification(s): terzaghi_basicthm
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.31.21PorousFlow shall be able to model standard poroelasticity and be able to calculate porosity and permeability increases in an unconfined sample where porepressure is increased
Specification(s): vol_expansion_poroperm
Design: Poroelasticity test descriptions
Issue(s): #13155
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Poroperm
16.32.1PorousFlow shall be able to calculate permeability as a Kozeny-Carman function of porosity, where permeability is defined via setting a grain size
Specification(s): PermFromPoro01
Design: Permeability PorousFlowPermeabilityKozenyCarman
Issue(s): #7632
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.32.2PorousFlow shall be able to calculate permeability as a Kozeny-Carman function of porosity, where permeability is defined via setting a reference value of porosity
Specification(s): PermFromPoro02
Design: Permeability PorousFlowPermeabilityKozenyCarman
Issue(s): #7632
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.32.3PorousFlow shall be able to calculate permeability as an exponential function of porosity, where an anisotropy is specified, and k is defined through an exponential function
Specification(s): PermFromPoro03
Design: Permeability PorousFlowPermeabilityExponential
Issue(s): #7632
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.32.4PorousFlow shall be able to calculate permeability as an exponential function of porosity, where an anisotropy is specified, and log(k) is defined through a linear function
Specification(s): PermFromPoro04
Design: Permeability PorousFlowPermeabilityExponential
Issue(s): #7632
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.32.5PorousFlow shall be able to calculate permeability as an exponential function of porosity, where an anisotropy is specified, and ln(k) is defined through a linear function
Specification(s): PermFromPoro05
Design: Permeability PorousFlowPermeabilityExponential
Issue(s): #7632
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.32.6PorousFlow shall be able to calculate porosity for thermo-hydro-mechanical coupled models
Specification(s): poro_thm
Design: Porosity PorousFlowPorosity
Issue(s): #10847
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.32.7PorousFlow shall be able to calculate porosity for thermo-mechanical coupled models
Specification(s): poro_tm
Design: Porosity PorousFlowPorosity
Issue(s): #10847
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.32.8PorousFlow shall be able to calculate porosity for hydro-mechanical coupled models
Specification(s): poro_hm
Design: Porosity PorousFlowPorosity
Issue(s): #10847
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.32.9PorousFlow shall produce an error if the porosity depends on temperature but no thermal expansion coefficient is provided
Specification(s): except1
Design: Porosity PorousFlowPorosity
Issue(s): #10847
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.32.10PorousFlow shall produce an error if the porosity depends on porepressure but no solid bulk modulus is provided
Specification(s): except2
Design: Porosity PorousFlowPorosity
Issue(s): #10847
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.32.11PorousFlow shall be able to calculate permeability as a product of an anisotropic tensor and a constant term
Specification(s): PermTensorFromVar01
Design: Permeability PorousFlowPermeabilityConstFromVar
Issue(s): #8061
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.32.12PorousFlow shall be able to calculate permeability as a product of an anisotropic tensor and a spatially-varying variable
Specification(s): PermTensorFromVar02
Design: Permeability PorousFlowPermeabilityConstFromVar
Issue(s): #8061
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.32.13PorousFlow shall be able to calculate isotropic, spatially-varying permeability
Specification(s): PermTensorFromVar03
Design: Permeability PorousFlowPermeabilityConstFromVar
Issue(s): #8061
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.32.14PorousFlow shall produce an error if a linear porosity relationship that depends on effective fluid pressure is used if there is no effective fluid pressure material
Specification(s): linear_except1
Design: Porosity PorousFlowPorosityLinear
Issue(s): #18079
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.32.15PorousFlow shall produce an error if a linear porosity relationship that depends on temperature is used if there is no temperature material
Specification(s): linear_except2
Design: Porosity PorousFlowPorosityLinear
Issue(s): #18079
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.32.16PorousFlow shall produce an error if a linear porosity relationship that depends on volumetric strain is used if there is no volumetric-strain material
Specification(s): linear_except3
Design: Porosity PorousFlowPorosityLinear
Issue(s): #18079
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.32.17PorousFlow shall be able to calculate porosity as a linear function of effective porepressure, temperature and volumetric strain
Specification(s): linear_test_vals1
Design: Porosity PorousFlowPorosityLinear
Issue(s): #18079
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.32.18PorousFlow shall be able to calculate porosity as a linear function of effective porepressure, temperature and volumetric strain and place a lower bound on the resulting porosity
Specification(s): linear_test_vals2
Design: Porosity PorousFlowPorosityLinear
Issue(s): #18079
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.32.17
31

porous_flow: Pressure Pulse
16.33.1PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D using 1 phase physics
Specification(s): pressure_pulse_1d
Design: Pressure-pulses in 1D
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.33.2PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D using 1 phase physics, and be able to employ the Action system in such settings
Specification(s): pressure_pulse_1d_action
Design: PorousFlowFullySaturated Pressure-pulses in 1D
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.33.1
31
16.33.3PorousFlow shall find the steady-state distribution resulting from a pressure pulse in 1D using 1 phase physics
Specification(s): pressure_pulse_1d_steady
Design: Pressure-pulses in 1D
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.33.4PorousFlow shall find the steady-state distribution resulting from a pressure pulse in 1D using 1 phase physics, and be able to employ the Action system in such settings
Specification(s): pressure_pulse_1d_steady_action
Design: PorousFlowFullySaturated Pressure-pulses in 1D
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.33.3
31
16.33.5PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D using 1 fluid phase with multiple components
Specification(s): pressure_pulse_1d_3comp
Design: Pressure-pulses in 1D
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.33.6PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D using 1 fluid phase with multiple components, and be able to employ the Action system in such simulations
Specification(s): pressure_pulse_1d_3comp_action
Design: Pressure-pulses in 1D
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.33.5
31
16.33.7PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 2 fluid phases, with 2 immiscible components, when one phase has zero saturation
Specification(s): pressure_pulse_1d_2phase
Design: Pressure-pulses in 1D
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.33.8PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 2 fluid phases, with 2 immiscible components, with constant capillary pressure
Specification(s): pressure_pulse_1d_2phasePS
Design: Pressure-pulses in 1D
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.33.9PorousFlow shall implement Kuzmin-Turek stabilization for multi-phase, multi-component PorousFlow simulations, and illustrate this through the transient evolution of a pressure pulse
Specification(s): pressure_pulse_1d_2phasePS_KT
Design: Numerical diffusion Worked example of Kuzmin-Turek stabilization How to use Kuzmin-Turek stabilization in PorousFlow simulations
Issue(s): #10426
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.33.10PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 2 fluid phases, with 2 immiscible components, with van-Genuchten capillary pressure
Specification(s): pressure_pulse_1d_2phasePSVG
Design: Pressure-pulses in 1D
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.33.11PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 2 fluid phases, with 2 immiscible components, with van-Genuchten capillary pressure and a logarithmic extension
Specification(s): pressure_pulse_1d_2phasePSVG2
Design: Pressure-pulses in 1D
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.33.12PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 1 fluid phase in the MD formulation where the primary variable is log(mass-density)
Specification(s): pressure_pulse_1d_MD
Design: Pressure-pulses in 1D
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.33.13PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 1 fluid phase and employing the fully-saturated version of Darcy flow
Specification(s): pressure_pulse_1d_fully_saturated
Design: Pressure-pulses in 1D
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.33.14PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 1 fluid phase with 3 components and employing the fully-saturated version of Darcy flow
Specification(s): pressure_pulse_1d_3comp_fully_saturated
Design: Pressure-pulses in 1D
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.33.15PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 1 fluid phase and employing the fully-saturated version of Darcy flow along with the fully-saturated version of the fluid-mass time derivative
Specification(s): pressure_pulse_1d_fully_saturated_2
Design: Pressure-pulses in 1D
Issue(s): #6845
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.33.16PorousFlow shall correctly simulate the transient evolution of a pressure pulse when mesh adaptivity is included
Specification(s): pressure_pulse_1d_adapt
Design: Pressure-pulses in 1D
Issue(s): #6845 #14035
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.33.17PorousFlow shall be able to advect tracers in fully-saturated single-phase systems, using a fluid-volume conservation approach, and be able to use full-upwinding in such settings
Specification(s): pressure_pulse_1d_2comp_nodens_full
Design: PorousFlowFullySaturated Pressure-pulses in 1D
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.33.18PorousFlow shall be able to advect tracers in fully-saturated single-phase systems, using a fluid-volume conservation approach, and be able to use no upwinding in such settings
Specification(s): pressure_pulse_1d_2comp_nodens_none
Design: PorousFlowFullySaturated Pressure-pulses in 1D
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.33.19PorousFlow shall be able to advect tracers in fully-saturated single-phase systems, using a fluid-volume conservation approach, and be able to use KT stabilization in such settings
Specification(s): pressure_pulse_1d_2comp_nodens_KT
Design: PorousFlowFullySaturated Pressure-pulses in 1D
Issue(s): #16841
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Radioactive Decay
16.34.1
Specification(s): radioactive_deacy01
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.34.2
Specification(s): exponential_decay
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Recover
16.35.1PorousFlow shall be able to recover from a checkpoint save
Specification(s): theis_full
Design: Restarting and recovering from previous simulations
Issue(s): #12927
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.35.2PorousFlow shall be able to recover from a checkpoint save
Specification(s): theis_part1
Design: Restarting and recovering from previous simulations
Issue(s): #12927
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.35.1
31
16.35.3PorousFlow shall be able to recover from a checkpoint save
Specification(s): theis_recover
Design: Restarting and recovering from previous simulations
Issue(s): #12927
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.35.2
31
16.35.4PorousFlow shall be able to recover from a checkpoint save
Specification(s): pffltvd_full
Design: Restarting and recovering from previous simulations
Issue(s): #12927
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.35.5PorousFlow shall be able to recover from a checkpoint save
Specification(s): pffltvd_part1
Design: Restarting and recovering from previous simulations
Issue(s): #12927
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.35.4
31
16.35.6PorousFlow shall be able to recover from a checkpoint save
Specification(s): pffltvd_recover
Design: Restarting and recovering from previous simulations
Issue(s): #12927
Collection(s): FUNCTIONAL
Type(s): CSVDiff
Prerequisite(s): 16.35.5
31

porous_flow: Relperm
16.36.1
Specification(s): unity
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.36.2
Specification(s): corey1
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.36.3
Specification(s): corey2
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.36.4
Specification(s): corey3
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.36.5
Specification(s): corey4
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.36.6
Specification(s): vangenuchten1
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.36.7
Specification(s): vangenuchten2
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.36.8
Specification(s): brookscorey1
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.36.9
Specification(s): brookscorey2
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Sinks
16.37.1PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow
Specification(s): s01
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): CSVDiff
58
16.37.2PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow, when the source/sink strength is multiplied by the mobility
Specification(s): s02
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): CSVDiff
60
16.37.3PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, unsaturated flow, when the source/sink strength is multiplied by the relative permeability
Specification(s): s03
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): CSVDiff
58
16.37.4PorousFlow shall be able to model source/sink boundary condition for single-phase, single-component flow, when the boundary flux is a piecewise-linear function of porepressure
Specification(s): s04
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): CSVDiff
58
16.37.5PorousFlow shall be able to model source/sink boundary condition for single-phase, single-component flow, when the boundary flux is a half-gaussian function of porepressure
Specification(s): s05
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): CSVDiff
60
16.37.6PorousFlow shall be able to model source/sink boundary condition for single-phase, single-component flow, when the boundary flux is a half-cubic function of porepressure
Specification(s): s06
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.37.7PorousFlow shall be able to model a source/sink boundary condition for single-phase, multi-component, fully-saturated flow
Specification(s): s07
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.37.8PorousFlow shall be able to model a source/sink boundary condition for multi-phase, multi-component flow
Specification(s): s08
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.37.9PorousFlow shall be able to model a source/sink boundary condition that holds porepressures fixed and extracts fluid components from boundaries at a rate prescribed by the flow within the model at the boundary - viz, the sink should behave like a free boundary
Specification(s): s09
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.37.10PorousFlow shall be able to model a source/sink boundary condition that holds porepressures fixed and extracts fluid components from boundaries at a rate prescribed by the flow within the model at the boundary - viz, the sink should behave like a free boundary, and this feature shall be compatible with the fully-saturated formalism within PorousFlow
Specification(s): s09_fully_saturated
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.37.11PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow, and the source/sink shall remove fluid from the correct node in a mesh: the left-side nodes in this case
Specification(s): s10_left
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.37.12PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow, and the source/sink shall remove fluid from the correct node in a mesh: the right-side nodes in this case
Specification(s): s10_right
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.37.13PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow, and the source/sink shall remove fluid from the correct node in a mesh: the top-side nodes in this case
Specification(s): s10_top
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.37.14PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow, and the source/sink shall remove fluid from the correct node in a mesh: the bottom-side nodes in this case
Specification(s): s10_bottom
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.37.15PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow, and the source/sink shall remove fluid from the correct node in a mesh: the front-side nodes in this case
Specification(s): s10_front
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.37.16PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow, and the source/sink shall remove fluid from the correct node in a mesh: the back-side nodes in this case
Specification(s): s10_back
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.37.17PorousFlow shall be able to inject fluid at user specified temperature.
Specification(s): s11
Design: PorousFlowEnthalpySink
Issue(s): #15742
Collection(s): FUNCTIONAL
Type(s): Exodiff
31
16.37.18PorousFlow shall be able to setup fluid injection at user specified temperature using a simplified syntax.
Specification(s): s11_act
Design: PorousFlowEnthalpySink PorousFlowSinkBC
Issue(s): #15742
Collection(s): FUNCTIONAL
Type(s): Exodiff
Prerequisite(s): 16.37.17
31
16.37.19PorousFlow shall report an error when incorrect number of variables is used when using a simplified enthalpy sink BC syntax.
Specification(s): s11_act_too_many_vars
Design: PorousFlowEnthalpySink PorousFlowSinkBC
Issue(s): #15742
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.37.20PorousFlow shall report an error when more than 2 porepressure variables are specified when using a simplified BC syntax.
Specification(s): s11_act_too_many_pressure_vars
Design: PorousFlowEnthalpySink PorousFlowSinkBC
Issue(s): #15742
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.37.21PorousFlow shall report an error when both external and pore pressures are specified.
Specification(s): s11_overspecified_pressure
Design: PorousFlowEnthalpySink PorousFlowSinkBC
Issue(s): #15742
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.37.22PorousFlow shall report an error when neither external and pore pressures are specified.
Specification(s): s11_underspecified_pressure
Design: PorousFlowEnthalpySink PorousFlowSinkBC
Issue(s): #15742
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.37.23PorousFlow shall report an error when incorrect fluid phase is specified in a BC for injecting fluid at user specified temperature.
Specification(s): s11_incorrect_fluid_phase
Design: PorousFlowEnthalpySink PorousFlowSinkBC
Issue(s): #15742
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.37.24PorousFlow shall be able to inject fluid at user specified pressure and temperature.
Specification(s): s12
Design: PorousFlowEnthalpySink
Issue(s): #15742
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.37.25PorousFlow shall be able to model a free boundary condition for multi-phase, multi-component fluids, and a clear example showing how this is possible shall be given
Specification(s): injection_production_eg
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #7333
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.37.26PorousFlow shall be able to model a source/sink boundary condition, and a clear example showing how these boundary conditions can be used to fix porepressures shall be given
Specification(s): PorousFlowPiecewiseLinearSink_BC_eg1
Design: Sinks test descriptions Boundary conditions Point and line sources/sinks
Issue(s): #12769
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.37.27PorousFlow shall report an error for an incorrect mass-fraction specification in PorousFlowOutflowBC
Specification(s): outflow_except1
Design: Sinks test descriptions Boundary conditions PorousFlowOutflowBC
Issue(s): #18037
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.37.28PorousFlow shall report an error if there is no nodal density Material when using PorousFlowOutflowBC
Specification(s): outflow_except2_dens
Design: Sinks test descriptions Boundary conditions PorousFlowOutflowBC
Issue(s): #18037
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.37.29PorousFlow shall report an error if there is no nodal relative-permeability Material when using PorousFlowOutflowBC
Specification(s): outflow_except2_relperm
Design: Sinks test descriptions Boundary conditions PorousFlowOutflowBC
Issue(s): #18037
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.37.30PorousFlow shall report an error if there is no nodal mass-fraction Material when using PorousFlowOutflowBC
Specification(s): outflow_except2_massfrac
Design: Sinks test descriptions Boundary conditions PorousFlowOutflowBC
Issue(s): #18037
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.37.31PorousFlow shall report an error if there is no thermal conductivity Material when using PorousFlowOutflowBC
Specification(s): outflow_except2_thermal_cond
Design: Sinks test descriptions Boundary conditions PorousFlowOutflowBC
Issue(s): #18037
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.37.32PorousFlow shall report an error if there is no enthalpy Material when using PorousFlowOutflowBC
Specification(s): outflow_except2_enthalpy
Design: Sinks test descriptions Boundary conditions PorousFlowOutflowBC
Issue(s): #18037
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.37.33PorousFlow shall report an error if there is no temperature Material when using PorousFlowOutflowBC
Specification(s): outflow_except2_T
Design: Sinks test descriptions Boundary conditions PorousFlowOutflowBC
Issue(s): #18037
Collection(s): FAILURE_ANALYSISFUNCTIONAL
Type(s): RunException
31
16.37.34PorousFlow shall be able to model an outflow boundary condition in single-phase, fully-saturated, multi-component cases
Specification(s): s13
Design: Sinks test descriptions Boundary conditions PorousFlowOutflowBC
Issue(s): #18037
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.37.35PorousFlow shall be able to model an outflow boundary condition in single-phase, fully-saturated, single-component case and record the total mass outflow
Specification(s): s14
Design: Sinks test descriptions Boundary conditions PorousFlowOutflowBC
Issue(s): #18037
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.37.36PorousFlow shall be able to model a heat-energy outflow boundary condition in single-phase, fully-saturated, single-component case and record the total heat-energy outflow
Specification(s): s15
Design: Sinks test descriptions Boundary conditions PorousFlowOutflowBC
Issue(s): #18037
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.37.37PorousFlow shall be able to model a free, outflow boundary condition for multi-phase, multi-component fluids
Specification(s): injection_production_eg_outflowBC
Design: Sinks test descriptions Boundary conditions PorousFlowOutflowBC
Issue(s): #18037
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Thermal Conductivity
16.38.1
Specification(s): ThermalCondPorosity01
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

porous_flow: Thm Rehbinder
16.39.1
Specification(s): fixed_outer
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.39.2
Specification(s): fixed_outer_rz
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31
16.39.3
Specification(s): free_outer
Collection(s): FUNCTIONAL
Type(s): CSVDiff
31

Usability Requirements

Performance Requirements

System Interface Requirements

References

No citations exist within this document.

[fullsat_brine]
  type = CSVDiff
  input = 'fullsat_brine.i'
  csvdiff = 'fullsat_brine.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "The system shall calculate proper density, viscosity, enthalpy and internal energy with the PorousFlowBrine material when using PorousFlowFullySaturated Action."
  issues = "#10093"
  design = "brineco2.md"
[]


[fullsat_brine_except1]
  type = RunException
  input = 'fullsat_brine_except1.i'
  expect_err = 'PorousFlowSinglePhaseBase: You must specify nacl_name when fluid_properties_type = PorousFlowBrine'
  threading = '!pthreads'
  requirement = "The system shall produce an error when attempting to use a PorousFlowBrine Material without any NaCl variable"
  issues = "#10093 #16841"
  design = "brineco2.md"
[]


[fullsat_brine_except2]
  type = RunException
  input = 'fullsat_brine_except2.i'
  expect_err = 'PorousFlowSinglePhaseBase: You should not specify fp when fluid_properties_type = PorousFlowBrine'
  match_literal = true
  threading = '!pthreads'
  requirement = "The system shall produce an error when attempting to use a PorousFlowBrine Material at the same time as a PorousFlowSimpleFluidProperties Material"
  issues = "#10093 #16841"
  design = "brineco2.md"
[]


[fullsat_brine_except3]
  type = RunException
  input = 'fullsat_brine_except3.i'
  expect_err = 'PorousFlowSinglePhaseBase: You should not specify a nacl_name when fluid_properties_type = PorousFlowSingleComponentFluid'
  match_literal = true
  threading = '!pthreads'
  requirement = "The system shall produce an error when attempting to use a PorousFlowSingleComponentFluid Material at the same time as a PorousFlowBrine Material"
  issues = "#10093 #16841"
  design = "brineco2.md"
[]


[fullsat_brine_except4]
  type = RunException
  input = 'fullsat_brine_except4.i'
  expect_err = 'PorousFlowSinglePhaseBase: You must specify fp when fluid_properties_type = PorousFlowSingleComponentFluid'
  match_literal = true
  threading = '!pthreads'
  requirement = "The system shall produce an error when attempting to use a PorousFlowSingleComponentFluid Material without a fluid-properties UserObject"
  issues = "#16841"
  design = "PorousFlowFullySaturated.md"
[]


[fullsat_brine_except5]
  type = RunException
  input = 'fullsat_brine_except5.i'
  expect_err = 'Must use pressure_unit = Pa for fluid_properties_type = PorousFlowBrine'
  match_literal = true
  threading = '!pthreads'
  requirement = "The system shall produce an error when attempting to use a non-standard pressure unit choice with PorousFlowBrine"
  issues = "#16841"
  design = "PorousFlowFullySaturated.md"
[]


[fullsat_brine_except6]
  type = RunException
  input = 'fullsat_brine_except6.i'
  expect_err = 'Must use time_unit = seconds for fluid_properties_type = PorousFlowBrine'
  match_literal = true
  threading = '!pthreads'
  requirement = "The system shall produce an error when attempting to use a non-standard time unit choice with PorousFlowBrine"
  issues = "#16841"
  design = "PorousFlowFullySaturated.md"
[]


[unsat_except1]
  type = RunException
  input = 'unsat_except1.i'
  expect_err = 'Some stabilization must be used in PorousFlowUnsaturated'
  threading = '!pthreads'
  requirement = "The system shall produce an error if PorousFlowUnsaturated is used with no stabilization."
  issues = "#16841"
  design = "PorousFlowUnsaturated.md"
[]


[unsat_except2]
  type = RunException
  input = 'unsat_except2.i'
  expect_err = 'The number of save_component_rate_in variables must be the number of fluid components + 1'
  match_literal = true
  threading = '!pthreads'
  requirement = "The system shall produce an error if the number of variables to save fluid-component rates-of-change into is not equal to the number of fluid components"
  issues = "#16841"
  design = "PorousFlowUnsaturated.md"
[]


[addjoiner]
  type = RunApp
  input = addjoiner.i
  threading = '!pthreads'
  no_error_deprecated = true
  requirement = "The system shall produce a warning when attempting to add materials to the simulation when using the PorousFlowFullySaturated Action."
  issues = "#10093"
  design = "PorousFlowAddMaterialJoiner.md"
[]


[addmaterials]
  type = RunApp
  input = addmaterials.i
  threading = '!pthreads'
  requirement = "The system shall handle adding materials properly when the add_nodes parameter and the at_nodes=true parameters are both active in the PorousFlowFullySaturated Action."
  issues = "#10093"
  design = "PorousFlowAddMaterialAction.md"
[]


[addmaterials2]
  type = RunApp
  input = addmaterials2.i
  threading = '!pthreads'
  requirement = "The system shall handle adding materials properly when the add_nodes parameter is supplied in the PorousFlowFullySaturated Action."
  issues = "#10093"
  design = "PorousFlowAddMaterialAction.md"
[]


[basicthm_h]
  type = Exodiff
  input = 'basicthm_h.i'
  exodiff = 'basicthm_h_out.e'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "The system shall add all required objects when using PorousFlowBasicTHM Action with coupling_type = Hydro."
  issues = "#8574"
  design = "PorousFlowBasicTHM.md"
[]


[basicthm_th]
  type = Exodiff
  input = 'basicthm_th.i'
  exodiff = 'basicthm_th_out.e'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "The system shall add all required objects when using PorousFlowBasicTHM Action with coupling_type = ThermoHydro."
  issues = "#8574"
  design = "PorousFlowBasicTHM.md"
[]


[basicthm_hm]
  type = Exodiff
  input = 'basicthm_hm.i'
  exodiff = 'basicthm_hm_out.e'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "The system shall add all required objects when using PorousFlowBasicTHM Action with coupling_type = HydroMechanical."
  issues = "#8574"
  design = "PorousFlowBasicTHM.md"
[]


[basicthm_thm]
  type = Exodiff
  input = 'basicthm_thm.i'
  exodiff = 'basicthm_thm_out.e'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "The system shall add all required objects when using PorousFlowBasicTHM Action with coupling_type = ThermoHydroMechanical."
  issues = "#8574"
  design = "PorousFlowBasicTHM.md"
[]


[block_restricted]
  type = Exodiff
  input = block_restricted_materials.i
  exodiff = block_restricted_materials_out.e
  threading = '!pthreads'
  requirement = "The system shall handle adding materials properly when materials are block restricted"
  issues = "#10093"
  design = "PorousFlowAddMaterialJoiner.md PorousFlowAddMaterialAction.md"
[]


[basicthm_bh]
  type = CSVDiff
  input = 'basicthm_borehole.i'
  csvdiff = 'basicthm_borehole_out.csv'
  threading = '!pthreads'
  requirement = "The system shall add all required objects when using PorousFlowBasicTHM Action to allow boreholes to be used"
  issues = "#17025"
  design = "PorousFlowBasicTHM.md"
[]


[fullsat_bh]
  type = CSVDiff
  input = 'fullsat_borehole.i'
  csvdiff = 'fullsat_borehole_out.csv'
  threading = '!pthreads'
  requirement = "The system shall add all required objects when using PorousFlowFullySaturated Action to allow boreholes to be used"
  issues = "#17025"
  design = "PorousFlowFullySaturated.md"
[]


[multiblock]
  type = 'CSVDiff'
  input = multiblock.i
  threading = '!pthreads'
  csvdiff = 'multiblock_out.csv'
  requirement = "PorousFlow shall be able to be block-restricted, specifically so that a model's physics is governed by PorousFlow only on part of the mesh"
  issues = '#20260'
  design = 'actions/PorousFlowAddMaterialJoiner.md'
[]


[block_restricted_and_not]
  type = RunApp
  input = block_restricted_and_not.i
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to be block-restricted, and Joiners shall work even when one PorousFlow material is block-restricted for one phase and non block-restricted for another"
  issues = '#20260'
  design = 'actions/PorousFlowAddMaterialJoiner.md'
[]

[./tri]
  type = Exodiff
  input = 'tri3_adaptivity.i'
  exodiff = 'tri3_adaptivity_out.e'
  threading = '!pthreads'
  requirement = "The system shall work when using mesh adaptivity with TRI3 elements"
  issues = "#14428"
  design = 'mass_lumping.md'
  max_threads = 1
[../]


[./quad]
  type = Exodiff
  input = 'quad_adaptivity.i'
  exodiff = 'quad_adaptivity_out.e'
  threading = '!pthreads'
  requirement = "The system shall work when using mesh adaptivity with QUAD elements"
  issues = "#14428"
  design = 'mass_lumping.md'
[../]


[./tet]
  type = Exodiff
  input = 'tet4_adaptivity.i'
  exodiff = 'tet4_adaptivity_out.e'
  threading = '!pthreads'
  requirement = "The system shall work when using mesh adaptivity with TET4 elements"
  issues = "#14428"
  design = 'mass_lumping.md'
[../]


[./hex]
  type = Exodiff
  input = 'hex_adaptivity.i'
  exodiff = 'hex_adaptivity_out.e'
  threading = '!pthreads'
  requirement = "The system shall work when using mesh adaptivity with HEX elements"
  issues = "#14428"
  design = 'mass_lumping.md'
[../]

[darcy_velocity]
  type = 'CSVDiff'
  input = 'darcy_velocity.i'
  csvdiff = 'darcy_velocity.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate the Darcy flow velocity vector for a fully-saturated case'
  issues = '#17159'
  design = 'PorousFlowDarcyVelocityComponent.md'
[]


[properties]
  type = 'Exodiff'
  input = 'properties.i'
  exodiff = 'properties_out.e'
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to populate AuxVariables corresponding to capillary pressure, saturation, fluid density, etc'
  issues = '#17159'
  design = 'PorousFlowPropertyAux.md'
[]


[darcy_velocity_lower]
  type = 'CSVDiff'
  input = 'darcy_velocity_lower.i'
  csvdiff = 'darcy_velocity_lower_out.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate the Darcy flow velocity vector on 2D fracture embedded inside a 3D matrix'
  issues = '#17159'
  design = 'PorousFlowDarcyVelocityComponentLowerDimensional.md'
[]


[darcy_velocity_lower_tets]
  type = 'CSVDiff'
  input = 'darcy_velocity_lower.i'
  cli_args = 'Mesh/file=fractured_block_tets.e'
  prereq = 'darcy_velocity_lower'
  csvdiff = 'darcy_velocity_lower_out.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate the Darcy flow velocity vector on 2D fracture embedded inside a 3D matrix, including the case with triangular and tetrahedral elements'
  issues = '#17159'
  design = 'PorousFlowDarcyVelocityComponentLowerDimensional.md'
[]


[darcy_velocity_lower_2D]
  type = 'CSVDiff'
  input = 'darcy_velocity_lower_2D.i'
  csvdiff = 'darcy_velocity_lower_2D_out.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate the Darcy flow velocity vector on 1D fracture embedded inside a 2D matrix'
  issues = '#17159'
  design = 'PorousFlowDarcyVelocityComponentLowerDimensional.md'
[]


[darcy_velocity_lower_except]
  type = 'RunException'
  input = 'darcy_velocity_lower_except.i'
  expect_err = 'The variable fracture_vel_x must must be defined on lower-dimensional elements only since it employs PorousFlowDarcyVelocityComponentLowerDimensional'
  threading = '!pthreads'
  requirement = 'An error shall be produced if PorousFlow is asked to calculate the Darcy flow velocity vector on a lower-dimensional fracture, but the variables are not defined only on the lower-dimensional elements'
  issues = '#17159'
  design = 'PorousFlowDarcyVelocityComponentLowerDimensional.md'
[]


[element_length_except1]
  type = RunException
  input = element_length_except1.i
  expect_err = 'The variable must be an elemental variable'
  requirement = 'PorousFlow shall be able to calculate a measure of element length in a given direction, and shall produce an error if a nodal variable is used to store the results'
  issues = '#18232'
  design = 'PorousFlowElementLength.md'
[]


[element_length_except2]
  type = RunException
  input = element_length_except2.i
  expect_err = 'Three values or variables must be provided'
  requirement = 'PorousFlow shall be able to calculate a measure of element length in a given direction, and shall produce an error if the direction is incorrectly specified'
  issues = '#18232'
  design = 'PorousFlowElementLength.md'
[]


[element_length_2D]
  type = CSVDiff
  input = element_length_2D.i
  csvdiff = element_length_2D_out.csv
  requirement = 'PorousFlow shall be able to calculate a measure of element length in a given direction, in 2D'
  issues = '#18232'
  design = 'PorousFlowElementLength.md'
[]


[element_length_3D]
  type = CSVDiff
  input = element_length_3D.i
  csvdiff = element_length_3D_out.csv
  requirement = 'PorousFlow shall be able to calculate a measure of element length in a given direction, in 3D'
  issues = '#18232'
  design = 'PorousFlowElementLength.md'
[]


[element_normal_except1]
  type = RunException
  input = element_normal_except1.i
  expect_err = 'The variable must be an elemental variable'
  requirement = 'PorousFlow shall be able to calculate element normal, and shall produce an error if a nodal variable is used to store the result'
  issues = '#18232'
  design = 'PorousFlowElementNormal.md'
[]


[element_normal_except2]
  type = RunException
  input = element_normal_except2.i
  expect_err = 'Must not be the zero vector'
  requirement = 'PorousFlow shall be able to calculate element normal for 1D elements if provided with a perpendicular vector, and shall produce an error if the perpendicular vector is incorrectly specified'
  issues = '#18232'
  design = 'PorousFlowElementNormal.md'
[]


[element_normal_except3]
  type = RunException
  input = element_normal_except3.i
  expect_err = 'Must not be the zero vector'
  requirement = 'PorousFlow shall be able to calculate element normals for meshes containing 3D elements if provided with a default value for the 3D elements, but shall produce an error if that default value is incorrectly specified'
  issues = '#18232'
  design = 'PorousFlowElementNormal.md'
[]


[element_normal_1D_2D]
  type = CSVDiff
  input = element_normal_1D_2D.i
  csvdiff = element_normal_1D_2D_out.csv
  requirement = 'PorousFlow shall be able to calculate element normals for 1D and 2D elements, if provided with a perpendicular vector for the 1D elements'
  issues = '#18232'
  design = 'PorousFlowElementNormal.md'
[]


[element_normal_2D_3D]
  type = CSVDiff
  input = element_normal_2D_3D.i
  csvdiff = element_normal_2D_3D_out.csv
  requirement = 'PorousFlow shall be able to calculate element normals for 2D and 3D elements, if provided with a default value for the 3D elements'
  issues = '#18232'
  design = 'PorousFlowElementNormal.md'
[]

[./except1]
  type = RunException
  input = except1.i
  expect_err = 'The Dictator proclaims that the maximum phase index in this simulation is 0 whereas you have used 1. Remember that indexing starts at 0. The Dictator is watching you, to ensure your wellbeing.'
  threading = '!pthreads'
[../]

[./bl01]
  type = 'Exodiff'
  input = 'bl01.i'
  exodiff = 'bl01.e'
  threading = '!pthreads'
  cli_args = 'UserObjects/pc/alpha=1E-4 Functions/timestepper/x=0 Functions/timestepper/y=7.5'
  requirement = 'PorousFlow shall be able to simulate a Buckley-Leverett problem'
  design = 'porous_flow/tests/buckley_leverett/buckley_leverett_tests.md'
  issues = '#13155 #16953'
[../]


[./bl01_heavy]
  type = CSVDiff
  input = bl01.i
  csvdiff = 'bl01_pp_0001.csv bl01_sat_0001.csv bl01_pp_0150.csv bl01_sat_0150.csv'
  heavy = true
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to simulate a Buckley-Leverett problem with small saturation'
  design = 'porous_flow/tests/buckley_leverett/buckley_leverett_tests.md'
  issues = '#13155 #16953'
[../]

[./except1]
  type = RunException
  input = except1.i
  expect_err = 'PorousFlowMassFractionAqueousEquilibriumChemistry: The number of secondary activity coefficients is 1 which must be equal to the number of secondary species \(2\)'
  threading = '!pthreads'
[../]


[./except2]
  type = RunException
  input = except2.i
  expect_err = 'The Dictator proclaims that the number of phases is 2 whereas PorousFlow1PhaseFullySaturated can only be used for 1-phase simulations. Be aware that the Dictator has noted your mistake.'
  threading = '!pthreads'
[../]


[./except3]
  type = RunException
  input = except3.i
  expect_err = 'This value must be equal to the Dictator\'s num_phases \(1\) multiplied by num_components-1 \(1\)'
  threading = '!pthreads'
[../]


[./except5]
  type = RunException
  input = except5.i
  expect_err = 'PorousFlowMassFractionAqueousEquilibriumChemistry: The number of equilibrium constants is 1 which must be equal to the number of reactions \(2\)'
  threading = '!pthreads'
[../]


[./except6]
  type = RunException
  input = except6.i
  expect_err = 'PorousFlowMassFractionAqueousEquilibriumChemistry: The number of primary activity coefficients is 1 which must be equal to the number of primary species \(2\)'
  threading = '!pthreads'
[../]


[./except7]
  type = RunException
  input = except7.i
  expect_err = 'PorousFlowMassFractionAqueousEquilibriumChemistry: The number of stoichiometric coefficients specified in \'reactions\' \(2\) must be equal to the number of reactions \(2\) multiplied by the number of primary species \(2\)'
  threading = '!pthreads'
[../]


[./except8]
  type = RunException
  input = except8.i
  expect_err = 'PorousFlowAqueousPreDisChemistry: The number of specific reactive surface areas provided is 2 which must be equal to the number of reactions \(1\)'
  threading = '!pthreads'
[../]


[./except9]
  type = RunException
  input = except9.i
  expect_err = 'PorousFlowAqueousPreDisChemistry: The number of kinetic rate constants is 2 which must be equal to the number of reactions \(1\)'
  threading = '!pthreads'
[../]


[./except10]
  type = RunException
  input = except10.i
  expect_err = 'PorousFlowAqueousPreDisChemistry: The number of activation energies is 2 which must be equal to the number of reactions \(1\)'
  threading = '!pthreads'
[../]


[./except11]
  type = RunException
  input = except11.i
  expect_err = 'PorousFlowAqueousPreDisChemistry: The number of molar volumes is 2 which must be equal to the number of reactions \(1\)'
  threading = '!pthreads'
[../]


[./except12]
  type = RunException
  input = except12.i
  expect_err = 'PorousFlowAqueousPreDisChemistry: The number of theta exponents is 2 which must be equal to the number of reactions \(1\)'
  threading = '!pthreads'
[../]


[./except13]
  type = RunException
  input = except13.i
  expect_err = 'PorousFlowAqueousPreDisChemistry: The number of eta exponents is 2 which must be equal to the number of reactions \(1\)'
  threading = '!pthreads'
[../]


[./except14]
  type = RunException
  input = except14.i
  expect_err = 'PorousFlowAqueousPreDisMineral: The number of initial concentrations is 2 but the Dictator knows that the number of aqueous kinetic \(precipitation-dissolution\) reactions is 1'
  threading = '!pthreads'
[../]


[./except15]
  type = RunException
  input = except15.i
  expect_err = 'The Dictator proclaims that the number of precipitation-dissolution secondary species in this simulation is 1 whereas you have provided 2. The Dictator does not take such mistakes lightly'
  threading = '!pthreads'
[../]


[./except16]
  type = RunException
  input = except16.i
  expect_err = 'The Dictator proclaims that the number of precipitation-dissolution secondary species in this simulation is 1 whereas you have provided 2. The Dictator does not take such mistakes lightly'
  threading = '!pthreads'
[../]


[./except17]
  type = RunException
  input = except17.i
  expect_err = 'PorousFlowMassFractionAqueousEquilibriumChemistry: You have specified the number of reactions to be 2 but the Dictator knows that the number of aqueous equilibrium reactions is 0'
  threading = '!pthreads'
[../]


[./except18]
  type = RunException
  input = except18.i
  expect_err = 'PorousFlowAqueousPreDisChemistry: You have specified the number of reactions to be 1 but the Dictator knows that the number of aqueous kinetic \(precipitation-dissolution\) reactions is 0'
  threading = '!pthreads'
[../]


[./except19]
  type = RunException
  input = except19.i
  expect_err = 'PorousFlowPorosity: When chemical=true you must provide the initial_mineral_concentrations.  The Dictator proclaims there should be 1 of these'
  threading = '!pthreads'
[../]


[./except20]
  type = RunException
  input = except20.i
  expect_err = 'PorousFlowPorosity: When chemical=true you must provide the reference_chemistry values.  The Dictator proclaims there should be 1 of these'
  threading = '!pthreads'
[../]


[./except21]
  type = RunException
  input = except21.i
  expect_err = 'PorousflowDictator: The aqueous phase number must be less than the number of fluid phases.  The Dictator does not appreciate jokes.'
  threading = '!pthreads'
[../]

[./squarepules]
  type = 'CSVDiff'
  input = 'squarepulse1.i'
  csvdiff = 'squarepulse1.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowSquarePulsePointSource shall provide a constant mass point source/sink between two specified times'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowSquarePulsePointSource.md'
  issues = '#6990'
[../]


[./frompps]
  type = 'CSVDiff'
  input = 'frompps.i'
  csvdiff = 'frompps.csv'
  threading = '!pthreads'
  requirement = 'The system shall provide a mass point source/sink computed by a postprocessor'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPointSourceFromPostprocessor.md'
  issues = '#15132'
[../]


[./hfrompps]
  type = 'CSVDiff'
  input = 'hfrompps.i'
  csvdiff = 'hfrompps.csv'
  threading = '!pthreads'
  requirement = 'The system shall provide an enthalphy point source computed by a postprocessor'
  design = 'porous_flow/sinks.md PorousFlowPointEnthalpySourceFromPostprocessor.md'
  issues = '#15742'
[../]


[./theis1]
  type = 'CSVDiff'
  input = 'theis1.i'
  csvdiff = 'theis1_pressure_0006.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowSquarePulsePointSource shall provide a constant mass point sink between two specified times'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowSquarePulsePointSource.md'
  issues = '#6990'
[../]


[./theis_rz]
  type = 'CSVDiff'
  input = 'theis_rz.i'
  csvdiff = 'theis_rz_csv_pp_0006.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to accurately simulate drawdown in 2D groundwater systems, to agree with the Theis solution'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowSquarePulsePointSource.md'
  issues = '#6990 #13155'
[../]


[./theis2]
  type = 'CSVDiff'
  input = 'theis2.i'
  csvdiff = 'theis2_pressure_0006.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowSquarePulsePointSource shall provide a constant mass point sink between two specified times'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowSquarePulsePointSource.md'
  issues = '#6990'
[../]


[./theis3]
  type = 'CSVDiff'
  input = 'theis3.i'
  csvdiff = 'theis3.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowSquarePulsePointSource shall provide a constant mass point source of a specified fluid phase'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowSquarePulsePointSource.md'
  issues = '#7677'
[../]


[./bh_except01]
  type = 'RunException'
  input = 'bh_except01.i'
  expect_err = 'The Dictator proclaims that the maximum phase index in this simulation is 0 whereas you have used 1. Remember that indexing starts at 0. You must try harder.'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if the fluid phase is larger than the number of phases in the system'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh_except02]
  type = 'RunException'
  input = 'bh_except02.i'
  expect_err = 'The Dictator proclaims that the maximum fluid component index in this simulation is 0 whereas you have used 1. Remember that indexing starts at 0. Please be assured that the Dictator has noted your error.'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if the fluid component is larger than the number of fluid components in the system'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh_except03]
  type = 'RunException'
  input = 'bh_except03.i'
  expect_err = 'PorousFlowLineSink: You have specified function_of=porepressure, but you do not have a quadpoint porepressure material'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if flux is a function of porepressure but no porepressure material exists'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh_except04]
  type = 'RunException'
  input = 'bh_except04.i'
  expect_err = 'PorousFlowLineSink: You have specified function_of=temperature, but you do not have a quadpoint temperature material'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if flux is a function of temperature but no temperature material exists'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh_except05]
  type = 'RunException'
  input = 'bh_except05.i'
  expect_err = 'PorousFlowLineSink: You have specified a fluid component, but do not have a nodal mass-fraction material'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if flux is restricted to a specific fluid component but no mass fraction material exists'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh_except06]
  type = 'RunException'
  input = 'bh_except06.i'
  expect_err = 'PorousFlowLineSink: You have set use_mobility=true, but do not have nodal density, relative permeability or viscosity material'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if flux is to be multiplied by mobility but no nodal fluid density material exists'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh_except07]
  type = 'RunException'
  input = 'bh_except07.i'
  expect_err = 'PorousFlowLineSink: You have set use_mobility=true, but do not have nodal density, relative permeability or viscosity material'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if flux is to be multiplied by mobility but no nodal relative permeability material exists'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh_except08]
  type = 'RunException'
  input = 'bh_except08.i'
  expect_err = 'PorousFlowLineSink: You have set use_mobility=true, but do not have nodal density, relative permeability or viscosity material'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if flux is to be multiplied by mobility but no nodal fluid density material exists'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh_except09]
  type = 'RunException'
  input = 'bh_except09.i'
  expect_err = 'PorousFlowLineSink: You have set use_enthalpy=true, but do not have a nodal enthalpy material'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if flux is to be multiplied by enthalpy but no fluid enthalpy material exists'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh_except10]
  type = 'RunException'
  input = 'bh_except10.i'
  expect_err = 'PorousFlowLineSink: You have set use_internal_energy=true, but do not have a nodal internal-energy material'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if flux is to be multiplied by internal energy but no fluid internal energy material exists'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh_except11]
  type = 'RunException'
  input = 'bh_except11.i'
  expect_err = 'PorousFlowLineSink: You have set use_relative_permeability=true, but do not have a nodal relative permeability material'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if flux is to be multiplied by relative permeability but no nodal relative permeability material exists'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh_except12]
  type = 'RunException'
  input = 'bh_except12.i'
  expect_err = 'PorousFlowLineGeometry: Error opening file does_not_exist'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if the given point file does not exist'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh_except13]
  type = 'RunException'
  input = 'bh_except13.i'
  expect_err = 'PorousFlowLineGeometry: zero-segment length detected at \(x,y,z\) = 0.1 0.2 0.3'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if two points in the point file are coincident'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh_except14]
  type = 'RunException'
  input = 'bh_except14.i'
  expect_err = 'The effective element size \(about 0.2-times-true-ele-size\) for an element containing a Peaceman-type borehole must be \(much\) larger than the borehole radius for the Peaceman formulation to be correct.  Your element has effective size 0.39598 and the borehole radius is 10'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if the element containing the dirac kernel is not larger than the specified borehole radius'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh_except15]
  type = 'RunException'
  input = 'bh_except15.i'
  expect_err = 'PorousFlowPeacemanBorehole: You have specified function_of=porepressure, but you do not have a quadpoint permeability material'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if flux is a function of porepressure but no permeability material exists'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh_except16]
  type = 'RunException'
  input = 'bh_except16.i'
  expect_err = 'PorousFlowPeacemanBorehole: You have specified function_of=temperature, but you do not have a quadpoint thermal_conductivity material'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall throw an error if flux is a function of temperature but no thermal conductivity material exists'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./pls01_00]
  type = 'CSVDiff'
  input = 'pls01.i'
  cli_args = 'DiracKernels/pls/point_file=pls01_00.bh Outputs/file_base=pls01_00'
  csvdiff = 'pls01_00.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall extract fluid at the specified rate'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPolyLineSink.md'
  issues = '#7992 #8139'
[../]


[./pls01_line_base]
  type = 'CSVDiff'
  input = 'pls01.i'
  cli_args = "DiracKernels/pls/point_file='' DiracKernels/pls/line_base='10 0 0' DiracKernels/pls/line_length=.02 DiracKernels/pls/line_direction='1 0 0' Outputs/file_base=pls01_line_base"
  csvdiff = 'pls01_line_base.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall extract fluid at the specified rate when using the line_base parameter'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPolyLineSink.md'
  issues = '#7992 #8139'
[../]


[./pls01_line_base_bounds]
  type = RunException
  input = 'pls01.i'
  cli_args = "DiracKernels/pls/point_file='' DiracKernels/pls/line_base='.1 0 0' DiracKernels/pls/line_length=42 DiracKernels/pls/line_direction='0 0 1'"
  expect_err = 'length causes end point.*to lie outside the mesh'
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall abort with an error if the line base, direction, and length cause the line to exit the mesh domain."'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPolyLineSink.md'
  issues = '#7992 #8139'
[../]


[./pls01_01]
  type = 'CSVDiff'
  input = 'pls01.i'
  cli_args = 'DiracKernels/pls/point_file=pls01_01.bh Outputs/file_base=pls01_01'
  csvdiff = 'pls01_01.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall extract fluid at the specified rate'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPolyLineSink.md'
  issues = '#7992 #8139'
[../]


[./pls01_20]
  type = 'CSVDiff'
  input = 'pls01.i'
  cli_args = 'DiracKernels/pls/point_file=pls01_20.bh Outputs/file_base=pls01_20'
  csvdiff = 'pls01_20.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall extract fluid at the specified rate'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPolyLineSink.md'
  issues = '#7992 #8139'
[../]


[./pls01_21]
  type = 'CSVDiff'
  input = 'pls01.i'
  cli_args = 'DiracKernels/pls/point_file=pls01_21.bh Outputs/file_base=pls01_21'
  csvdiff = 'pls01_21.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall extract fluid at the specified rate'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPolyLineSink.md'
  issues = '#7992 #8139'
[../]


[./pls02]
  type = 'CSVDiff'
  input = 'pls02.i'
  csvdiff = 'pls02.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall extract fluid at the specified rate'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPolyLineSink.md'
  issues = '#7992 #8139'
[../]


[./pls02_autopoints]
  type = 'CSVDiff'
  input = 'pls02.i'
  csvdiff = 'pls02_dirac_pts_0004.csv'
  allow_test_objects = true
  mesh_mode = replicated
  cli_args = "VectorPostprocessors/dirac_pts/type=DiracPointsWriter DiracKernels/pls/point_file='' DiracKernels/pls/line_base='0.1 0.01 0.01 -0.249' DiracKernels/pls/line_direction='0 0 1' DiracKernels/pls/line_length=0.5 Adaptivity/max_h_level=4 Adaptivity/steps=3 Adaptivity/marker=box Adaptivity/Markers/box/type=BoxMarker Adaptivity/Markers/box/bottom_left='-2 -2 -2' Adaptivity/Markers/box/top_right='2 2 2' Adaptivity/Markers/box/inside=refine Adaptivity/Markers/box/outside=do_nothing Executioner/end_time=4"
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall be able to dynamically create dirac points automatically in response to changing mesh geometry.'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPolyLineSink.md'
  issues = '#15528 #15547'
[../]


[./pls03_00]
  type = 'CSVDiff'
  input = 'pls03.i'
  cli_args = 'ICs/pp/function="if((x<1)&(y<0.5),1E7,-1E7)" Outputs/file_base=pls03_00'
  csvdiff = 'pls03_00.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall extract fluid at the specified rate'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPolyLineSink.md'
  issues = '#7992 #8139'
[../]


[./pls03_01]
  type = 'CSVDiff'
  input = 'pls03.i'
  cli_args = 'ICs/pp/function="if((x<1)&(y>0.5),1E7,-1E7)" Outputs/file_base=pls03_01'
  csvdiff = 'pls03_01.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall extract fluid at the specified rate'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPolyLineSink.md'
  issues = '#7992 #8139'
[../]


[./pls03_20]
  type = 'CSVDiff'
  input = 'pls03.i'
  cli_args = 'ICs/pp/function="if((x>1)&(y<0.5),1E7,-1E7)" Outputs/file_base=pls03_20'
  csvdiff = 'pls03_20.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall extract fluid at the specified rate'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPolyLineSink.md'
  issues = '#7992 #8139'
[../]


[./pls03_21]
  type = 'CSVDiff'
  input = 'pls03.i'
  cli_args = 'ICs/pp/function="if((x>1)&(y>0.5),1E7,-1E7)" Outputs/file_base=pls03_21'
  csvdiff = 'pls03_21.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall extract fluid at the specified rate'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPolyLineSink.md'
  issues = '#7992 #8139'
[../]


[./pls03_action]
  type = 'CSVDiff'
  input = 'pls03_action.i'
  csvdiff = 'pls03_action.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall extract fluid at the specified rate'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPolyLineSink.md'
  issues = '#7992 #8139'
[../]


[./pls02reporter]
  type = 'CSVDiff'
  input = 'pls02reporter.i'
  csvdiff = 'pls02reporter_out.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall extract fluid at the specified rate getting the coordinates from a reporter'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPolyLineSink.md'
  issues = '#20018'
[../]


[./pls02reporter_wrongSize]
  type = RunException
  input = 'pls02reporter.i'
  cli_args = "Reporters/pls02file/real_vector_values='0.10; 0 0; 0 0; -0.25 0.25'"
  expect_err = 'weight size = 1;  x_coord size = 2;  y_coord size = 2;  z_coord size = 2'
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall abort with an error if the reporter containing the coordinates is not the same size as the reporter containing weights'
  design = 'PorousFlowPolyLineSink.md'
  issues = '#20506'
[../]


[./pls02reporter_empty]
  type = RunException
  input = 'pls02reporter.i'
  cli_args = "Reporters/pls02file/type=EmptyReporter"
  expect_err = 'PorousFlowLineGeometry: No points found in input.'
  allow_test_objects = true
  threading = '!pthreads'
  requirement = 'PorousFlowPolyLineSink shall abort with an error if the coordinates reporter is empty'
  design = 'PorousFlowPolyLineSink.md'
  issues = '#20506'
[../]


[./bh02]
  type = 'CSVDiff'
  input = 'bh02.i'
  csvdiff = 'bh02.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall extract fluid at the specified rate in a fully-saturated system'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh03]
  type = 'CSVDiff'
  input = 'bh03.i'
  csvdiff = 'bh03.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall inject fluid at the specified rate in a fully-saturated system'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139 #20452'
[../]


[./bh04]
  type = 'CSVDiff'
  input = 'bh04.i'
  csvdiff = 'bh04.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall extract fluid at the specified rate in a fully-saturated system'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh05]
  type = 'CSVDiff'
  input = 'bh05.i'
  csvdiff = 'bh05.csv'
  rel_err = 5.7e-06 # diff is ~5.6e-6 on falcon
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall inject fluid at the specified rate in an unsaturated system'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh07]
  type = 'CSVDiff'
  input = 'bh07.i'
  cli_args = 'Outputs/file_base=bh07_csv'
  csvdiff = 'bh07_csv_pp_0003.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall extract fluid at the specified rate in a cylindrical model'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh07_exo]
  type = 'Exodiff'
  input = 'bh07.i'
  exodiff = 'bh07.e'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall extract fluid at the specified rate in a cylindrical model'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./bh02reporter]
  type = 'CSVDiff'
  input = 'bh02reporter.i'
  csvdiff = 'bh02reporter_out.csv'
  threading = '!pthreads'
  requirement = 'PorousFlowPeacemanBorehole shall extract fluid at the specified rate in a fully-saturated system using reporter for input'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#20018'
[../]


[./injection_production]
  type = 'Exodiff'
  input = 'injection_production.i'
  exodiff = 'injection_production_out.e'
  threading = '!pthreads'
  requirement = 'Multiple PorousFlowPeacemanBorehole objects shall be able to inject and extract fluid in different locations'
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#7992 #8139'
[../]


[./strain_at_nearest_qp]
  type = RunApp
  input = strain_at_nearest_qp.i
  threading = '!pthreads'
  requirement = "If the strain at the nearest quadpoint is used when evaluating PorousFlowPorosity that is coupled to solid mechanics, all PorousFlow DiracKernels shall be usable"
  issues = "#12541"
  design = 'porous_flow/tests/dirackernels/dirackernels_tests.md porous_flow/sinks.md'
[../]


[./injection_with_plasticity]
  type = 'Exodiff'
  input = 'injection_with_plasticity.i'
  exodiff = 'injection_with_plasticity_out.e'
  threading = '!pthreads'
  abs_zero = 1E-5
  requirement = 'It shall be possible to use PorousFlow DiracKernels in simulations involving plastic deformation'
  design = 'porous_flow/sinks.md PorousFlowPeacemanBorehole.md'
  issues = '#12962'
[../]

[./diff01]
  type = 'CSVDiff'
  input = 'diff01.i'
  csvdiff = 'diff01_out_xmass_0021.csv'
  threading = '!pthreads'
  issues = '#13155'
  design = 'porous_flow/tests/dispersion/dispersion_tests.md'
  requirement = 'PorousFlow shall correctly simulate the molecular diffusion'
[../]


[./diff01_action]
  type = 'CSVDiff'
  input = 'diff01_action.i'
  csvdiff = 'diff01_action_out_xmass_0021.csv'
  threading = '!pthreads'
  issues = '#13155'
  design = 'porous_flow/tests/dispersion/dispersion_tests.md'
  requirement = 'PorousFlow shall correctly simulate the molecular diffusion when using an action'
[../]


[./disp01]
  type = 'CSVDiff'
  input = 'disp01.i'
  csvdiff = 'disp01_out_xmass_0029.csv'
  rel_err = 1E-5
  threading = '!pthreads'
  issues = '#13155'
  design = 'porous_flow/tests/dispersion/dispersion_tests.md'
  requirement = 'PorousFlow shall correctly simulate the hydrodynamic dispersion'
[../]


[./disp01_heavy]
  type = 'CSVDiff'
  input = 'disp01_heavy.i'
  csvdiff = 'disp01_heavy_out_xmass_0105.csv'
  rel_err = 1E-5
  heavy = true
  threading = '!pthreads'
  issues = '#13155'
  design = 'porous_flow/tests/dispersion/dispersion_tests.md'
  requirement = 'PorousFlow shall correctly simulate the hydrodynamic dispersion in a high-resolution setting'
[../]

[./except01]
  type = 'RunException'
  input = 'except01.i'
  expect_err = 'The Dictator proclaims that the phase index 1 is greater than the largest phase index possible, which is 0'
  threading = '!pthreads'
  issues = '#8123'
  design = 'PorousFlowHeatEnergy.md PorousFlowHeatVolumetricExpansion.md PorousFlowEnergyTimeDerivative.md PorousFlowFullySaturatedHeatAdvection.md PorousFlowHeatAdvection.md PorousFlowHeatConduction.md PorousFlowPlasticHeatEnergy.md'
  requirement = 'PorousFlow shall produce an error if the user specifies a phase number that is too large for the simulation according to the PorousFlowDictator'
[../]


[./except02]
  type = 'RunException'
  input = 'except02.i'
  expect_err = 'The Dictator pronounces that the number of PorousFlow variables is 2, however you have used 2. This is an error'
  threading = '!pthreads'
  issues = '#8123'
  design = 'PorousFlowHeatEnergy.md PorousFlowHeatVolumetricExpansion.md PorousFlowEnergyTimeDerivative.md PorousFlowFullySaturatedHeatAdvection.md PorousFlowHeatAdvection.md PorousFlowHeatConduction.md PorousFlowPlasticHeatEnergy.md'
  requirement = 'PorousFlow shall produce an error if the user specifies a porous-flow variable that is too large for the simulation according to the PorousFlowDictator'
[../]


[./heat01]
  type = 'CSVDiff'
  input = 'heat01.i'
  csvdiff = 'heat01.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#8123'
  design = 'PorousFlowHeatEnergy.md PorousFlowHeatVolumetricExpansion.md PorousFlowEnergyTimeDerivative.md PorousFlowFullySaturatedHeatAdvection.md PorousFlowHeatAdvection.md PorousFlowHeatConduction.md PorousFlowPlasticHeatEnergy.md'
  requirement = 'PorousFlow shall correctly calculate the heat energy using the heat-energy postprocessor when there are no fluids and constant porosity'
[../]


[./heat02]
  type = 'CSVDiff'
  input = 'heat02.i'
  csvdiff = 'heat02.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#8123'
  design = 'PorousFlowHeatEnergy.md PorousFlowHeatVolumetricExpansion.md PorousFlowEnergyTimeDerivative.md PorousFlowFullySaturatedHeatAdvection.md PorousFlowHeatAdvection.md PorousFlowHeatConduction.md PorousFlowPlasticHeatEnergy.md'
  requirement = 'PorousFlow shall correctly calculate the heat energy using the heat-energy postprocessor when there is 1 fluid phase and constant porosity'
[../]


[./heat03]
  type = 'CSVDiff'
  input = 'heat03.i'
  csvdiff = 'heat03.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#8123'
  design = 'PorousFlowHeatEnergy.md PorousFlowHeatVolumetricExpansion.md PorousFlowEnergyTimeDerivative.md PorousFlowFullySaturatedHeatAdvection.md PorousFlowHeatAdvection.md PorousFlowHeatConduction.md PorousFlowPlasticHeatEnergy.md'
  requirement = 'PorousFlow shall correctly conserve heat energy in a THM simulation when the model is squashed mechanically'
[../]


[./heat03_rz]
  type = 'CSVDiff'
  input = 'heat03_rz.i'
  csvdiff = 'heat03_rz_csv.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#18324'
  design = 'PorousFlowHeatEnergy.md PorousFlowHeatVolumetricExpansion.md PorousFlowEnergyTimeDerivative.md PorousFlowFullySaturatedHeatAdvection.md PorousFlowHeatAdvection.md PorousFlowHeatConduction.md PorousFlowPlasticHeatEnergy.md'
  requirement = 'PorousFlow shall correctly conserve heat energy in a THM simulation when the model is squashed mechanically, in RZ coordinates'
[../]


[./heat04]
  type = 'CSVDiff'
  input = 'heat04.i'
  csvdiff = 'heat04.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#8123'
  design = 'PorousFlowHeatEnergy.md PorousFlowHeatVolumetricExpansion.md PorousFlowEnergyTimeDerivative.md PorousFlowFullySaturatedHeatAdvection.md PorousFlowHeatAdvection.md PorousFlowHeatConduction.md PorousFlowPlasticHeatEnergy.md'
  requirement = 'PorousFlow shall correctly calculate time-varying temperature, porepressure, stress and porosity in a model containing a source of heat energy'
[../]


[./heat04_rz]
  type = 'CSVDiff'
  input = 'heat04_rz.i'
  csvdiff = 'heat04_rz_csv.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#8123'
  design = 'PorousFlowHeatEnergy.md PorousFlowHeatVolumetricExpansion.md PorousFlowEnergyTimeDerivative.md PorousFlowFullySaturatedHeatAdvection.md PorousFlowHeatAdvection.md PorousFlowHeatConduction.md PorousFlowPlasticHeatEnergy.md'
  requirement = 'PorousFlow shall correctly calculate time-varying temperature, porepressure, stress and porosity in a model containing a source of heat energy and fluid, in RZ coordinates'
[../]


[./heat04_action]
  type = 'CSVDiff'
  input = 'heat04_action.i'
  csvdiff = 'heat04_action.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#18324'
  design = 'PorousFlowHeatEnergy.md PorousFlowHeatVolumetricExpansion.md PorousFlowEnergyTimeDerivative.md PorousFlowFullySaturatedHeatAdvection.md PorousFlowHeatAdvection.md PorousFlowHeatConduction.md PorousFlowPlasticHeatEnergy.md'
  requirement = 'PorousFlow shall correctly calculate time-varying temperature, porepressure, stress and porosity in a model containing a source of heat energy, when using the PorousFlowUnsaturated Action'
[../]


[./heat04_fullysat_action]
  type = 'CSVDiff'
  input = 'heat04_fullysat_action.i'
  csvdiff = 'heat04_fullysat_action.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#8123'
  design = 'PorousFlowHeatEnergy.md PorousFlowHeatVolumetricExpansion.md PorousFlowEnergyTimeDerivative.md PorousFlowFullySaturatedHeatAdvection.md PorousFlowHeatAdvection.md PorousFlowHeatConduction.md PorousFlowPlasticHeatEnergy.md'
  requirement = 'PorousFlow shall correctly calculate time-varying temperature, porepressure, stress and porosity in a model containing a source of heat energy, when using the PorousFlowFullySaturated Action'
[../]


[./heat04_action_KT]
  type = 'CSVDiff'
  input = 'heat04_action_KT.i'
  csvdiff = 'heat04_action.csv'
  prereq = heat04_action
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#8123 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md PorousFlowHeatEnergy.md PorousFlowHeatVolumetricExpansion.md PorousFlowEnergyTimeDerivative.md PorousFlowFullySaturatedHeatAdvection.md PorousFlowHeatAdvection.md PorousFlowHeatConduction.md PorousFlowPlasticHeatEnergy.md'
  requirement = 'PorousFlow shall correctly calculate time-varying temperature, porepressure, stress and porosity in a model containing a source of heat energy, when using the PorousFlowUnsaturated Action with Kuzmin-Turek stabilization'
[../]


[./heat05]
  type = 'CSVDiff'
  input = 'heat05.i'
  csvdiff = 'heat05.csv'
  threading = '!pthreads'
  issues = '#8123'
  design = 'PorousFlowHeatEnergy.md PorousFlowHeatVolumetricExpansion.md PorousFlowEnergyTimeDerivative.md PorousFlowFullySaturatedHeatAdvection.md PorousFlowHeatAdvection.md PorousFlowHeatConduction.md PorousFlowPlasticHeatEnergy.md'
  requirement = 'In fully-coupled THM situations, PorousFlow shall correctly initialize the porosity when it depends on all Variables'
[../]

[./h2o]
  type = 'CSVDiff'
  input = 'h2o.i'
  csvdiff = 'h2o.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to use high-precision equations of state for water from the FluidProperties module"
  issues = "#11716"
  design = 'PorousFlowSingleComponentFluid.md'
[../]


[./methane]
  type = 'CSVDiff'
  input = 'methane.i'
  csvdiff = 'methane.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to use high-precision equations of state for methane from the FluidProperties module"
  issues = "#11716"
  design = 'PorousFlowSingleComponentFluid.md'
[../]


[./ideal_gas]
  type = 'CSVDiff'
  input = 'ideal_gas.i'
  csvdiff = 'ideal_gas.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to use equations of state for an ideal gas from the FluidProperties module"
  issues = "#11716"
  design = 'PorousFlowSingleComponentFluid.md'
[../]


[./brine1]
  type = 'CSVDiff'
  input = 'brine1.i'
  csvdiff = 'brine1.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to use high-precision equations of state for brine from the FluidProperties module"
  issues = "#11716"
  design = 'PorousFlowBrine.md'
[../]


[./brine1_tab]
  type = 'CSVDiff'
  input = 'brine1_tabulated.i'
  csvdiff = 'brine1.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  prereq = 'brine1'
  requirement = "PorousFlow shall be able to use a given UserObject for water properties"
  issues = "#11716 #13882"
  design = 'PorousFlowBrine.md'
[../]


[./co2]
  type = 'CSVDiff'
  input = 'co2.i'
  csvdiff = 'co2.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to use high-precision equations of state for CO2 from the FluidProperties module"
  issues = "#11716"
  design = 'PorousFlowSingleComponentFluid.md'
[../]


[./simple_fluid]
  type = 'CSVDiff'
  input = 'simple_fluid.i'
  csvdiff = 'simple_fluid.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to use equations of state from the FluidProperties module for a single-component fluid and specify the temperature unit in Kelvin"
  issues = "#13154"
  design = 'PorousFlowSingleComponentFluid.md'
[../]


[./simple_fluid_MPa]
  type = 'CSVDiff'
  input = 'simple_fluid_MPa.i'
  csvdiff = 'simple_fluid_MPa_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to use equations of state from the FluidProperties module for a single-component fluid and specify the pressure unit in MPa"
  issues = "#13154"
  design = 'PorousFlowSingleComponentFluid.md'
[../]


[./simple_fluid_dy]
  type = 'CSVDiff'
  input = 'simple_fluid_dy.i'
  csvdiff = 'simple_fluid_dy_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to use equations of state from the FluidProperties module for a single-component fluid and specify the time unit in days"
  issues = "#13154"
  design = 'PorousFlowSingleComponentFluid.md'
[../]


[./simple_fluid_hr]
  type = 'CSVDiff'
  input = 'simple_fluid_hr.i'
  csvdiff = 'simple_fluid_hr_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to use equations of state from the FluidProperties module for a single-component fluid and specify the time unit in hours"
  issues = "#13154"
  design = 'PorousFlowSingleComponentFluid.md'
[../]


[./simple_fluid_yr]
  type = 'CSVDiff'
  input = 'simple_fluid_yr.i'
  csvdiff = 'simple_fluid_yr_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to use equations of state from the FluidProperties module for a single-component fluid and specify the time unit in years"
  issues = "#13154"
  design = 'PorousFlowSingleComponentFluid.md'
[../]


[./simple_fluid_yr_MPa_C]
  type = 'CSVDiff'
  input = 'simple_fluid_yr_MPa_C.i'
  csvdiff = 'simple_fluid_yr_MPa_C_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to use equations of state from the FluidProperties module for a single-component fluid and specify the time unit in years, the pressure unit in MPa and the temperature unit in Celsius"
  issues = "#13154"
  design = 'PorousFlowSingleComponentFluid.md'
[../]


[./simple_fluid_yr_MPa_C_action]
  type = 'CSVDiff'
  input = 'simple_fluid_yr_MPa_C_action.i'
  prereq = simple_fluid_yr_MPa_C
  csvdiff = 'simple_fluid_yr_MPa_C_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to use equations of state from the FluidProperties module for a single-component fluid and specify the time unit in years, the pressure unit in MPa and the temperature unit in Celsius, and this functionality shall be available through the PorousFlowActions"
  issues = "#13154 #16841"
  design = 'PorousFlowSingleComponentFluid.md PorousFlowFullySaturated.md'
[../]

[./waterncg_liquid]
  type = 'Exodiff'
  input = 'waterncg.i'
  exodiff = 'waterncg_liquid.e'
  threading = '!pthreads'
  requirement = 'PorousFlow shall calculate the properties of the liquid phase in a water and NCG system'
  design = 'PorousFlowWaterNCG.md'
  issues = '#8818'
[../]


[./waterncg_twophase]
  type = 'Exodiff'
  input = 'waterncg.i'
  exodiff = 'waterncg_twophase.e'
  cli_args = 'Variables/z/initial_condition=0.25 Outputs/file_base=waterncg_twophase'
  threading = '!pthreads'
  requirement = 'PorousFlow shall calculate the solubilities and properties of both the gas and liquid phase in a water and NCG system'
  design = 'PorousFlowWaterNCG.md'
  issues = '#8818'
[../]


[./waterncg_gas]
  type = 'Exodiff'
  input = 'waterncg.i'
  exodiff = 'waterncg_gas.e'
  cli_args = 'Variables/z/initial_condition=0.999 Outputs/file_base=waterncg_gas'
  threading = '!pthreads'
  requirement = 'PorousFlow shall calculate the properties of the gas phase in a water and NCG system'
  design = 'PorousFlowWaterNCG.md'
  issues = '#8818'
[../]


[./theis]
  type = 'CSVDiff'
  input = 'theis.i'
  csvdiff = "theis_csvout.csv"
  threading = '!pthreads'
  requirement = 'PorousFlow shall evolve a gas phase as a gas component is added in a water and NCG system'
  design = 'PorousFlowWaterNCG.md'
  issues = '#8818'
[../]


[./theis_tabulated]
  type = 'CSVDiff'
  input = 'theis_tabulated.i'
  csvdiff = "theis_tabulated_csvout.csv theis_tabulated_csvout_line_0010.csv"
  threading = '!pthreads'
  requirement = 'PorousFlow shall evolve a gas phase as a gas component is added in a water and NCG system'
  design = 'PorousFlowWaterNCG.md'
  issues = '#8818'
[../]


[./theis_nonisothermal]
  type = 'CSVDiff'
  input = 'theis_nonisothermal.i'
  csvdiff = "theis_nonisothermal_out.csv"
  threading = '!pthreads'
  requirement = 'PorousFlow shall evolve a gas phase as a gas component is added in a nonisothermal water and NCG system'
  design = 'PorousFlowWaterNCG.md'
  issues = '#8818 #10167'
[../]


[./brineco2]
  type = 'CSVDiff'
  input = 'brineco2.i'
  csvdiff = 'brineco2.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall calculate the solubilities and properties of both the gas and liquid phase in a brine and CO2 system'
  design = 'PorousFlowBrineCO2.md'
  issues = '#8818'
[../]


[./brineco2_2]
  type = 'CSVDiff'
  input = 'brineco2_2.i'
  csvdiff = 'brineco2_2.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall evolve a gas phase as CO2 is added to a liquid brine phase'
  design = 'PorousFlowBrineCO2.md'
  issues = '#8818'
[../]


[./brineco2_hightemp]
  type = 'CSVDiff'
  input = 'brineco2_hightemp.i'
  csvdiff = 'brineco2_hightemp_out.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall evolve a gas phase as CO2 is added to a liquid brine phase in the high temperature regime'
  design = 'PorousFlowBrineCO2.md'
  issues = '#8818 #11359'
[../]


[./theis_brineco2]
  type = 'CSVDiff'
  input = 'theis_brineco2.i'
  csvdiff = "theis_brineco2_csvout.csv theis_brineco2_csvout_line_0028.csv"
  heavy = true
  max_time = 1000
  threading = '!pthreads'
  requirement = 'PorousFlow shall evolve a gas phase as CO2 is added to a liquid brine phase'
  design = 'PorousFlowBrineCO2.md'
  issues = '#8818'
[../]


[./theis_brineco2_nonisothermal]
  type = 'CSVDiff'
  input = 'theis_brineco2_nonisothermal.i'
  csvdiff = "theis_brineco2_nonisothermal_out.csv"
  threading = '!pthreads'
  requirement = 'PorousFlow shall evolve a gas phase as CO2 is added to a liquid brine phase in a nonisothermal model'
  design = 'PorousFlowBrineCO2.md'
  issues = '#8818 #10167'
[../]


[./waterncg_ic]
  type = 'CSVDiff'
  input = 'waterncg_ic.i'
  csvdiff = "waterncg_ic_out.csv"
  threading = '!pthreads'
  requirement = 'PorousFlow shall calculate the initial value of total mass fraction corresponding to the specified gas saturation in a water and NCG system'
  design = 'PorousFlowFluidStateWaterNCGIC.md'
  issues = '#9377'
[../]


[./brineco2_ic]
  type = 'CSVDiff'
  input = 'brineco2_ic.i'
  csvdiff = "brineco2_ic_out.csv"
  threading = '!pthreads'
  requirement = 'PorousFlow shall calculate the initial value of total mass fraction corresponding to the specified gas saturation in a brine and CO2 system'
  design = 'PorousFlowFluidStateBrineCO2IC.md'
  issues = '#9377'
[../]


[./water_vapor_2phase]
  type = 'CSVDiff'
  input = 'water_vapor.i'
  csvdiff = 'water_vapor_twophase.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall calculate the properties of both the gas and liquid phase in a water-steam system'
  design = 'PorousFlowWaterVapor.md'
  issues = '#13108'
[../]


[./water_vapor_liquid]
  type = 'CSVDiff'
  input = 'water_vapor.i'
  cli_args = '/Variables/h/initial_condition=5e5 /Outputs/file_base=water_vapor_liquid'
  csvdiff = 'water_vapor_liquid.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall calculate the liquid properties in a saturated liquid system'
  design = 'PorousFlowWaterVapor.md'
  issues = '#13108'
[../]


[./water_vapor_gas]
  type = 'CSVDiff'
  input = 'water_vapor.i'
  cli_args = '/Variables/h/initial_condition=3e6 /Outputs/file_base=water_vapor_gas'
  csvdiff = 'water_vapor_gas.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall calculate the gas properties in a saturated gas system'
  design = 'PorousFlowWaterVapor.md'
  issues = '#13108'
[../]


[./water_vapor_phase_change]
  type = 'CSVDiff'
  input = 'water_vapor_phasechange.i'
  csvdiff = 'water_vapor_phasechange_out.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall evolve a vapor phase as conditions enter the two phase region'
  design = 'PorousFlowWaterVapor.md'
  issues = '#13108'
[../]


[./geothermal_1d]
  type = 'CSVDiff'
  input = 'coldwater_injection.i'
  csvdiff = 'coldwater_injection_csv_line_0007.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall calculate the temperature profile in a 1D Avdonin problem'
  design = 'PorousFlowWaterVapor.md'
  issues = '#13108'
[../]


[./geothermal_1d_radial]
  type = 'CSVDiff'
  input = 'coldwater_injection_radial.i'
  csvdiff = 'coldwater_injection_radial_csv_line_0005.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall calculate the temperature profile in a 1D radial Avdonin problem'
  design = 'PorousFlowWaterVapor.md'
  issues = '#13108'
  rel_err = 4e-5
[../]

[./except_01]
  type = 'RunException'
  input = 'except_01.i'
  expect_err = "The AdvectiveFluxCalculator UserObject fluo execute_on parameter must include, at least, 'linear'.  This is to ensure that this UserObject computes all necessary quantities just before the Kernels evaluate their Residuals"
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization, and shall error-out if the flux-limiting computations are not evaluated on linear'
[../]


[./jacobian_01]
  type = 'PetscJacobianTester'
  input = 'jacobian_01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  heavy = true
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries when there is no antidiffusion'
[../]


[./jacobian_02_minmod]
  type = 'PetscJacobianTester'
  input = 'jacobian_02.i'
  cli_args = 'UserObjects/fluo/flux_limiter_type=minmod'
  ratio_tol = 1E-7
  difference_tol = 1E10
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries when the flux limiter is minmod'
[../]


[./jacobian_02_vanleer]
  type = 'PetscJacobianTester'
  input = 'jacobian_02.i'
  cli_args = 'UserObjects/fluo/flux_limiter_type=vanleer'
  ratio_tol = 1E-7
  difference_tol = 1E10
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries when the flux limiter is vanleer'
[../]


[./jacobian_02_mc]
  type = 'PetscJacobianTester'
  input = 'jacobian_02.i'
  cli_args = 'UserObjects/fluo/flux_limiter_type=mc'
  ratio_tol = 1E-7
  difference_tol = 1E10
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries when the flux limiter is mc'
[../]


[./jacobian_02_superbee]
  type = 'PetscJacobianTester'
  input = 'jacobian_02.i'
  cli_args = 'UserObjects/fluo/flux_limiter_type=superbee'
  ratio_tol = 1E-7
  difference_tol = 1E10
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries when the flux limiter is superbee'
[../]


[./jacobian_02_vanleer_threads]
  type = 'PetscJacobianTester'
  input = 'jacobian_02.i'
  cli_args = 'UserObjects/fluo/flux_limiter_type=vanleer'
  ratio_tol = 1E-7
  difference_tol = 1E10
  min_threads = 3
  max_threads = 3
  prereq = jacobian_02_vanleer
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries, for more than 1 thread'
[../]


[./jacobian_03_vanleer]
  type = 'PetscJacobianTester'
  input = 'jacobian_03.i'
  cli_args = 'UserObjects/fluo/flux_limiter_type=vanleer'
  ratio_tol = 1E-7
  difference_tol = 1E10
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries when the flux limiter is vanleer, when the variable is such that the flux limiter is 1'
[../]


[./jacobian_03_mc]
  type = 'PetscJacobianTester'
  input = 'jacobian_03.i'
  cli_args = 'UserObjects/fluo/flux_limiter_type=mc'
  ratio_tol = 1E-7
  difference_tol = 1E10
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization, and shall fully compute all Jacobian entries when the flux limiter is mc, when the variable is such that the flux limiter is 1'
[../]


[./fltvd_1D]
  type = 'CSVDiff'
  input = 'fltvd_1D.i'
  csvdiff = 'fltvd_1D_out_tracer_0101.csv'
  abs_zero = 1.0E-5
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 1D'
[../]


[./fltvd_1D_threads]
  type = 'CSVDiff'
  input = 'fltvd_1D.i'
  csvdiff = 'fltvd_1D_out_tracer_0101.csv'
  abs_zero = 1.0E-5
  min_threads = 3
  max_threads = 3
  prereq = fltvd_1D
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 1D with more than 1 thread'
[../]


[./fltvd_2D]
  type = 'CSVDiff'
  input = 'fltvd_2D.i'
  csvdiff = 'fltvd_2D_out_tracer_0101.csv'
  abs_zero = 1.0E-5
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 2D'
[../]


[./fltvd_2D_threads]
  type = 'CSVDiff'
  input = 'fltvd_2D.i'
  csvdiff = 'fltvd_2D_out_tracer_0101.csv'
  abs_zero = 1.0E-5
  min_threads = 3
  max_threads = 3
  prereq = 'fltvd_1D_threads fltvd_2D'
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 2D with more than 1 thread'
[../]


[./fltvd_3D]
  type = 'CSVDiff'
  input = 'fltvd_3D.i'
  csvdiff = 'fltvd_3D_out_tracer_0101.csv'
  abs_zero = 1.0E-5
  heavy = true
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 3D'
[../]


[./fltvd_2D_angle]
  type = Exodiff
  input = 'fltvd_2D_angle.i'
  exodiff = 'fltvd_2D_angle_out.e'
  abs_zero = 4.0E-4
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 2D when the velocity is not aligned with the mesh'
[../]


[./fltvd_2D_trimesh]
  type = 'CSVDiff'
  input = 'fltvd_2D_trimesh.i'
  csvdiff = 'fltvd_2D_trimesh_out_tracer_0101.csv'
  heavy = true
  abs_zero = 1.0E-5
  max_time = 1000
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 2D when using triangular mesh elements'
[../]


[./fltvd_2D_trimesh_threads]
  type = 'CSVDiff'
  input = 'fltvd_2D_trimesh.i'
  csvdiff = 'fltvd_2D_trimesh_out_tracer_0101.csv'
  heavy = true
  max_time = 1000
  min_threads = 3
  max_threads = 3
  prereq = 'fltvd_2D_trimesh'
  abs_zero = 1.0E-5
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 2D when using triangular mesh elements and with more than 1 thread'
[../]


[./fltvd_2D_blocks]
  type = 'CSVDiff'
  input = 'fltvd_2D_blocks.i'
  csvdiff = 'fltvd_2D_blocks_out_tracer_bot_0101.csv fltvd_2D_blocks_out_tracer_top_0101.csv'
  abs_zero = 1.0E-5
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 2D when the advection is block limited'
[../]


[./fltvd_2D_blocks_threads]
  type = 'CSVDiff'
  input = 'fltvd_2D_blocks.i'
  csvdiff = 'fltvd_2D_blocks_out_tracer_bot_0101.csv fltvd_2D_blocks_out_tracer_top_0101.csv'
  abs_zero = 1.0E-5
  min_threads = 3
  max_threads = 3
  prereq = 'fltvd_1D_threads fltvd_2D_blocks'
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 2D when the advection is block limited, and when more than 1 thread is used'
[../]


[./fltvd_1D_adaptivity]
  type = 'CSVDiff'
  input = 'fltvd_1D_adaptivity.i'
  csvdiff = 'fltvd_1D_adaptivity_out_tracer_0101.csv'
  abs_zero = 1.0E-5
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 1D when mesh adaptivity is used'
[../]


[./fltvd_1D_adaptivity_threads]
  type = 'CSVDiff'
  input = 'fltvd_1D_adaptivity.i'
  csvdiff = 'fltvd_1D_adaptivity_out_tracer_0101.csv'
  abs_zero = 1.0E-5
  min_threads = 3
  max_threads = 3
  prereq = 'fltvd_1D_threads fltvd_1D_adaptivity'
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 1D when mesh adaptivity is used, and when more than 1 thread is used'
[../]

[./except01]
  type = 'RunException'
  input = 'except01.i'
  expect_err = "Phase number entered is greater than the number of phases specified in the Dictator. Remember that indexing starts at 0"
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall error-out if the specified phase number >= number of phases in the model, when using Kuzmin-Turek stabilization'
[../]


[./except02]
  type = 'RunException'
  input = 'except02.i'
  expect_err = "Fluid component number entered is greater than the number of fluid components specified in the Dictator. Remember that indexing starts at 0"
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall error-out if the specified fluid component number >= number of fluid components in the model, when using Kuzmin-Turek stabilization'
[../]


[./except03]
  type = 'RunException'
  input = 'except03.i'
  expect_err = "fe_order: If you specify fe_family you must also specify fe_order"
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall error-out if the fe_family is specified but not fe_order, when using Kuzmin-Turek stabilization'
[../]


[./except04]
  type = 'RunException'
  input = 'except04.i'
  expect_err = "fe_family: If you specify fe_order you must also specify fe_family"
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow error-out if the fe_order is specified but not fe_family, when using Kuzmin-Turek stabilization'
[../]


[./except05]
  type = 'RunException'
  input = 'except05.i'
  expect_err = "fe_family: The PorousFlowDictator cannot determine the appropriate FE type to use because your porous_flow_vars are of different types.  You must specify the appropriate fe_family and fe_order to use."
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall error-out if the PorousFlowDictator cannot determine a consistent FE type to use and if no FE type is specified, when using Kuzmin-Turek stabilization'
[../]


[./jacobian_01]
  type = 'PetscJacobianTester'
  input = 'jacobian_01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  heavy = true
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall compute all Jacobian entries when there is no antidiffusion in Kuzmin-Turek stabilized PorousFlow simulations involving full saturation of 1 phase and 1 component'
[../]


[./jacobian_01_threads]
  type = 'PetscJacobianTester'
  input = 'jacobian_01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  heavy = true
  min_threads = 3
  max_threads = 3
  prereq = jacobian_01
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall compute all Jacobian entries when there is no antidiffusion in Kuzmin-Turek stabilized PorousFlow simulations involving full saturation of 1 phase and 1 component, when using more than 1 thread'
[../]


[./jacobian_02]
  type = 'PetscJacobianTester'
  input = 'jacobian_02.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall compute all Jacobian entries when there is no antidiffusion in Kuzmin-Turek stabilized PorousFlow simulations involving 1 unsaturated fluid phase with multiple components'
[../]


[./jacobian_03]
  type = 'PetscJacobianTester'
  input = 'jacobian_03.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  heavy = true
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall compute all Jacobian entries when there is no antidiffusion in Kuzmin-Turek stabilized PorousFlow simulations involving multiple fluid phases and multiple fluid components'
[../]


[./jacobian_03_threads]
  type = 'PetscJacobianTester'
  input = 'jacobian_03.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  heavy = true
  threading = '!pthreads'
  issues = '#10426'
  min_threads = 3
  max_threads = 3
  prereq = jacobian_03
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall compute all Jacobian entries when there is no antidiffusion in Kuzmin-Turek stabilized PorousFlow simulations involving multiple fluid phases and multiple fluid components, when using more than 1 thread'
[../]


[./jacobian_04_minmod]
  type = 'PetscJacobianTester'
  input = 'jacobian_04.i'
  cli_args = 'UserObjects/advective_flux_calculator/flux_limiter_type=minmod'
  heavy = true
  ratio_tol = 1E-7
  difference_tol = 1E10
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall compute all Jacobian entries when the flux limiter is minmod in Kuzmin-Turek stabilized PorousFlow simulations involving full saturation of 1 phase and 1 component'
[../]


[./jacobian_04_vanleer]
  type = 'PetscJacobianTester'
  input = 'jacobian_04.i'
  cli_args = 'UserObjects/advective_flux_calculator/flux_limiter_type=vanleer'
  ratio_tol = 1E-7
  difference_tol = 1E10
  heavy = true
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall compute all Jacobian entries when the flux limiter is vanleer in Kuzmin-Turek stabilized PorousFlow simulations involving full saturation of 1 phase and 1 component'
[../]


[./jacobian_04_mc]
  type = 'PetscJacobianTester'
  input = 'jacobian_04.i'
  cli_args = 'UserObjects/advective_flux_calculator/flux_limiter_type=mc'
  ratio_tol = 1E-7
  difference_tol = 1E10
  heavy = true
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall compute all Jacobian entries when the flux limiter is mc in Kuzmin-Turek stabilized PorousFlow simulations involving full saturation of 1 phase and 1 component'
[../]


[./jacobian_04_superbee]
  type = 'PetscJacobianTester'
  input = 'jacobian_04.i'
  cli_args = 'UserObjects/advective_flux_calculator/flux_limiter_type=superbee'
  ratio_tol = 1E-7
  difference_tol = 1E10
  heavy = true
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall compute all Jacobian entries when the flux limiter is superbee in Kuzmin-Turek stabilized PorousFlow simulations involving full saturation of 1 phase and 1 component'
[../]


[./jacobian_04_vanleer_threads]
  type = 'PetscJacobianTester'
  input = 'jacobian_04.i'
  cli_args = 'UserObjects/advective_flux_calculator/flux_limiter_type=vanleer'
  ratio_tol = 1E-7
  difference_tol = 1E10
  threading = '!pthreads'
  issues = '#10426'
  heavy = true
  min_threads = 3
  max_threads = 3
  prereq = jacobian_04_vanleer
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall compute all Jacobian entries when the flux limiter is vanleer in Kuzmin-Turek stabilized PorousFlow simulations involving full saturation of 1 phase and 1 component, when using more than 1 thread'
[../]


[./jacobian_05]
  type = 'PetscJacobianTester'
  input = 'jacobian_05.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall compute all Jacobian entries when using any non-trivial flux limiter in Kuzmin-Turek stabilized PorousFlow simulations involving multiple phases and multiple components'
[../]


[./jacobian_05_threads]
  type = 'PetscJacobianTester'
  input = 'jacobian_05.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  min_threads = 3
  max_threads = 3
  prereq = jacobian_05
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall compute all Jacobian entries when using any non-trivial flux limiter in Kuzmin-Turek stabilized PorousFlow simulations involving multiple phases and multiple components, when using more than 1 thread'
[../]


[./pffltvd_1D]
  type = 'CSVDiff'
  input = 'pffltvd_1D.i'
  csvdiff = 'pffltvd_1D_out_tracer_0101.csv'
  abs_zero = 1.0E-5
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 1D for PorousFlow simulations'
[../]


[./pffltvd_1D_threads]
  type = 'CSVDiff'
  input = 'pffltvd_1D.i'
  csvdiff = 'pffltvd_1D_out_tracer_0101.csv'
  abs_zero = 1.0E-5
  threading = '!pthreads'
  issues = '#10426'
  min_threads = 3
  max_threads = 3
  prereq = pffltvd_1D
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 1D for PorousFlow simulations, for more than 1 thread'
[../]


[./pffltvd_2D]
  type = 'CSVDiff'
  input = 'pffltvd_2D.i'
  csvdiff = 'pffltvd_2D_out_tracer_0011.csv'
  cli_args = 'Executioner/end_time=0.6'
  abs_zero = 1.0E-5
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 2D for PorousFlow simulations'
[../]


[./pffltvd_2D_threads]
  type = 'CSVDiff'
  input = 'pffltvd_2D.i'
  csvdiff = 'pffltvd_2D_out_tracer_0011.csv'
  cli_args = 'Executioner/end_time=0.6'
  abs_zero = 1.0E-5
  threading = '!pthreads'
  issues = '#10426'
  min_threads = 3
  max_threads = 3
  prereq = 'pffltvd_1D_threads pffltvd_2D'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 2D for PorousFlow simulations, for more than 1 thread'
[../]


[./memory_inefficiency]
  type = 'RunException'
  input = 'pffltvd_2D.i'
  prereq = 'pffltvd_1D_threads pffltvd_2D pffltvd_2D_threads'
  expect_err = "In at least one processor, the sequential node-numbering internal data structure used in advective_flux_calculator_0 is using memory inefficiently.\nThe memory wasted is 4.57764e-05 megabytes.\n  The node-numbering data structure has been optimized for speed at the expense of memory, but that may not be an appropriate optimization for your case, because the node numbering is not close to sequential in your case."
  threading = '!pthreads'
  cli_args = 'UserObjects/advective_flux_calculator_0/allowable_MB_wastage=0.000001'
  min_parallel = 2
  max_parallel = 2
  issues = '#13078'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall issue a warning if the memory is inefficiently used for multi-processor simulations involving Kuzmin-Turek stablization'
[../]


[./pffltvd_3D]
  type = 'CSVDiff'
  input = 'pffltvd_3D.i'
  csvdiff = 'pffltvd_3D_out_tracer_0006.csv'
  cli_args = 'Executioner/end_time=0.3'
  heavy = true
  abs_zero = 1.0E-5
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 2D for PorousFlow simulations'
[../]


[./pffltvd_2D_angle]
  type = Exodiff
  input = 'pffltvd_2D_angle.i'
  exodiff = 'pffltvd_2D_angle_out.e'
  abs_zero = 4.0E-4
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 2D for PorousFlow simulations, when the Darcy velocity is not aligned with the mesh'
[../]


[./pffltvd_2D_trimesh]
  type = CSVDiff
  input = 'pffltvd_2D_trimesh.i'
  csvdiff = 'pffltvd_2D_trimesh_out_tracer_0006.csv'
  cli_args = 'Executioner/end_time=0.3'
  heavy = true
  abs_zero = 1.0E-5
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 2D for PorousFlow simulations, when using triangular mesh elements'
[../]


[./pffltvd_2D_trimesh_threads]
  type = CSVDiff
  input = 'pffltvd_2D_trimesh.i'
  csvdiff = 'pffltvd_2D_trimesh_out_tracer_0006.csv'
  cli_args = 'Executioner/end_time=0.3'
  heavy = true
  min_threads = 3
  max_threads = 3
  prereq = 'pffltvd_2D_trimesh'
  abs_zero = 1.0E-5
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 2D for PorousFlow simulations, when using triangular mesh elements, and more than 1 thread'
[../]


[./pffltvd_1D_adaptivity]
  type = 'CSVDiff'
  input = 'pffltvd_1D_adaptivity.i'
  csvdiff = 'pffltvd_1D_adaptivity_out_tracer_0101.csv'
  abs_zero = 1.0E-5

  max_threads = 1 # See issue #14558
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization in 1D for PorousFlow simulations when mesh adaptivity is used'
[../]

[./grav01a]
  type = 'CSVDiff'
  input = 'grav01a.i'
  csvdiff = 'grav01a.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations"
  issues = '#6845 #7677 #8073 #8585 #8574 #9537'
  design = 'porous_flow/governing_equations.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./grav01b]
  type = 'CSVDiff'
  input = 'grav01b.i'
  csvdiff = 'grav01b.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations"
  issues = '#6845 #7677 #8073 #8585 #8574 #9537'
  design = 'porous_flow/governing_equations.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./grav01c]
  type = 'CSVDiff'
  input = 'grav01c.i'
  csvdiff = 'grav01c.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations"
  issues = '#6845 #7677 #8073 #8585 #8574 #9537'
  design = 'porous_flow/governing_equations.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./grav01c_action]
  type = 'CSVDiff'
  input = 'grav01c_action.i'
  csvdiff = 'grav01c_action.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations"
  issues = '#6845 #7677 #8073 #8585 #8574 #9537'
  design = 'porous_flow/governing_equations.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./grav02a]
  type = 'CSVDiff'
  input = 'grav02a.i'
  csvdiff = 'grav02a.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations"
  issues = '#6845 #7677 #8073 #8585 #8574 #9537'
  design = 'porous_flow/governing_equations.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./grav02b]
  type = 'CSVDiff'
  input = 'grav02b.i'
  csvdiff = 'grav02b.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations"
  issues = '#6845 #7677 #8073 #8585 #8574 #9537'
  design = 'porous_flow/governing_equations.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./grav02c]
  type = 'CSVDiff'
  input = 'grav02c.i'
  csvdiff = 'grav02c.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations"
  issues = '#6845 #7677 #8073 #8585 #8574 #9537'
  design = 'porous_flow/governing_equations.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./grav02d]
  type = 'CSVDiff'
  input = 'grav02d.i'
  csvdiff = 'grav02d.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations"
  issues = '#6845 #7677 #8073 #8585 #8574 #9537'
  design = 'porous_flow/governing_equations.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./grav02e]
  type = 'Exodiff'
  input = 'grav02e.i'
  exodiff = 'grav02e.e'
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations"
  issues = '#6845 #7677 #8073 #8585 #8574 #9537'
  design = 'porous_flow/governing_equations.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./grav02f]
  type = 'Exodiff'
  input = 'grav02f.i'
  exodiff = 'grav02f.e'
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations"
  issues = '#6845 #7677 #8073 #8585 #8574 #9537'
  design = 'porous_flow/governing_equations.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./grav02g]
  type = 'Exodiff'
  input = 'grav02g.i'
  exodiff = 'grav02g.e'
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations"
  issues = '#6845 #7677 #8073 #8585 #8574 #9537'
  design = 'porous_flow/governing_equations.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./fully_saturated_grav01a]
  type = 'CSVDiff'
  input = 'fully_saturated_grav01a.i'
  csvdiff = 'fully_saturated_grav01a.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations"
  issues = '#6845 #7677 #8073 #8585 #8574 #9537'
  design = 'porous_flow/governing_equations.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./fully_saturated_grav01b]
  type = 'CSVDiff'
  input = 'fully_saturated_grav01b.i'
  csvdiff = 'fully_saturated_grav01b.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations"
  issues = '#6845 #7677 #8073 #8585 #8574 #9537'
  design = 'porous_flow/governing_equations.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./fully_saturated_grav01c]
  type = 'CSVDiff'
  input = 'fully_saturated_grav01c.i'
  csvdiff = 'fully_saturated_grav01c.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  max_parallel = 1
  requirement = "PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero: for single-phase fully-saturated, single-phase partially-saturated, two-phase PP formulations, and two-phase PS formulations"
  issues = '#6845 #7677 #8073 #8585 #8574 #9537 #12505'
  design = 'porous_flow/governing_equations.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./fully_saturated_upwinded_grav01c]
  type = 'CSVDiff'
  input = 'fully_saturated_upwinded_grav01c.i'
  cli_args = 'Outputs/file_base=fsupg'
  csvdiff = 'fsupg.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  max_parallel = 1
  requirement = "PorousFlow shall be able to find steady-state porepressure for single-phase, fully-saturated, multicomponent systems"
  issues = '#16841'
  design = 'PorousFlowFullySaturatedAdvectiveFlux.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./fully_saturated_upwinded_nodens_grav01c]
  type = 'CSVDiff'
  input = 'fully_saturated_upwinded_grav01c.i'
  prereq = fully_saturated_upwinded_grav01c
  cli_args = 'Outputs/file_base=fsupg Kernels/flux0/multiply_by_density=false Kernels/flux1/multiply_by_density=false'
  csvdiff = 'fsupg.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  max_parallel = 1
  requirement = "PorousFlow shall be able to find steady-state porepressure for single-phase, fully-saturated, multicomponent systems, if the Darcy flow is expressed in terms of fluid volumes"
  issues = '#16841'
  design = 'PorousFlowFullySaturatedAdvectiveFlux.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./fully_saturated_upwinded_grav01c_action]
  type = 'CSVDiff'
  input = 'fully_saturated_upwinded_grav01c_action.i'
  prereq = fully_saturated_upwinded_nodens_grav01c
  cli_args = 'Outputs/file_base=fsupg'
  csvdiff = 'fsupg.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  max_parallel = 1
  requirement = "PorousFlow shall be able to find steady-state porepressure for single-phase, fully-saturated, multicomponent systems, when using an action"
  issues = '#16841'
  design = 'PorousFlowFullySaturated.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./fully_saturated_upwinded_nodens_grav01c_action]
  type = 'CSVDiff'
  input = 'fully_saturated_upwinded_nodens_grav01c_action.i'
  prereq = fully_saturated_upwinded_grav01c_action
  cli_args = 'Outputs/file_base=fsupg'
  csvdiff = 'fsupg.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  max_parallel = 1
  requirement = "PorousFlow shall be able to find steady-state porepressure for single-phase, fully-saturated, multicomponent systems, when using an action and a fluid-volume calculation"
  issues = '#16841'
  design = 'PorousFlowFullySaturated.md porous_flow/tests/gravity/gravity_tests.md'
[../]


[./grav01d]
  type = 'CSVDiff'
  input = 'grav01d.i'
  csvdiff = 'grav01d.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to find steady-state and long-time transient porepressure when gravity is nonzero, when the simulation contains more than one domain, with each domain having its own capillary pressure and relative permeability function"
  issues = '#13116'
  design = 'porous_flow/governing_equations.md porous_flow/tests/gravity/gravity_tests.md'
[../]

[./except1]
  type = RunException
  input = except1.i
  expect_err = "PorousFlowFullySaturatedUpwindHeatAdvection should not be used for multi-phase scenarios as it does not include relative-permeability effects"
  threading = '!pthreads'
  issues = '#16841'
  design = 'PorousFlowFullySaturatedUpwindHeatAdvection.md'
  requirement = 'PorousFlow shall produce an error when the kernel describing heat advection by a single-phase fluid is used in a multi-phase situation'
[../]


[./heat_advection_1d_fully_saturated]
  type = CSVDiff
  input = heat_advection_1d_fully_saturated.i
  csvdiff = 'heat_advection_1d_fully_saturated_T_0010.csv heat_advection_1d_fully_saturated_T_0060.csv'
  threading = '!pthreads'
  issues = '#7984'
  design = 'PorousFlowHeatAdvection.md PorousFlowEnergyTimeDerivative.md porous_flow/tests/heat_advection/heat_advection_tests.md'
  requirement = 'PorousFlow shall correctly advect heat energy with a moving fluid, using no numerical stabilization'
[../]


[./heat_advection_1d_fully_saturated_action_none]
  type = CSVDiff
  input = heat_advection_1d_fully_saturated_action.i
  prereq = heat_advection_1d_fully_saturated
  cli_args = 'PorousFlowFullySaturated/stabilization=none Outputs/file_base=heat_advection_1d_fully_saturated'
  csvdiff = 'heat_advection_1d_fully_saturated_T_0010.csv heat_advection_1d_fully_saturated_T_0060.csv'
  threading = '!pthreads'
  issues = '#10426'
  design = 'PorousFlowFullySaturated.md porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/tests/heat_advection/heat_advection_tests.md'
  requirement = 'PorousFlow shall correctly advect heat energy with a moving fluid, using no numerical stabilization, and the user should be able to activiate this stabilization using the PorousFlow Action system'
[../]


[./heat_advection_1d]
  type = CSVDiff
  input = heat_advection_1d.i
  csvdiff = 'heat_advection_1d_csv_T_0010.csv heat_advection_1d_csv_T_0060.csv'
  threading = '!pthreads'
  issues = '#7984'
  design = 'PorousFlowHeatAdvection.md PorousFlowEnergyTimeDerivative.md porous_flow/tests/heat_advection/heat_advection_tests.md'
  requirement = 'PorousFlow shall correctly advect heat energy with a moving fluid, using full-upwinding for numerical stabilization'
[../]


[./heat_advection_1d_fullsat]
  type = CSVDiff
  input = heat_advection_1d_fullsat.i
  prereq = heat_advection_1d
  cli_args = 'Outputs/file_base=heat_advection_1d_csv'
  csvdiff = 'heat_advection_1d_csv_T_0010.csv heat_advection_1d_csv_T_0060.csv'
  threading = '!pthreads'
  issues = '#16841'
  design = 'PorousFlowFullySaturatedUpwindHeatAdvection.md PorousFlowEnergyTimeDerivative.md porous_flow/tests/heat_advection/heat_advection_tests.md'
  requirement = 'PorousFlow shall correctly advect heat energy with a moving fluid, using full-upwinding for numerical stabilization, in fully-saturated single-phase systems'
[../]


[./heat_advection_1d_fully_saturated_action_full]
  type = CSVDiff
  input = heat_advection_1d_fully_saturated_action.i
  prereq = heat_advection_1d_fullsat
  cli_args = 'PorousFlowFullySaturated/stabilization=Full Outputs/file_base=heat_advection_1d_csv'
  csvdiff = 'heat_advection_1d_csv_T_0010.csv heat_advection_1d_csv_T_0060.csv'
  threading = '!pthreads'
  issues = '#16841'
  design = 'PorousFlowFullySaturated.md PorousFlowEnergyTimeDerivative.md porous_flow/tests/heat_advection/heat_advection_tests.md'
  requirement = 'PorousFlow shall correctly advect heat energy with a moving fluid, using full-upwinding for numerical stabilization, in fully-saturated single-phase systems, and the user should be able to activiate this stabilization using the PorousFlow Action system'
[../]


[./heat_advection_1d_KT]
  type = CSVDiff
  input = heat_advection_1d_KT.i
  csvdiff = 'heat_advection_1d_KT_T_0010.csv heat_advection_1d_KT_T_0060.csv'
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/tests/heat_advection/heat_advection_tests.md'
  requirement = 'PorousFlow shall correctly advect heat energy with a moving fluid, using the Kuzmin-Turek for numerical stabilization'
[../]


[./heat_advection_1d_fully_saturated_action_KT]
  type = CSVDiff
  input = heat_advection_1d_fully_saturated_action.i
  prereq = heat_advection_1d_KT
  cli_args = 'PorousFlowFullySaturated/stabilization=KT Outputs/file_base=heat_advection_1d_KT'
  csvdiff = 'heat_advection_1d_KT_T_0010.csv heat_advection_1d_KT_T_0060.csv'
  threading = '!pthreads'
  issues = '#10426'
  design = 'PorousFlowFullySaturated.md porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/tests/heat_advection/heat_advection_tests.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization for PorousFlow simulations involving the advection of heat energy in a moving fluid, and the user should be able to activiate this stabilization using the PorousFlow Action system'
[../]


[./heat_advection_1d_KT_threads]
  type = CSVDiff
  input = heat_advection_1d_KT.i
  cli_args = 'Outputs/file_base=heat_advection_1d_KT_threads'
  csvdiff = 'heat_advection_1d_KT_threads_T_0010.csv heat_advection_1d_KT_threads_T_0060.csv'
  min_threads = 3
  max_threads = 3
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/tests/heat_advection/heat_advection_tests.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization for PorousFlow simulations involving the advection of heat energy in a moving fluid'
[../]

[./no_fluid]
  type = 'CSVDiff'
  input = 'no_fluid.i'
  csvdiff = 'no_fluid.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to simulate heat conduction in a fluid-free environment'
  design = 'porous_flow/tests/heat_conduction/heat_conduction_tests.md'
  issues = '#13155'
[../]


[./two_phase]
  type = 'CSVDiff'
  input = 'two_phase.i'
  csvdiff = 'two_phase.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to simulate heat conduction for systems containing multi-phase fluids'
  design = 'porous_flow/tests/heat_conduction/heat_conduction_tests.md'
  issues = '#13155'
[../]

[./testvariable_transfer_0D]
  type = 'CSVDiff'
  input = 'variable_transfer_0D.i'
  csvdiff = 'variable_transfer_0D_out.csv'
  requirement = 'PorousFlow shall be able to transfer heat or mass from one Variable to another when the transfer coefficient is a constant.'
  design = 'PorousFlowHeatMassTransfer.md'
  issues = '#11050'
[../]


[./testvariable_transfer_variable_0D]
  type = 'CSVDiff'
  input = 'variable_transfer_variable_0D.i'
  csvdiff = 'variable_transfer_variable_0D_out.csv'
  requirement = 'PorousFlow shall be able to transfer heat or mass from one Variable to another when the transfer coefficient is a variable.'
  design = 'PorousFlowHeatMassTransfer.md'
  issues = '#11050'
[../]

[./constant_poroperm]
  type = 'Exodiff'
  input = 'constant_poroperm.i'
  exodiff = 'constant_poroperm_out.e'
  threading = '!pthreads'
  requirement = "The system shall allow the assignment of porosity and permeability from an AuxVariable field."
  issues = "#8062"
  design = "PorousFlowPorosity.md"
[../]


[./constant_poroperm2]
  type = 'Exodiff'
  input = 'constant_poroperm2.i'
  exodiff = 'constant_poroperm2_out.e'
  threading = '!pthreads'
  requirement = "The system shall allow the assignment of porosity and permeability from an AuxVariable field with binlinear relationships."
  issues = "#8062"
  design = "PorousFlowPorosity.md"
[../]


[./constant_poroperm3]
  type = 'Exodiff'
  input = 'constant_poroperm3.i'
  exodiff = 'constant_poroperm2_out.e'
  prereq = constant_poroperm2
  threading = '!pthreads'
  requirement = "The system shall allow the assignment of porosity and permeability from an AuxVariable read from a mesh"
  issues = "#13478"
  design = "PorousFlowPorosity.md"
[../]


[./vol_expansion_poroperm]
  type = Exodiff
  input = vol_expansion_poroperm.i
  exodiff = vol_expansion_poroperm_out.e
  threading = '!pthreads'
  requirement = "The system shall calculate permeability from a changing porosity."
  issues = "#8062"
  design = "PorousFlowPorosity.md"
[../]

[./except01]
  type = 'RunException'
  input = 'except01.i'
  expect_err = 'The Dictator proclaims that the number of fluid phases is 1 while you have foolishly entered 1 for your liquid phase number.  Remember that indexing starts at 0.  Be aware that the Dictator does not tolerate mistakes.'
  requirement = 'If the liquid phase number exceeds the number of phases in the system, PorousFlow shall produce an appropriate error message and exit'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./except02]
  type = 'RunException'
  input = 'except02.i'
  expect_err = 'The initial order must be less than the max order, which is hard-coded to 3'
  requirement = 'The maximum order for hysteretic relative permeabilities and capillary pressures is 3 and if the user specifies an initial order greater than this amount, an error shall be thrown'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./except03]
  type = 'RunException'
  input = 'except03.i'
  expect_err = 'previous_turning_points: initial_order is 1 so there must be this many previous_turning_points'
  requirement = 'An error shall be thrown if the initial order of hysteresis is incommensurate with previous_turning_points'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./except04]
  type = 'RunException'
  input = 'except04.i'
  expect_err = 'Each previous_turning_point must lie in the range [0.0, 1.0]'
  match_literal = true
  requirement = 'An error shall be thrown if the hysteretic turning points do not lie in the range \[0, 1\]'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./except05]
  type = 'RunException'
  input = 'except05.i'
  expect_err = 'Each previous_turning_point must lie in the range [0.0, 1.0]'
  match_literal = true
  requirement = 'An error shall be thrown if the hysteretic turning points do not lie in the range \[0, 1\]'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./except06]
  type = 'RunException'
  input = 'except06.i'
  expect_err = 'The previous_turning_points vector, {a, b, c, ...}, must be obey the following order: a < 1; b > a; a < c < b, etc'
  match_literal = true
  requirement = 'An error shall be thrown if the turning points are incorrectly ordered'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./except07]
  type = 'RunException'
  input = 'except07.i'
  expect_err = 'The previous_turning_points vector, {a, b, c, ...}, must be obey the following order: a < 1; b > a; a < c < b, etc'
  match_literal = true
  requirement = 'An error shall be thrown if the turning points are incorrectly ordered'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./except08]
  type = 'RunException'
  input = 'except08.i'
  expect_err = 'The previous_turning_points vector, {a, b, c, ...}, must be obey the following order: a < 1; b > a; a < c < b, etc'
  match_literal = true
  requirement = 'An error shall be thrown if the turning points are incorrectly ordered'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./except09]
  type = 'RunException'
  input = 'except09.i'
  expect_err = 'The maximum number of hysteresis turning points is 3'
  requirement = 'An error shall be thrown if the hysteresis turning-point information is requested for the Nth turning point, when N exceeds the maximum number of turning points'
  design = 'PorousFlowHysteresisOrder.md PorousFlowPropertyAux.md'
  issues = '#16021'
[../]


[./except10]
  type = 'RunException'
  input = 'except10.i'
  expect_err = 'Must be less than 1 - S_l_min'
  match_literal = true
  requirement = 'An error shall be thrown if the maximum gas residual saturation is greater than 1 - minimum_liquid_saturation in hysteretic problems'
  design = 'hysteresis.md'
  issues = '#16129'
[../]


[./except11]
  type = 'RunException'
  input = 'except11.i'
  expect_err = 'Should be chosen sufficiently close to 1 so that the high extension does not interfere with the low extension.  Instead, you may have chosen Pc_max too low'
  match_literal = true
  requirement = 'An error shall be thrown if parameters are chosen such that the high and low extension regions of the hysteretic capillary pressure overlap'
  design = 'hysteresis.md'
  issues = '#16129'
[../]


[./except12]
  type = 'RunException'
  input = 'except12.i'
  expect_err = 'S_lr should usually be greater than S_l_min'
  match_literal = true
  cli_args = '--error'
  requirement = 'A warning shall be produced if the residual saturation is not greater than the minimum saturation in hysteretic simulations'
  design = 'hysteresis.md'
  issues = '#16129'
[../]


[./except13]
  type = 'RunException'
  input = 'except13.i'
  expect_err = 'The Dictator proclaims that the number of phases is 2 whereas PorousFlow1PhaseHysP can only be used for 1-phase simulations.  Be aware that the Dictator has noted your mistake.'
  match_literal = true
  requirement = 'An exception shall be thrown if a single-phase hysteretic capillary-pressure Material is used in situations with more than one fluid phase'
  design = 'PorousFlow1PhaseHysP.md'
  issues = '#16129'
[../]


[./except14]
  type = 'RunException'
  input = 'except14.i'
  expect_err = 'The Dictator announces that the number of phases is 1 whereas PorousFlow2PhaseHysPP can only be used for 2-phase simulation.  When you have efficient government, you have dictatorship.'
  match_literal = true
  requirement = 'An exception shall be thrown if a two-phase PP hysteretic capillary-pressure Material is used in models that do not have exactly 2 phases'
  design = 'PorousFlow2PhaseHysPP.md'
  issues = '#16260'
[../]


[./except15]
  type = 'RunException'
  input = 'except15.i'
  expect_err = 'The Dictator announces that the number of phases is 1 whereas PorousFlow2PhaseHysPS can only be used for 2-phase simulation.  The Dictator is always watching.'
  match_literal = true
  requirement = 'An exception shall be thrown if a two-phase PS hysteretic capillary-pressure Material is used in models that do not have exactly 2 phases'
  design = 'PorousFlow2PhaseHysPS.md'
  issues = '#16260'
[../]


[./except16]
  type = 'RunException'
  input = 'except16.i'
  expect_err = 'Must be less than 1 - S_lr'
  match_literal = true
  requirement = 'When using hysteretic relative permeabilities, an exception shall be thrown if the gas residual saturation is not less than 1 - liquid_residual_saturation'
  design = 'PorousFlowHystereticRelativePermeabilityLiquid.md PorousFlowHystereticRelativePermeabilityGas.md'
  issues = '#16324'
[../]


[./hys_order_01]
  type = CSVDiff
  input = 'hys_order_01.i'
  csvdiff = 'hys_order_01_csv.csv'
  requirement = 'PorousFlow shall be able to calculate the hysteresis order'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./hys_order_02]
  type = CSVDiff
  input = 'hys_order_02.i'
  csvdiff = 'hys_order_02_csv.csv'
  requirement = 'PorousFlow shall be able to calculate the hysteresis order'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./hys_order_03]
  type = CSVDiff
  input = 'hys_order_03.i'
  csvdiff = 'hys_order_03_csv.csv'
  requirement = 'PorousFlow shall be able to calculate the hysteresis order'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./hys_order_04]
  type = CSVDiff
  input = 'hys_order_04.i'
  csvdiff = 'hys_order_04_csv.csv'
  requirement = 'PorousFlow shall be able to calculate the hysteresis order and hysteresis order shall be able to be initialized to a nonzero value'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./hys_order_05]
  type = CSVDiff
  input = 'hys_order_05.i'
  csvdiff = 'hys_order_05_csv.csv'
  requirement = 'PorousFlow shall be able to calculate the hysteresis order and hysteresis order shall be able to be initialized to a nonzero value'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./hys_order_06]
  type = CSVDiff
  input = 'hys_order_06.i'
  csvdiff = 'hys_order_06_csv.csv'
  requirement = 'PorousFlow shall be able to calculate the hysteresis order and hysteresis order shall be able to be initialized to a nonzero value'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./hys_order_07]
  type = CSVDiff
  input = 'hys_order_07.i'
  csvdiff = 'hys_order_07_csv.csv'
  requirement = 'PorousFlow shall be able to calculate the hysteresis order and hysteresis order shall be able to be initialized to a nonzero value'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./hys_order_08]
  type = CSVDiff
  input = 'hys_order_08.i'
  csvdiff = 'hys_order_08_csv.csv'
  requirement = 'PorousFlow shall be able to calculate the hysteresis order and hysteresis order shall be able to be initialized to a nonzero value, and jumps of greater than 2 in hysteresis order shall be allowed within one time-step'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./hys_order_09]
  type = CSVDiff
  input = 'hys_order_09.i'
  csvdiff = 'hys_order_09_csv.csv'
  requirement = 'PorousFlow shall be able to calculate the hysteresis order and hysteresis order shall be able to be initialized to a nonzero value, and jumps of greater than 2 in hysteresis order shall be allowed within one time-step, and turning points shall be correctly identified in such situations'
  design = 'PorousFlowHysteresisOrder.md'
  issues = '#16021'
[../]


[./hys_sat_01]
  type = CSVDiff
  input = 'hys_sat_01.i'
  csvdiff = 'hys_sat_01_out_sat_0001.csv'
  requirement = 'PorousFlow shall be able to compute saturation according to the primary drying curve in hysteretic problems, using no low extension'
  design = 'PorousFlow1PhaseHysP.md'
  issues = '#16129'
[../]


[./hys_sat_02]
  type = CSVDiff
  input = 'hys_sat_02.i'
  csvdiff = 'hys_sat_02_out_sat_0001.csv'
  requirement = 'PorousFlow shall be able to compute saturation according to the primary drying curve in hysteretic problems, using quadratic low extension'
  design = 'PorousFlow1PhaseHysP.md'
  issues = '#16129'
[../]


[./hys_sat_03]
  type = CSVDiff
  input = 'hys_sat_03.i'
  csvdiff = 'hys_sat_03_out_sat_0001.csv'
  requirement = 'PorousFlow shall be able to compute saturation according to the primary drying curve in hysteretic problems, using exponential low extension'
  design = 'PorousFlow1PhaseHysP.md'
  issues = '#16129'
[../]


[./hys_pc_01]
  type = CSVDiff
  input = 'hys_pc_01.i'
  csvdiff = 'hys_pc_01_out_pc_0001.csv'
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the primary drying curve in hysteretic problems, using no low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_02]
  type = CSVDiff
  input = 'hys_pc_02.i'
  csvdiff = 'hys_pc_02_out_pc_0001.csv'
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the primary drying curve in hysteretic problems, using quadratic low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_03]
  type = CSVDiff
  input = 'hys_pc_03.i'
  csvdiff = 'hys_pc_03_out_pc_0001.csv'
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the primary drying curve in hysteretic problems, using exponential low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_1_w_none_none]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_pc_p_w_none_none_pc_0001.csv'
  cli_args = 'Materials/hys_order/previous_turning_points=0.1 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_pc_p_w_none_none'
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the primary wetting curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_1_w_none_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_pc_p_w_none_power_pc_0001.csv'
  cli_args = 'Materials/hys_order/previous_turning_points=0.1 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_pc_p_w_none_power'
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the primary wetting curve in hysteretic problems, using no low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_1_w_quadratic_none]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_pc_p_w_quadratic_none_pc_0001.csv'
  cli_args = 'Materials/hys_order/previous_turning_points=0.1 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_pc_p_w_quadratic_none'
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the primary wetting curve in hysteretic problems, using quadratic low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_1_w_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_pc_p_w_quadratic_power_pc_0001.csv'
  cli_args = 'Materials/hys_order/previous_turning_points=0.1 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_pc_p_w_quadratic_power'
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the primary wetting curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_1_w_exponential_none]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_pc_p_w_exponential_none_pc_0001.csv'
  cli_args = 'Materials/hys_order/previous_turning_points=0.1 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_pc_p_w_exponential_none'
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the primary wetting curve in hysteretic problems, using exponential low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_1_w_exponential_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_pc_p_w_exponential_power_pc_0001.csv'
  cli_args = 'Materials/hys_order/previous_turning_points=0.1 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_pc_p_w_exponential_power'
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the primary wetting curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_1_none_none]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_pc_p_1_none_none_pc_0001.csv'
  cli_args = "Mesh/mesh/xmin=0.5 VectorPostprocessors/pc/start_point='0.5 0 0' Materials/hys_order/previous_turning_points=0.5 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_pc_p_1_none_none"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the first-order wetting curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_1_none_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_pc_p_1_none_power_pc_0001.csv'
  cli_args = "Mesh/mesh/xmin=0.5 VectorPostprocessors/pc/start_point='0.5 0 0' Materials/hys_order/previous_turning_points=0.5 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_pc_p_1_none_power"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the first-order wetting curve in hysteretic problems, using no low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_1_quadratic_none]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_pc_p_1_quadratic_none_pc_0001.csv'
  cli_args = "Mesh/mesh/xmin=0.5 VectorPostprocessors/pc/start_point='0.5 0 0' Materials/hys_order/previous_turning_points=0.5 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_pc_p_1_quadratic_none"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the first-order wetting curve in hysteretic problems, using quadratic low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_1_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_pc_p_1_quadratic_power_pc_0001.csv'
  cli_args = "Mesh/mesh/xmin=0.5 VectorPostprocessors/pc/start_point='0.5 0 0' Materials/hys_order/previous_turning_points=0.5 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_pc_p_1_quadratic_power"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the first-order wetting curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_1_exponential_none]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_pc_p_1_exponential_none_pc_0001.csv'
  cli_args = "Mesh/mesh/xmin=0.5 VectorPostprocessors/pc/start_point='0.5 0 0' Materials/hys_order/previous_turning_points=0.5 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_pc_p_1_exponential_none"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the first-order wetting curve in hysteretic problems, using exponential low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_1_exponential_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_pc_p_1_exponential_power_pc_0001.csv'
  cli_args = "Mesh/mesh/xmin=0.5 VectorPostprocessors/pc/start_point='0.5 0 0' Materials/hys_order/previous_turning_points=0.5 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_pc_p_1_exponential_power"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the first-order wetting curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_2_none_none]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_pc_p_2_none_none_pc_0001.csv'
  cli_args = "Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_pc_p_2_none_none"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the second-order drying  curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_2_none_power]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_pc_p_2_none_power_pc_0001.csv'
  cli_args = "Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_pc_p_2_none_power"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the second-order drying  curve in hysteretic problems, using no low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_2_quadratic_none]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_pc_p_2_quadratic_none_pc_0001.csv'
  cli_args = "Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_pc_p_2_quadratic_none"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the second-order drying  curve in hysteretic problems, using quadratic low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_2_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_pc_p_2_quadratic_power_pc_0001.csv'
  cli_args = "Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_pc_p_2_quadratic_power"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the second-order drying  curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_2_exponential_none]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_pc_p_2_exponential_none_pc_0001.csv'
  cli_args = "Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_pc_p_2_exponential_none"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the second-order drying  curve in hysteretic problems, using exponential low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_2_exponential_power]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_pc_p_2_exponential_power_pc_0001.csv'
  cli_args = "Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_pc_p_2_exponential_power"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the second-order drying  curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_3_none_none]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_pc_p_3_none_none_pc_0001.csv'
  cli_args = "Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_pc_p_3_none_none"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the third-order wetting curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_3_none_power]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_pc_p_3_none_power_pc_0001.csv'
  cli_args = "Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_pc_p_3_none_power"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the third-order wetting curve in hysteretic problems, using no low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_3_quadratic_none]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_pc_p_3_quadratic_none_pc_0001.csv'
  cli_args = "Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_pc_p_3_quadratic_none"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the third-order wetting curve in hysteretic problems, using quadratic low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_3_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_pc_p_3_quadratic_power_pc_0001.csv'
  cli_args = "Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_pc_p_3_quadratic_power"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the third-order wetting curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_3_exponential_none]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_pc_p_3_exponential_none_pc_0001.csv'
  cli_args = "Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_pc_p_3_exponential_none"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the third-order wetting curve in hysteretic problems, using exponential low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_pc_3_exponential_power]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_pc_p_3_exponential_power_pc_0001.csv'
  cli_args = "Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_pc_p_3_exponential_power"
  requirement = 'PorousFlow shall be able to compute capillary pressure according to the third-order wetting curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_prim_01]
  type = CSVDiff
  input = 'hys_pc_01.i'
  csvdiff = 'hys_sat_01_none_pc_0001.csv'
  cli_args = "Materials/pc_calculator/info_required=sat Outputs/file_base=hys_sat_01_none"
  requirement = 'PorousFlow shall be able to compute saturation from capillary pressure according to the primary drying curve in hysteretic problems, using no low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_prim_02]
  type = CSVDiff
  input = 'hys_pc_02.i'
  csvdiff = 'hys_sat_02_quad_pc_0001.csv'
  cli_args = "Materials/pc_calculator/info_required=sat Outputs/file_base=hys_sat_02_quad"
  requirement = 'PorousFlow shall be able to compute saturation from capillary pressure according to the primary drying curve in hysteretic problems, using quadratic low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_prim_03]
  type = CSVDiff
  input = 'hys_pc_03.i'
  csvdiff = 'hys_sat_03_exp_pc_0001.csv'
  cli_args = "Materials/pc_calculator/info_required=sat Outputs/file_base=hys_sat_03_exp"
  requirement = 'PorousFlow shall be able to compute saturation from capillary pressure according to the primary drying curve in hysteretic problems, using exponential low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_1_w_none_none]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_sat_p_w_none_none_pc_0001.csv'
  cli_args = 'Materials/hys_order/previous_turning_points=0.1 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_sat_p_w_none_none Materials/pc_calculator/info_required=sat'
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the primary wetting curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_1_w_none_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_sat_p_w_none_power_pc_0001.csv'
  cli_args = 'Materials/hys_order/previous_turning_points=0.1 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_sat_p_w_none_power Materials/pc_calculator/info_required=sat'
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the primary wetting curve in hysteretic problems, using no low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_1_w_quadratic_none]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_sat_p_w_quadratic_none_pc_0001.csv'
  cli_args = 'Materials/hys_order/previous_turning_points=0.1 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_sat_p_w_quadratic_none Materials/pc_calculator/info_required=sat'
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the primary wetting curve in hysteretic problems, using quadratic low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_1_w_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_sat_p_w_quadratic_power_pc_0001.csv'
  cli_args = 'Materials/hys_order/previous_turning_points=0.1 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_sat_p_w_quadratic_power Materials/pc_calculator/info_required=sat Materials/pc_calculator/Pc_max=0.5'
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the primary wetting curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_1_w_exponential_none]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_sat_p_w_exponential_none_pc_0001.csv'
  cli_args = 'Materials/hys_order/previous_turning_points=0.1 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_sat_p_w_exponential_none Materials/pc_calculator/info_required=sat'
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the primary wetting curve in hysteretic problems, using exponential low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_1_w_exponential_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_sat_p_w_exponential_power_pc_0001.csv'
  cli_args = 'Materials/hys_order/previous_turning_points=0.1 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_sat_p_w_exponential_power Materials/pc_calculator/info_required=sat Materials/pc_calculator/Pc_max=0.5'
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the primary wetting curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_2_none_none]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_sat_p_2_none_none_pc_0001.csv'
  cli_args = "Materials/pc_calculator/info_required=sat Materials/pc_calculator/Pc_max=0.5 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_sat_p_2_none_none"
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the second-order drying  curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_2_none_power]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_sat_p_2_none_power_pc_0001.csv'
  cli_args = "Materials/pc_calculator/info_required=sat Materials/pc_calculator/Pc_max=0.5 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_sat_p_2_none_power"
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the second-order drying  curve in hysteretic problems, using no low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_2_quadratic_none]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_sat_p_2_quadratic_none_pc_0001.csv'
  cli_args = "Materials/pc_calculator/info_required=sat Materials/pc_calculator/Pc_max=0.5 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_sat_p_2_quadratic_none"
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the second-order drying  curve in hysteretic problems, using quadratic low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_2_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_sat_p_2_quadratic_power_pc_0001.csv'
  cli_args = "Materials/pc_calculator/info_required=sat Materials/pc_calculator/Pc_max=0.5 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_sat_p_2_quadratic_power"
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the second-order drying  curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_2_exponential_none]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_sat_p_2_exponential_none_pc_0001.csv'
  cli_args = "Materials/pc_calculator/info_required=sat Materials/pc_calculator/Pc_max=0.5 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_sat_p_2_exponential_none"
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the second-order drying  curve in hysteretic problems, using exponential low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_2_exponential_power]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_sat_p_2_exponential_power_pc_0001.csv'
  cli_args = "Materials/pc_calculator/info_required=sat Materials/pc_calculator/Pc_max=0.5 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_sat_p_2_exponential_power"
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the second-order drying  curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_3_none_power]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_sat_p_3_none_power_pc_0001.csv'
  cli_args = "Materials/pc_calculator/info_required=sat Materials/pc_calculator/Pc_max=0.3 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_sat_p_3_none_power"
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the third-order wetting curve in hysteretic problems, using no low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_3_quadratic_none]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_sat_p_3_quadratic_none_pc_0001.csv'
  cli_args = "Materials/pc_calculator/info_required=sat Materials/pc_calculator/Pc_max=0.3 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_sat_p_3_quadratic_none"
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the third-order wetting curve in hysteretic problems, using quadratic low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_3_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_sat_p_3_quadratic_power_pc_0001.csv'
  cli_args = "Materials/pc_calculator/info_required=sat Materials/pc_calculator/Pc_max=0.3 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_sat_p_3_quadratic_power"
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the third-order wetting curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_3_exponential_none]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_sat_p_3_exponential_none_pc_0001.csv'
  cli_args = "Materials/pc_calculator/info_required=sat Materials/pc_calculator/Pc_max=0.3 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_sat_p_3_exponential_none"
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the third-order wetting curve in hysteretic problems, using exponential low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_sat_3_exponential_power]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_sat_p_3_exponential_power_pc_0001.csv'
  cli_args = "Materials/pc_calculator/info_required=sat Materials/pc_calculator/Pc_max=0.3 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_sat_p_3_exponential_power"
  requirement = 'PorousFlow shall be able to compute liquid saturation according to the third-order wetting curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dpc_prim_01]
  type = CSVDiff
  input = 'hys_pc_01.i'
  csvdiff = 'hys_dpc_01_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dPc_dS_err Outputs/file_base=hys_dpc_01_none"
  requirement = 'PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along to the primary drying curve in hysteretic problems, using no low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dpc_prim_02]
  type = CSVDiff
  input = 'hys_pc_02.i'
  csvdiff = 'hys_dpc_02_quad_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dPc_dS_err Outputs/file_base=hys_dpc_02_quad"
  requirement = 'PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along to the primary drying curve in hysteretic problems, using quadratic low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dpc_prim_03]
  type = CSVDiff
  input = 'hys_pc_03.i'
  csvdiff = 'hys_dpc_03_exp_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dPc_dS_err Outputs/file_base=hys_dpc_03_exp"
  requirement = 'PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along to the primary drying curve in hysteretic problems, using exponential low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dpc_1_none_none]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_dpc_p_1_none_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dPc_dS_err Mesh/mesh/xmin=0.5 VectorPostprocessors/pc/start_point='0.5 0 0' Materials/hys_order/previous_turning_points=0.5 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_dpc_p_1_none_none"
  requirement = 'PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along the first-order wetting curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dpc_1_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_dpc_p_1_quadratic_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dPc_dS_err Mesh/mesh/xmin=0.5 VectorPostprocessors/pc/start_point='0.5 0 0' Materials/hys_order/previous_turning_points=0.5 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_dpc_p_1_quadratic_power"
  requirement = 'PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along the first-order wetting curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dpc_1_exponential_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_dpc_p_1_exponential_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dPc_dS_err Mesh/mesh/xmin=0.5 VectorPostprocessors/pc/start_point='0.5 0 0' Materials/hys_order/previous_turning_points=0.5 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_dpc_p_1_exponential_power"
  requirement = 'PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along the first-order wetting curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dpc_2_none_none]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_dpc_p_2_none_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dPc_dS_err Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_dpc_p_2_none_none"
  requirement = 'PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along the second-order drying  curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dpc_2_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_dpc_p_2_quadratic_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dPc_dS_err Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_dpc_p_2_quadratic_power"
  requirement = 'PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along the second-order drying  curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dpc_2_exponential_power]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_dpc_p_2_exponential_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dPc_dS_err Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_dpc_p_2_exponential_power"
  requirement = 'PorousFlow shall be able to compute the derivative of capillary pressure with respect to liquid saturation along the second-order drying  curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dpc_3_none_none]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_dpc_p_3_none_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dPc_dS_err Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_dpc_p_3_none_none"
  requirement = 'PorousFlow shall be able to compute the derivative of the capillary pressure with respect to the liquid saturation along the third-order wetting curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dpc_3_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_dpc_p_3_quadratic_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dPc_dS_err Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_dpc_p_3_quadratic_power"
  requirement = 'PorousFlow shall be able to compute the derivative of the capillary pressure with respect to the liquid saturation along the third-order wetting curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dpc_3_exponential_power]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_dpc_p_3_exponential_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dPc_dS_err Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_dpc_p_3_exponential_power"
  requirement = 'PorousFlow shall be able to compute the derivative of the capillary pressure with respect to the liquid saturation along the third-order wetting curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2pc_prim_01]
  type = CSVDiff
  input = 'hys_pc_01.i'
  csvdiff = 'hys_d2pc_01_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2Pc_dS2_err Outputs/file_base=hys_d2pc_01_none"
  requirement = 'PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along to the primary drying curve in hysteretic problems, using no low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2pc_prim_02]
  type = CSVDiff
  input = 'hys_pc_02.i'
  csvdiff = 'hys_d2pc_02_quad_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2Pc_dS2_err Outputs/file_base=hys_d2pc_02_quad"
  requirement = 'PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along to the primary drying curve in hysteretic problems, using quadratic low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2pc_prim_03]
  type = CSVDiff
  input = 'hys_pc_03.i'
  csvdiff = 'hys_d2pc_03_exp_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2Pc_dS2_err Outputs/file_base=hys_d2pc_03_exp"
  requirement = 'PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along to the primary drying curve in hysteretic problems, using exponential low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2pc_1_none_none]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_d2pc_p_1_none_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2Pc_dS2_err Mesh/mesh/xmin=0.5 VectorPostprocessors/pc/start_point='0.5 0 0' Materials/hys_order/previous_turning_points=0.5 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_d2pc_p_1_none_none"
  requirement = 'PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along the first-order wetting curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2pc_1_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_d2pc_p_1_quadratic_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2Pc_dS2_err Mesh/mesh/xmin=0.5 VectorPostprocessors/pc/start_point='0.5 0 0' Materials/hys_order/previous_turning_points=0.5 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_d2pc_p_1_quadratic_power"
  requirement = 'PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along the first-order wetting curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2pc_1_exponential_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_d2pc_p_1_exponential_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2Pc_dS2_err Mesh/mesh/xmin=0.5 VectorPostprocessors/pc/start_point='0.5 0 0' Materials/hys_order/previous_turning_points=0.5 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_d2pc_p_1_exponential_power"
  requirement = 'PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along the first-order wetting curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2pc_2_none_none]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_d2pc_p_2_none_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2Pc_dS2_err Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_d2pc_p_2_none_none"
  requirement = 'PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along the second-order drying  curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2pc_2_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_d2pc_p_2_quadratic_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2Pc_dS2_err Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_d2pc_p_2_quadratic_power"
  requirement = 'PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along the second-order drying  curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2pc_2_exponential_power]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_d2pc_p_2_exponential_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2Pc_dS2_err Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_d2pc_p_2_exponential_power"
  requirement = 'PorousFlow shall be able to compute the second derivative of capillary pressure with respect to liquid saturation along the second-order drying  curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2pc_3_none_none]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_d2pc_p_3_none_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2Pc_dS2_err Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_d2pc_p_3_none_none"
  requirement = 'PorousFlow shall be able to compute the second derivative of the capillary pressure with respect to the liquid saturation along the third-order wetting curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2pc_3_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_d2pc_p_3_quadratic_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2Pc_dS2_err Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_d2pc_p_3_quadratic_power"
  requirement = 'PorousFlow shall be able to compute the second derivative of the capillary pressure with respect to the liquid saturation along the third-order wetting curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2pc_3_exponential_power]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_d2pc_p_3_exponential_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2Pc_dS2_err Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_d2pc_p_3_exponential_power"
  requirement = 'PorousFlow shall be able to compute the second derivative of the capillary pressure with respect to the liquid saturation along the third-order wetting curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dsat_prim_01]
  type = CSVDiff
  input = 'hys_pc_01.i'
  csvdiff = 'hys_dsat_01_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dS_dPc_err Outputs/file_base=hys_dsat_01_none"
  requirement = 'PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along to the primary drying curve in hysteretic problems, using no low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dsat_prim_02]
  type = CSVDiff
  input = 'hys_pc_02.i'
  csvdiff = 'hys_dsat_02_quad_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dS_dPc_err Outputs/file_base=hys_dsat_02_quad"
  requirement = 'PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along to the primary drying curve in hysteretic problems, using quadratic low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dsat_prim_03]
  type = CSVDiff
  input = 'hys_pc_03.i'
  csvdiff = 'hys_dsat_03_exp_pc_0001.csv'
  abs_zero = 1E-5
  cli_args = "Materials/pc_calculator/info_required=dS_dPc_err Outputs/file_base=hys_dsat_03_exp VectorPostprocessors/pc/start_point='0.05 0 0'"
  requirement = 'PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along to the primary drying curve in hysteretic problems, using exponential low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dsat_1_none_none]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_dsat_p_1_none_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dS_dPc_err Materials/pc_calculator/Pc_max=0.5 VectorPostprocessors/pc/start_point='0.09 0 0' Materials/hys_order/previous_turning_points=0.05 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_dsat_p_1_none_none"
  requirement = 'PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along the first-order wetting curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dsat_1_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_dsat_p_1_quadratic_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dS_dPc_err Materials/pc_calculator/Pc_max=0.5 VectorPostprocessors/pc/start_point='0.09 0 0' VectorPostprocessors/pc/end_point='0.95 0 0' Materials/hys_order/previous_turning_points=0.05 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_dsat_p_1_quadratic_power"
  requirement = 'PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along the first-order wetting curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dsat_1_exponential_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_dsat_p_1_exponential_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dS_dPc_err Materials/pc_calculator/Pc_max=0.5 VectorPostprocessors/pc/start_point='0.09 0 0' VectorPostprocessors/pc/end_point='0.95 0 0' Materials/hys_order/previous_turning_points=0.05 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_dsat_p_1_exponential_power"
  requirement = 'PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along the first-order wetting curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dsat_2_none_none]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_dsat_p_2_none_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dS_dPc_err Materials/pc_calculator/Pc_max=0.5 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_dsat_p_2_none_none"
  requirement = 'PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along the second-order drying  curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dsat_2_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_dsat_p_2_quadratic_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dS_dPc_err Materials/pc_calculator/Pc_max=0.5 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_dsat_p_2_quadratic_power"
  requirement = 'PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along the second-order drying  curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dsat_2_exponential_power]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_dsat_p_2_exponential_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dS_dPc_err Materials/pc_calculator/Pc_max=0.5 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_dsat_p_2_exponential_power"
  requirement = 'PorousFlow shall be able to compute the derivative of liquid saturation with respect to capillary pressure along the second-order drying  curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dsat_3_none_none]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_dsat_p_3_none_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dS_dPc_err Materials/pc_calculator/Pc_max=0.3 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_dsat_p_3_none_none"
  requirement = 'PorousFlow shall be able to compute the derivative of the liquid saturation with respect to capillary pressure along the third-order wetting curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dsat_3_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_dsat_p_3_quadratic_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dS_dPc_err Materials/pc_calculator/Pc_max=0.3 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_dsat_p_3_quadratic_power"
  requirement = 'PorousFlow shall be able to compute the derivative of the liquid saturation with respect to capillary pressure along the third-order wetting curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_dsat_3_exponential_power]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_dsat_p_3_exponential_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=dS_dPc_err Materials/pc_calculator/Pc_max=0.3 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_dsat_p_3_exponential_power"
  requirement = 'PorousFlow shall be able to compute the derivative of the liquid saturation with respect to capillary pressure along the third-order wetting curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2sat_prim_01]
  type = CSVDiff
  input = 'hys_pc_01.i'
  csvdiff = 'hys_d2sat_01_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2S_dPc2_err Outputs/file_base=hys_d2sat_01_none"
  requirement = 'PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along to the primary drying curve in hysteretic problems, using no low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2sat_prim_02]
  type = CSVDiff
  input = 'hys_pc_02.i'
  csvdiff = 'hys_d2sat_02_quad_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2S_dPc2_err Outputs/file_base=hys_d2sat_02_quad"
  requirement = 'PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along to the primary drying curve in hysteretic problems, using quadratic low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2sat_prim_03]
  type = CSVDiff
  input = 'hys_pc_03.i'
  csvdiff = 'hys_d2sat_03_exp_pc_0001.csv'
  abs_zero = 1E-5
  cli_args = "Materials/pc_calculator/info_required=d2S_dPc2_err Outputs/file_base=hys_d2sat_03_exp VectorPostprocessors/pc/start_point='0.05 0 0'"
  requirement = 'PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along to the primary drying curve in hysteretic problems, using exponential low extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2sat_1_none_none]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_d2sat_p_1_none_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2S_dPc2_err Materials/pc_calculator/Pc_max=0.5 VectorPostprocessors/pc/start_point='0.09 0 0' Materials/hys_order/previous_turning_points=0.05 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_d2sat_p_1_none_none"
  requirement = 'PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along the first-order wetting curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2sat_1_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_d2sat_p_1_quadratic_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2S_dPc2_err Materials/pc_calculator/Pc_max=0.5 VectorPostprocessors/pc/start_point='0.09 0 0' VectorPostprocessors/pc/end_point='0.95 0 0' Materials/hys_order/previous_turning_points=0.05 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_d2sat_p_1_quadratic_power"
  requirement = 'PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along the first-order wetting curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2sat_1_exponential_power]
  type = CSVDiff
  input = 'hys_pc_1.i'
  csvdiff = 'hys_d2sat_p_1_exponential_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2S_dPc2_err Materials/pc_calculator/Pc_max=0.5 VectorPostprocessors/pc/start_point='0.09 0 0' VectorPostprocessors/pc/end_point='0.95 0 0' Materials/hys_order/previous_turning_points=0.05 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_d2sat_p_1_exponential_power"
  requirement = 'PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along the first-order wetting curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2sat_2_none_none]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_d2sat_p_2_none_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2S_dPc2_err Materials/pc_calculator/Pc_max=0.5 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_d2sat_p_2_none_none"
  requirement = 'PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along the second-order drying  curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2sat_2_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_d2sat_p_2_quadratic_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2S_dPc2_err Materials/pc_calculator/Pc_max=0.5 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_d2sat_p_2_quadratic_power"
  requirement = 'PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along the second-order drying  curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2sat_2_exponential_power]
  type = CSVDiff
  input = 'hys_pc_2.i'
  csvdiff = 'hys_d2sat_p_2_exponential_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2S_dPc2_err Materials/pc_calculator/Pc_max=0.5 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_d2sat_p_2_exponential_power"
  requirement = 'PorousFlow shall be able to compute the second derivative of liquid saturation with respect to capillary pressure along the second-order drying  curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2sat_3_none_none]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_d2sat_p_3_none_none_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2S_dPc2_err Materials/pc_calculator/Pc_max=0.3 Materials/pc_calculator/low_extension_type=none Materials/pc_calculator/high_extension_type=none Outputs/file_base=hys_d2sat_p_3_none_none"
  requirement = 'PorousFlow shall be able to compute the second derivative of the liquid saturation with respect to capillary pressure along the third-order wetting curve in hysteretic problems, using no low extension and no high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2sat_3_quadratic_power]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_d2sat_p_3_quadratic_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2S_dPc2_err Materials/pc_calculator/Pc_max=0.3 Materials/pc_calculator/low_extension_type=quadratic Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_d2sat_p_3_quadratic_power"
  requirement = 'PorousFlow shall be able to compute the second derivative of the liquid saturation with respect to capillary pressure along the third-order wetting curve in hysteretic problems, using quadratic low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./hys_d2sat_3_exponential_power]
  type = CSVDiff
  input = 'hys_pc_3.i'
  csvdiff = 'hys_d2sat_p_3_exponential_power_pc_0001.csv'
  abs_zero = 1E-6
  cli_args = "Materials/pc_calculator/info_required=d2S_dPc2_err Materials/pc_calculator/Pc_max=0.3 Materials/pc_calculator/low_extension_type=exponential Materials/pc_calculator/high_extension_type=power Outputs/file_base=hys_d2sat_p_3_exponential_power"
  requirement = 'PorousFlow shall be able to compute the second derivative of the liquid saturation with respect to capillary pressure along the third-order wetting curve in hysteretic problems, using exponential low extension and power high extension'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./vary_sat_1a]
  type = CSVDiff
  input = 'vary_sat_1.i'
  csvdiff = 'vary_sat_1_out.csv'
  requirement = 'PorousFlow shall be able to compute capillary pressure as a function of saturation in hysteretic time-dependent problems, along the primary drying curve'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./vary_sat_1b]
  type = CSVDiff
  input = 'vary_sat_1.i'
  csvdiff = 'vary_sat_1b.csv'
  cli_args = "AuxKernels/sat_aux/function='if(t <= 0.5, 1 - 2 * t, 2 * t - 1)' Executioner/dt=0.0625 Outputs/file_base=vary_sat_1b"
  requirement = 'PorousFlow shall be able to compute capillary pressure as a function of saturation in hysteretic time-dependent problems, along the primary drying curve and then the primary wetting curve'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./vary_sat_1c]
  type = CSVDiff
  input = 'vary_sat_1.i'
  csvdiff = 'vary_sat_1c.csv'
  cli_args = "AuxKernels/sat_aux/function='if(t <= 0.4, 1 - 2 * t, 2 * t - 0.6)' Executioner/dt=0.05 Executioner/end_time=0.8 Outputs/file_base=vary_sat_1c"
  requirement = 'PorousFlow shall be able to compute capillary pressure as a function of saturation in hysteretic time-dependent problems, along the primary drying curve and then the first-order wetting'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./vary_sat_1d]
  type = CSVDiff
  input = 'vary_sat_1.i'
  csvdiff = 'vary_sat_1d.csv'
  cli_args = "AuxKernels/sat_aux/function='if(t <= 0.4, 1 - 2 * t, if(t <= 0.7, 2 * t - 0.6, 0.8 - 2 * (t - 0.7)))' Executioner/dt=0.05 Executioner/end_time=1.4 Outputs/file_base=vary_sat_1d"
  requirement = 'PorousFlow shall be able to compute capillary pressure as a function of saturation in hysteretic time-dependent problems, along the primary drying curve, then first-order wetting, and then second-order drying'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./vary_sat_1e]
  type = CSVDiff
  input = 'vary_sat_1.i'
  csvdiff = 'vary_sat_1e.csv'
  cli_args = "AuxKernels/sat_aux/function='if(t <= 0.4, 1 - 2 * t, if(t <= 0.7, 2 * t - 0.6, if(t <= 0.95, 0.8 - 2 * (t - 0.7), 0.3 + 2 * (t - 0.95))))' Executioner/dt=0.025 Executioner/end_time=1.3 Outputs/file_base=vary_sat_1e"
  requirement = 'PorousFlow shall be able to compute capillary pressure as a function of saturation in hysteretic time-dependent problems, along the primary drying curve, then first-order wetting, and then second-order drying, and then third-order'
  design = 'PorousFlowHystereticInfo.md'
  issues = '#16129'
[../]


[./1phase]
  type = CSVDiff
  input = '1phase.i'
  csvdiff = '1phase_out.csv'
  requirement = 'PorousFlow shall be able to compute saturation in 1-phase hysteretic systems, as the system evolves in time along the primary drying curve and then along a first-order wetting curve'
  design = 'PorousFlow1PhaseHysP.md'
  issues = '#16129'
[../]


[./1phase_3rd]
  type = CSVDiff
  input = '1phase_3rd.i'
  csvdiff = '1phase_3rd_out.csv'
  requirement = 'PorousFlow shall be able to compute saturation in 1-phase hysteretic systems, as the system evolves in time along the primary drying curve and then along first, second and third order curves'
  design = 'PorousFlow1PhaseHysP.md'
  issues = '#16129'
[../]


[./2phasePP_jacobian]
  type = PetscJacobianTester
  input = '2phasePP_jac.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  requirement = 'PorousFlow shall be able to compute the full Jacobian entries in 2-phase hysteretic systems when using a PP formulation'
  design = 'PorousFlow2PhaseHysPP.md'
  issues = '#16129'
[../]


[./2phasePP_1]
  type = CSVDiff
  input = '2phasePP.i'
  csvdiff = '2phasePP_out.csv'
  requirement = 'PorousFlow shall be able to compute saturations and porepressures in 2-phase hysteretic systems when using a PP formulation, as the system evolves in time along the primary drying curve and then along a first-order curve'
  design = 'PorousFlow2PhaseHysPP.md'
  issues = '#16129'
[../]


[./2phasePP_2]
  type = CSVDiff
  input = '2phasePP_2.i'
  csvdiff = '2phasePP_2_out.csv'
  requirement = 'PorousFlow shall be able to compute saturations and porepressures in 2-phase hysteretic systems when using a PP formulation, as the system evolves in time along the primary drying curve and then along a first-order curve and then along a second-order drying curve until it meets the primary drying curve'
  design = 'PorousFlow2PhaseHysPP.md'
  issues = '#16129'
[../]


[./2phasePS_jacobian]
  type = PetscJacobianTester
  input = '2phasePS_jac.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  requirement = 'PorousFlow shall be able to compute the full Jacobian entries in 2-phase hysteretic systems when using a PS formulation'
  design = 'PorousFlow2PhaseHysPS.md'
  issues = '#16129'
[../]


[./2phasePS_1]
  type = CSVDiff
  input = '2phasePS.i'
  csvdiff = '2phasePS_out.csv'
  requirement = 'PorousFlow shall be able to compute saturations and porepressures in 2-phase hysteretic systems when using a PS formulation, as the system evolves in time along the primary drying curve and then along a first-order curve'
  design = 'PorousFlow2PhaseHysPS.md'
  issues = '#16129'
[../]


[./2phasePS_2]
  type = CSVDiff
  input = '2phasePS_2.i'
  csvdiff = '2phasePS_2_out.csv'
  requirement = 'PorousFlow shall be able to compute saturations and porepressures in 2-phase hysteretic systems when using a PS formulation, as the system evolves in time along the primary drying curve and then along a first-order curve and then along a second-order drying curve until it meets the primary drying curve'
  design = 'PorousFlow2PhaseHysPS.md'
  issues = '#16129'
[../]


[./1phase_relperm]
  type = CSVDiff
  input = '1phase_relperm.i'
  csvdiff = '1phase_relperm_out.csv'
  requirement = 'PorousFlow shall be able to compute hysteretic relative permeability in 1-phase systems as the system evolves in time along the primary drying curve and then along a first-order wetting curve'
  design = 'PorousFlowHystereticRelativePermeabilityLiquid.md'
  issues = '#16324'
[../]


[./1phase_relperm_2]
  type = CSVDiff
  input = '1phase_relperm_2.i'
  csvdiff = '1phase_relperm_2_csv.csv'
  requirement = 'PorousFlow shall be able to compute hysteretic relative permeability in 1-phase systems as the saturation cycles between high and low values, including going below the residual saturation'
  design = 'PorousFlowHystereticRelativePermeabilityLiquid.md'
  issues = '#16324'
[../]


[./2phasePS_relperm]
  type = CSVDiff
  input = '2phasePS_relperm.i'
  csvdiff = '2phasePS_relperm_out.csv'
  requirement = 'PorousFlow shall be able to compute hysteretic liquid and gas relative permeabilities in 2-phase systems as the system evolves in time along the primary drying curve and then along first-order wetting curves'
  design = 'PorousFlowHystereticRelativePermeabilityLiquid.md PorousFlowHystereticRelativePermeabilityGas.md'
  issues = '#16324'
[../]


[./2phasePS_relperm_2_linear_like]
  type = CSVDiff
  input = '2phasePS_relperm_2.i'
  csvdiff = '2phasePS_relperm_2_linear_like.csv'
  cli_args = 'Materials/relperm_gas/k_rg_max=0.4 Materials/relperm_gas/gas_low_extension_type=linear_like Outputs/csv/file_base=2phasePS_relperm_2_linear_like'
  requirement = 'PorousFlow shall be able to compute hysteretic liquid and gas relative permeabilities in 2-phase systems as the system dries and then re-wets, and the gas relative permeability is extended to low saturations using a linear-like extension'
  design = 'PorousFlowHystereticRelativePermeabilityLiquid.md PorousFlowHystereticRelativePermeabilityGas.md'
  issues = '#16324'
[../]


[./2phasePS_relperm_2_cubic]
  type = CSVDiff
  input = '2phasePS_relperm_2.i'
  csvdiff = '2phasePS_relperm_2_cubic.csv'
  cli_args = 'Materials/relperm_gas/k_rg_max=0.4 Materials/relperm_gas/gas_low_extension_type=cubic Outputs/csv/file_base=2phasePS_relperm_2_cubic'
  requirement = 'PorousFlow shall be able to compute hysteretic liquid and gas relative permeabilities in 2-phase systems as the system dries and then re-wets, and the gas relative permeability is extended to low saturations using a cubic extension'
  design = 'PorousFlowHystereticRelativePermeabilityLiquid.md PorousFlowHystereticRelativePermeabilityGas.md'
  issues = '#16324'
[../]


[./2phasePS_relperm_2_none]
  type = CSVDiff
  input = '2phasePS_relperm_2.i'
  csvdiff = '2phasePS_relperm_2_none.csv'
  cli_args = 'Materials/relperm_gas/k_rg_max=1.0 Outputs/csv/file_base=2phasePS_relperm_2_none'
  requirement = 'PorousFlow shall be able to compute hysteretic liquid and gas relative permeabilities in 2-phase systems as the system dries and then re-wets, and the gas relative permeability is extended to low saturations by assuming is is unity'
  design = 'PorousFlowHystereticRelativePermeabilityLiquid.md PorousFlowHystereticRelativePermeabilityGas.md'
  issues = '#16324'
[../]


[./relperm_jac]
  type = PetscJacobianTester
  input = 'relperm_jac.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  requirement = 'PorousFlow shall be able to compute the full Jacobian entries when using hysteretic relative permeabilities, as the system evolves along a zeroth order curve'
  design = 'PorousFlowHystereticRelativePermeabilityLiquid.md PorousFlowHystereticRelativePermeabilityGas.md'
  issues = '#16324'
[../]


[./relperm_jac_1]
  type = PetscJacobianTester
  input = 'relperm_jac_1.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  requirement = 'PorousFlow shall be able to compute the full Jacobian entries when using hysteretic relative permeabilities, as the system evolves along a first-order curve'
  design = 'PorousFlowHystereticRelativePermeabilityLiquid.md PorousFlowHystereticRelativePermeabilityGas.md'
  issues = '#16324'
[../]

[./fluidpropic]
  type = 'CSVDiff'
  input = 'fluidpropic.i'
  csvdiff = 'fluidpropic_out.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall calculate an initial condition for a fluid property given pressure and temperature'
  design = 'PorousFlowFluidPropertyIC.md'
  issues = '#13108'
[../]


[./fluidpropic_celsius]
  type = 'CSVDiff'
  input = 'fluidpropic_celsius.i'
  csvdiff = 'fluidpropic_out.csv'
  threading = '!pthreads'
  prereq = 'fluidpropic'
  requirement = 'PorousFlow shall calculate an initial condition for a fluid property given pressure and temperature (in C)'
  design = 'PorousFlowFluidPropertyIC.md'
  issues = '#13108'
[../]

[./bw01]
  type = 'Exodiff'
  input = 'bw01.i'
  exodiff = 'bw01.e'
  rel_err = 1E-5
  use_old_floor = True
  heavy = true
  max_time = 1000
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model 2-phase infiltration and agree with the analytic solution'
  issues = '#13155'
  design = 'porous_flow/tests/infiltration_and_drainage/infiltration_and_drainage_tests.md'
[../]


[./bw02]
  type = 'Exodiff'
  input = 'bw02.i'
  exodiff = 'bw02.e'
  rel_err = 1E-5
  use_old_floor = True
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model 2-phase infiltration on a coarse mesh and agree with the analytic solution'
  issues = '#13155'
  design = 'porous_flow/tests/infiltration_and_drainage/infiltration_and_drainage_tests.md'
[../]


[./wli01]
  type = 'Exodiff'
  input = 'wli01.i'
  exodiff = 'wli01.e'
  rel_err = 1E-5
  use_old_floor = True
  heavy = true
  max_time = 2000
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model 2-phase drainage and agree with the analytic solution'
  issues = '#13155'
  design = 'porous_flow/tests/infiltration_and_drainage/infiltration_and_drainage_tests.md'
[../]


[./wli02]
  type = 'Exodiff'
  input = 'wli02.i'
  exodiff = 'wli02.e'
  rel_err = 1E-5
  use_old_floor = True
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model 2-phase drainage on a coarse mesh and agree with the analytic solution'
  issues = '#13155'
  design = 'porous_flow/tests/infiltration_and_drainage/infiltration_and_drainage_tests.md'
[../]


[./rd01]
  type = 'Exodiff'
  input = 'rd01.i'
  exodiff = 'rd01.e'
  rel_err = 1E-4
  use_old_floor = True
  heavy = true
  max_time = 1000
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model single-phase infiltration and agree with the analytic solution'
  issues = '#13155'
  design = 'porous_flow/tests/infiltration_and_drainage/infiltration_and_drainage_tests.md'
[../]


[./rd02]
  type = 'Exodiff'
  input = 'rd02.i'
  exodiff = 'rd02.e'
  rel_err = 1E-4
  heavy = true
  use_old_floor = True
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model single-phase short-term drainage and agree with the analytic solution'
  issues = '#13155'
  design = 'porous_flow/tests/infiltration_and_drainage/infiltration_and_drainage_tests.md'
[../]


[./rd03]
  type = 'Exodiff'
  input = 'rd03.i'
  exodiff = 'rd03.e'
  rel_err = 1E-4
  use_old_floor = True
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model single-phase long-term drainage and agree with the analytic solution'
  issues = '#13155'
  design = 'porous_flow/tests/infiltration_and_drainage/infiltration_and_drainage_tests.md'
[../]


[./rsc01]
  type = 'Exodiff'
  input = 'rsc01.i'
  exodiff = 'rsc01.e'
  rel_err = 1E-5
  use_old_floor = True
  heavy = true
  max_time = 1000
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model water infiltration into a 2-phase and agree with the analytic solution'
  issues = '#13155'
  design = 'porous_flow/tests/infiltration_and_drainage/infiltration_and_drainage_tests.md'
[../]


[./rsc02]
  type = 'Exodiff'
  input = 'rsc02.i'
  exodiff = 'rsc02.e'
  rel_err = 1E-5
  use_old_floor = True
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model water infiltration into a 2-phase and agree with the analytic solution in a high-resolution test'
  issues = '#13155'
  design = 'porous_flow/tests/infiltration_and_drainage/infiltration_and_drainage_tests.md'
[../]

[./mass01]
  type = 'PetscJacobianTester'
  input = 'mass01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1phase, constant-bulk density, constant porosity, 1-component, fully saturated'
[../]


[./mass01_nodens]
  type = 'PetscJacobianTester'
  input = 'mass01_nodens.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1phase, constant-bulk density, constant porosity, 1-component, fully saturated, in a volume approach'
  issues = '#16841'
  design = 'PorousFlowMassTimeDerivative.md porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./mass02]
  type = 'PetscJacobianTester'
  input = 'mass02.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1phase, constant-bulk density, constant porosity, 1-component, unsaturated'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./mass03]
  type = 'PetscJacobianTester'
  input = 'mass03.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1phase, constant-bulk density, constant porosity, multi-component, unsaturated'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./mass04]
  type = 'PetscJacobianTester'
  input = 'mass04.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 2-phase, constant-bulk density, constant porosity, 2-component'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./mass05]
  type = 'PetscJacobianTester'
  input = 'mass05.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 2-phase, constant-bulk density, constant porosity, multi-component'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./mass05_nodens]
  type = 'PetscJacobianTester'
  input = 'mass05_nodens.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 2-phase, constant-bulk density, constant porosity, multi-component, in a volume formulation'
  issues = '#16841'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./mass06]
  type = 'PetscJacobianTester'
  input = 'mass06.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1-phase, constant-bulk density, constant porosity, 1-component, in a log(mass-density) formulation'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./mass07]
  type = 'PetscJacobianTester'
  input = 'mass07.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1-phase, constant-bulk density, constant porosity, 1-component, in a log(mass-density), volumetric formulation'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./mass08]
  type = 'PetscJacobianTester'
  input = 'mass08.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1-phase, constant-bulk density, HMporosity, 1-component, unsaturated'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./mass09]
  type = 'PetscJacobianTester'
  input = 'mass09.i'
  ratio_tol = 5E-6 # lots of chain rules here
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 2-phase, constant-bulk density, 2-component, PS-formulation'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./mass10]
  type = 'PetscJacobianTester'
  input = 'mass10.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1-phase, constant-bulk density, HM-porosity, 1-component, unsaturated'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./mass10_nodens]
  type = 'PetscJacobianTester'
  input = 'mass10_nodens.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1-phase, constant-bulk density, HM-porosity, 1-component, unsaturated, with a volumetric formulation'
  issues = '#16841'
  design = 'PorousFlowMassTimeDerivative.md porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./mass01_fully_saturated]
  type = 'PetscJacobianTester'
  input = 'mass01_fully_saturated.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass time derivative of 1-phase, with a fully-saturated formulation'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./fflux01]
  type = 'PetscJacobianTester'
  input = 'fflux01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 1-component, unsaturated, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./fflux02]
  type = 'PetscJacobianTester'
  input = 'fflux02.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 3-component, unsaturated, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./fflux03]
  type = 'PetscJacobianTester'
  input = 'fflux03.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 2-phase, 2-component, PS formulation, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./fflux04]
  type = 'PetscJacobianTester'
  input = 'fflux04.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 2-phase, 3-component, PP formulation, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./fflux05]
  type = 'PetscJacobianTester'
  input = 'fflux05.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, log-mass-density formulation, fully-saturated, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./fflux06]
  type = 'PetscJacobianTester'
  input = 'fflux06.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, log-mass-density formulation, unsaturated, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./fflux07]
  type = 'PetscJacobianTester'
  input = 'fflux07.i'
  ratio_tol = 1E-6 # lots of chain rules here
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 2-phase, 2-component with components in both phases, PS formulation, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./fflux08]
  type = 'PetscJacobianTester'
  input = 'fflux08.i'
  ratio_tol = 1E-7 # lots of chain rules here
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 1-component, constant viscosity, Kozeny-Carman permeability, constant fluid-bulk modulus, Corey-relative permeability'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./fflux09]
  type = 'PetscJacobianTester'
  input = 'fflux09.i'
  ratio_tol = 1E-7 # lots of chain rules here
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 2-phase, 3-component, PP formulation, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability, with RSC capilarity'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./fflux10]
  type = 'PetscJacobianTester'
  input = 'fflux10.i'
  ratio_tol = 1E-7 # lots of chain rules here
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 3-component, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability, with BW capilarity'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./fflux11]
  type = 'PetscJacobianTester'
  input = 'fflux11.i'
  ratio_tol = 1E-7 # lots of chain rules here
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 3-component, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability, with VG capilarity with a cubic extension'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./fflux12]
  type = 'PetscJacobianTester'
  input = 'fflux12.i'
  ratio_tol = 1E-7 # lots of chain rules here
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 3-component, constant viscosity, constant permeability, constant fluid-bulk modulus, FLAC-relative permeability'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./fflux13]
  type = 'PetscJacobianTester'
  input = 'fflux13.i'
  ratio_tol = 1E-6 # lots of chain rules here
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 2-phase, 3-component, PP-formulation, constant viscosity, constant permeability, constant fluid-bulk modulus, Corey-relative permeability, with a harmonic-mean mobility'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./fflux01_fully_saturated]
  type = 'PetscJacobianTester'
  input = 'fflux01_fully_saturated.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 3-components, constant viscosity, constant permeability, constant fluid-bulk modulus, fully-saturated formulation'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./fflux02_fully_saturated]
  type = 'PetscJacobianTester'
  input = 'fflux02_fully_saturated.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the fluid flux, with 1-phase, 3-components, constant viscosity, constant permeability, constant fluid-bulk modulus, fully-saturated formulation with strong advection'
  issues = '#16841'
  design = 'PorousFlowFullySaturated.md PorousFlowFullySaturatedAdvectiveFlux.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./eff_stress01]
  type = 'PetscJacobianTester'
  input = 'eff_stress01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the effective stress, with 2-phase, 2-component, PP formulation'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./eff_stress02]
  type = 'PetscJacobianTester'
  input = 'eff_stress02.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the effective stress, with 2-phase, 2-component, PS formulation'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./eff_stress03]
  type = 'PetscJacobianTester'
  input = 'eff_stress03.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the effective stress, with 2-phase, 2-component, PP formulation, in RZ coordinates'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./eff_stress04]
  type = 'PetscJacobianTester'
  input = 'eff_stress04.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the effective stress, with 2-phase, 2-component, PS formulation, in RZ coordinates'
  issues = '#6845 #12506'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./mass_vol_exp01]
  type = 'PetscJacobianTester'
  input = 'mass_vol_exp01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass volumetric expansion, with constant bulk modulus, constant porosity and VG capilarity'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./mass_vol_exp02]
  type = 'PetscJacobianTester'
  input = 'mass_vol_exp02.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass volumetric expansion, with constant bulk modulus, HM porosity and VG capilarity'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./mass_vol_exp03]
  type = 'PetscJacobianTester'
  input = 'mass_vol_exp03.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass volumetric expansion, with constant bulk modulus, HM porosity and VG capilarity, in a volumetric formulation'
  issues = '#16841'
  design = 'PorousFlowMassVolumetricExpansion.md porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./pls01]
  type = 'PetscJacobianTester'
  input = 'pls01.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the piecewise linear sink, with 1-phase and 1-component'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./pls02]
  type = 'PetscJacobianTester'
  input = 'pls02.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the piecewise linear sink, with 2-phase and 2-components'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./pls03]
  type = 'PetscJacobianTester'
  input = 'pls03.i'
  ratio_tol = 1E-6
  cli_args = 'Executioner/num_steps=1'
  difference_tol = 1E10
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the piecewise linear sink, with 2-phase and 3-components'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./pls04]
  type = 'PetscJacobianTester'
  input = 'pls04.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the piecewise linear sink, with 2-phase and 3-components, with enthalpy, internal energy and thermal conductivity'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./hgs01]
  type = 'PetscJacobianTester'
  input = 'hgs01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the half-gaussian sink'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./hcs01]
  type = 'PetscJacobianTester'
  input = 'hcs01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the half-cubic sink of fluid'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./hcs02]
  type = 'PetscJacobianTester'
  input = 'hcs02.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the half-cubic sink of heat'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./hcond01]
  type = 'PetscJacobianTester'
  input = 'hcond01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the heat conduction, with 0 phases'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./hcond02]
  type = 'PetscJacobianTester'
  input = 'hcond02.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the heat conduction, with 2 phases'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./denergy01]
  type = 'PetscJacobianTester'
  input = 'denergy01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the energy-density time derivative, with 0 phases'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./denergy02]
  type = 'PetscJacobianTester'
  input = 'denergy02.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the energy-density time derivative, with 2-phase, 1-component, with solid displacements'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./denergy03]
  type = 'PetscJacobianTester'
  input = 'denergy03.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the energy-density time derivative, with 2-phase, 1-component, with solid displacements, and TM porosity'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./denergy04]
  type = 'PetscJacobianTester'
  input = 'denergy04.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the energy-density time derivative, with 2-phase, 1-component, with solid displacements, and THM porosity'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./denergy05]
  type = 'PetscJacobianTester'
  input = 'denergy05.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the energy-density time derivative, with 2-phase, 1-component, with solid displacements, and THM porosity, compressive strains and ensuring porosity remains positivie'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./heat_advection01]
  type = 'PetscJacobianTester'
  input = 'heat_advection01.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the heat advection, with 1 phase, unsaturated'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./heat_advection02]
  type = 'PetscJacobianTester'
  input = 'heat_advection02.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the heat advection, with 2 phase, unsaturated'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./heat_advection01_fully_saturated]
  type = 'PetscJacobianTester'
  input = 'heat_advection01_fully_saturated.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the heat advection, with 1 phase, fully-saturated formulation'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./heat_advection01_fullsat_upwind]
  type = 'PetscJacobianTester'
  input = 'heat_advection01_fullsat_upwind.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the heat advection, with 1 phase, fully-saturated, fully-upwinded formulation'
  issues = '#16841'
  design = 'PorousFlowFullySaturatedUpwindHeatAdvection.md porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./diff01]
  type = 'PetscJacobianTester'
  input = 'diff01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the diffusion'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./diff02]
  type = 'PetscJacobianTester'
  input = 'diff02.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the diffusion with constant tortuousity and diffusivity'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./diff03]
  type = 'PetscJacobianTester'
  input = 'diff03.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the diffusion  with 2-phases, with saturation-dependent tortuousity and MQ diffusion coefficients'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./disp01]
  type = 'PetscJacobianTester'
  input = 'disp01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the transverse dispersion'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./disp02]
  type = 'PetscJacobianTester'
  input = 'disp02.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the transverse dispersion and diffusion'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./disp03]
  type = 'PetscJacobianTester'
  input = 'disp03.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the transverse and longitudinal dispersion'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./disp04]
  type = 'PetscJacobianTester'
  input = 'disp04.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the transverse and longitudinal dispersion and diffusion'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./heat_vol_exp01]
  type = 'PetscJacobianTester'
  input = 'heat_vol_exp01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the heat volumetric expansion, 1phase with constant bulk modulus, VG capilarity and THM porosity'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./phe01]
  type = 'PetscJacobianTester'
  input = 'phe01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the plastic heat energy'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./line_sink01]
  type = 'PetscJacobianTester'
  input = 'line_sink01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the a peaceman line sink, with 2-phase, 3-components, with enthalpy, internal energy and thermal conductivity'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./line_sink02]
  type = 'PetscJacobianTester'
  input = 'line_sink02.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the a poly-line sink, with 2-phase, 3-components, with enthalpy, internal energy and thermal conductivity'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./line_sink03]
  type = 'PetscJacobianTester'
  input = 'line_sink03.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the a peaceman sink, with 2-phase, 3-components, with enthalpy, internal energy and thermal conductivity, and with many points within each element'
  issues = '#6845 #10471 #16255'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./line_sink01_5]
  type = 'PetscJacobianTester'
  input = 'line_sink01.i'
  cli_args = 'DiracKernels/dirac4/point_file=five_points.bh DiracKernels/dirac5/point_file=five_points.bh DiracKernels/dirac6/point_file=five_points.bh Executioner/num_steps=1'
  ratio_tol = 1E-7
  difference_tol = 1E10
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the a peaceman sink, with 2-phase, 3-components, with enthalpy, internal energy and thermal conductivity, and with 5 points within each element'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./line_sink02_5]
  type = 'PetscJacobianTester'
  input = 'line_sink02.i'
  cli_args = 'DiracKernels/dirac4/point_file=five_points.bh DiracKernels/dirac5/point_file=five_points.bh DiracKernels/dirac6/point_file=five_points.bh Executioner/num_steps=1'
  ratio_tol = 1E-7
  difference_tol = 1E10
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the a poly-line sink, with 2-phase, 3-components, with enthalpy, internal energy and thermal conductivity, and with 5 points within each element'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./line_sink04]
  type = 'PetscJacobianTester'
  input = 'line_sink04.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the a poly-line sink, with 2-phase, 3-components, with enthalpy, internal energy and thermal conductivity, and with 1 point within each element'
  issues = '#6845 #10471'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./desorped_mass01]
  type = 'PetscJacobianTester'
  input = 'desorped_mass01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the desorbed mass'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./desorped_mass_vol_exp01]
  type = 'PetscJacobianTester'
  input = 'desorped_mass_vol_exp01.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the volumetric expansion of desorbed mass'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./waterncg_twophase]
  type = 'PetscJacobianTester'
  input = 'waterncg_twophase.i'
  ratio_tol = 1e-6 # Lots of chain rule derivatives
  difference_tol = 1e10
  cli_args = '-mat_fd_type ds Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the non-condensible gas version of water, 2 phase'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./waterncg_liqiud]
  type = 'PetscJacobianTester'
  input = 'waterncg_liquid.i'
  ratio_tol = 1e-6
  difference_tol = 1e10
  cli_args = '-mat_fd_type ds Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the non-condensible gas version of water, 1 liquid phase'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./waterncg_gas]
  type = 'PetscJacobianTester'
  input = 'waterncg_gas.i'
  ratio_tol = 1e-6 # Lots of chain rule derivatives
  difference_tol = 1e10
  cli_args = '-mat_fd_type ds Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the non-condensible gas version of water, 1 gas phase'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./waterncg_twophase_nonisothermal]
  type = 'PetscJacobianTester'
  input = 'waterncg_twophase_nonisothermal.i'
  ratio_tol = 1e-6 # Lots of chain rule derivatives
  difference_tol = 1e10
  cli_args = '-mat_fd_type ds Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the non-condensible gas version of water, 2 phase, nonisothermal'
  issues = '#6845 #10167'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./brineco2_twophase]
  type = 'PetscJacobianTester'
  input = 'brineco2_twophase.i'
  ratio_tol = 1e-6 # Lots of chain rule derivatives
  difference_tol = 1e10
  cli_args = '-mat_fd_type ds Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the brine equation of state, 2 phase'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./brineco2_liquid]
  type = 'PetscJacobianTester'
  input = 'brineco2_liquid.i'
  ratio_tol = 1e-6 # Lots of chain rule derivatives
  difference_tol = 1e10
  cli_args = '-mat_fd_type ds Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the brine equation of state, 1 liquid phase'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./brineco2_gas]
  type = 'PetscJacobianTester'
  input = 'brineco2_gas.i'
  ratio_tol = 1e-6 # Lots of chain rule derivatives
  difference_tol = 1e10
  cli_args = '-mat_fd_type ds Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the brine equation of state, 1 gas phase'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./brineco2_twophase_nonisothermal]
  type = 'PetscJacobianTester'
  input = 'brineco2_twophase_nonisothermal.i'
  ratio_tol = 1e-6 # Lots of chain rule derivatives
  difference_tol = 1e10
  cli_args = '-mat_fd_type ds Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the brine equation of state, 2 phase, nonisothermal'
  issues = '#6845 #10167'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./brineco2_liquid_2]
  type = 'PetscJacobianTester'
  input = 'brineco2_liquid_2.i'
  ratio_tol = 1e-6 # Lots of chain rule derivatives
  difference_tol = 1e10
  cli_args = '-mat_fd_type ds Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the brine equation of state, 1 phase with salt fraction as a variable'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./exponential_decay]
  type = 'PetscJacobianTester'
  input = 'exponential_decay.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the exponential decay'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./chem01]
  type = 'PetscJacobianTester'
  input = 'chem01.i'
  ratio_tol = 1E-3 # lots of crazy chain rules
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissoluation not depending on temperature'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./chem02]
  type = 'PetscJacobianTester'
  input = 'chem02.i'
  ratio_tol = 1E-5 # lots of crazy chain rules
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the chemical precipitation not depending on temperature'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./chem03]
  type = 'PetscJacobianTester'
  input = 'chem03.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution depending on temperature'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./chem04]
  type = 'PetscJacobianTester'
  input = 'chem04.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the chemical precipitation not depending on temperature'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./chem05]
  type = 'PetscJacobianTester'
  input = 'chem05.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution not depending on temperature where one concentration is initialized to zero, and the stoichiometry is > 1'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./chem06]
  type = 'PetscJacobianTester'
  input = 'chem06.i'
  ratio_tol = 1E-4
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution not depending on temperature where one concentration is initialized to zero, and the stoichiometry is = 1'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./chem07]
  type = 'PetscJacobianTester'
  input = 'chem07.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution not depending on temperature where the concentrations are initialized to zero'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./chem08]
  type = 'PetscJacobianTester'
  input = 'chem08.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution depending on temperature where one concentration is initialized to zero, and the stoichiometry is > 1'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./chem09]
  type = 'PetscJacobianTester'
  input = 'chem09.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution depending on temperature where one concentration is initialized to zero, and the stoichiometry is = 1'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./chem10]
  type = 'PetscJacobianTester'
  input = 'chem10.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution depending on temperature where concentrations are initialized to zero'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./chem11]
  type = 'PetscJacobianTester'
  input = 'chem11.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution depending on temperature with 3 primary variables and 4 reactions'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./chem12]
  type = 'PetscJacobianTester'
  input = 'chem12.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution depending on temperature with 3 primary variables and 4 reactions, with negative initial concentrations'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./chem13]
  type = 'PetscJacobianTester'
  input = 'chem13.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the chemical dissolution depending on temperature with 3 primary variables and 4 reactions, with some zero initial concentrations'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./chem14]
  type = 'PetscJacobianTester'
  input = 'chem14.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the porosity depending on chemical concentrations'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./chem15]
  type = 'PetscJacobianTester'
  input = 'chem15.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the mass-fractions that depend on chemical concentrations'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./basic_advection1]
  type = 'PetscJacobianTester'
  input = 'basic_advection1.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the basic advection with a pre-defined velocity vector, in the 0-phase, no temperature case'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./basic_advection2]
  type = 'PetscJacobianTester'
  input = 'basic_advection2.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the basic advection with a Darcy velocity vector in the fully-saturated, constant permeability, constant viscosity case'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./basic_advection3]
  type = 'PetscJacobianTester'
  input = 'basic_advection3.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the basic advection with a Darcy velocity vector in the unsaturated, constant permeability, constant viscosity case'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./basic_advection4]
  type = 'PetscJacobianTester'
  input = 'basic_advection4.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the basic advection with a Darcy velocity vector in the unsaturated, non-isothermal, constant permeability, constant viscosity case'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./basic_advection5]
  type = 'PetscJacobianTester'
  input = 'basic_advection5.i'
  ratio_tol = 1E-7
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the basic advection with a Darcy velocity vector in the unsaturated case'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./basic_advection6]
  type = 'PetscJacobianTester'
  input = 'basic_advection6.i'
  ratio_tol = 1E-5
  difference_tol = 1E10
  cli_args = 'Executioner/num_steps=1'
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the basic advection with a Darcy velocity vector in the 2-phase PP case'
  issues = '#6845'
  design = 'porous_flow/tutorial_09.md porous_flow/tutorial_02.md porous_flow/solvers.md porous_flow/nonlinear_convergence_problems.md PorousFlowDictator.md'
[../]


[./esbc01]
  type = 'PetscJacobianTester'
  input = 'esbc01.i'
  ratio_tol = 1E-8
  difference_tol = 1E10
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the enthalpy sink, where porepressure is specified'
  issues = '#15742'
  design = 'PorousFlowEnthalpySink.md'
[../]


[./esbc02]
  type = 'PetscJacobianTester'
  input = 'esbc02.i'
  ratio_tol = 1E-9
  difference_tol = 1E10
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the enthalpy sink, where external pressure is specified'
  issues = '#15742'
  design = 'PorousFlowEnthalpySink.md'
[../]


[./hfrompps]
  type = 'PetscJacobianTester'
  input = 'hfrompps.i'
  ratio_tol = 1E-5
  difference_tol = 1E10
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the enthalpy source'
  issues = '#15742'
  design = 'PorousFlowPointEnthalpySourceFromPostprocessor.md'
[../]


[./outflowbc01]
  type = 'PetscJacobianTester'
  input = 'outflowbc01.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the outflow boundary condition, 1-phase, 1-component'
  issues = '#18037'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md PorousFlowOutflowBC.md'
[../]


[./outflowbc02]
  type = 'PetscJacobianTester'
  input = 'outflowbc02.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the outflow heat boundary condition, 1-phase, 1-component'
  issues = '#18037'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md PorousFlowOutflowBC.md'
[../]


[./outflowbc03]
  type = 'PetscJacobianTester'
  input = 'outflowbc03.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the outflow fluid and heat boundary conditions, 1-phase, multi-component'
  issues = '#18037'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md PorousFlowOutflowBC.md'
[../]


[./outflowbc04]
  type = 'PetscJacobianTester'
  input = 'outflowbc04.i'
  ratio_tol = 1E-6
  difference_tol = 1E10
  threading = '!pthreads'
  requirement = 'PorousFlow shall compute all Jacobian entries of Kernels for the outflow fluid boundary conditions, multi-phase, multi-component'
  issues = '#18037'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md PorousFlowOutflowBC.md'
[../]


[./linear_por]
  type = PetscJacobianTester
  input = linear_por.i
  ratio_tol = 1E-6
  difference_tol = 1E10
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate the analytic Jacobian of systems that include a porosity that is a linear function of effective porepressure, temperature and volumetric strain'
  issues = '#18079'
  design = 'porous_flow/porosity.md PorousFlowPorosityLinear.md'
[]

[./mass01]
  type = 'CSVDiff'
  input = 'mass01.i'
  csvdiff = 'mass01.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall correctly compuate the total fluid mass in a single-phase, single-component fluid'
  design = 'porous_flow/tests/mass_conservation/mass_conservation_tests.md PorousFlowFluidMass.md'
  issues = '#13155'
[../]


[./mass02]
  type = 'CSVDiff'
  input = 'mass02.i'
  csvdiff = 'mass02.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall correctly compuate the total fluid masses in a single-phase, multi-component fluid'
  design = 'porous_flow/tests/mass_conservation/mass_conservation_tests.md PorousFlowFluidMass.md'
  issues = '#13155'
[../]


[./mass03]
  type = 'CSVDiff'
  input = 'mass03.i'
  csvdiff = 'mass03.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall correctly compuate the evolution of fluid mass when there is a source of fluid'
  design = 'porous_flow/tests/mass_conservation/mass_conservation_tests.md PorousFlowFluidMass.md'
  issues = '#13155'
[../]


[./mass04]
  type = 'CSVDiff'
  input = 'mass04.i'
  csvdiff = 'mass04.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall conserve mass in a material with impermeable boundaries that is compressed mechanically'
  design = 'porous_flow/tests/mass_conservation/mass_conservation_tests.md PorousFlowFluidMass.md'
  issues = '#13155 #18324'
[../]


[./mass05]
  type = 'CSVDiff'
  input = 'mass05.i'
  csvdiff = 'mass05.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall correctly compuate the total fluid masses in a multi-phase, multi-component fluid'
  design = 'porous_flow/tests/mass_conservation/mass_conservation_tests.md PorousFlowFluidMass.md'
  issues = '#13155'
[../]


[./mass06]
  type = 'CSVDiff'
  input = 'mass06.i'
  csvdiff = 'mass06.csv'
  compiler = '!INTEL'
  threading = '!pthreads'
  requirement = 'PorousFlow shall correctly compuate the component and phase fluid masses in a multi-phase, multi-component fluid, at all saturations, and above a saturation threshold'
  design = 'porous_flow/tests/mass_conservation/mass_conservation_tests.md PorousFlowFluidMass.md'
  issues = '#13155'
[../]


[./mass07]
  type = 'RunException'
  input = 'mass07.i'
  expect_err = 'The Dictator decrees that the number of phases in this simulation is 2 but you have entered 3 phases.'
  threading = '!pthreads'
  requirement = 'If the phase number exceeds the number of phases in the system, PorousFlow shall produce an appropriate error message and exit'
  design = 'porous_flow/tests/mass_conservation/mass_conservation_tests.md PorousFlowFluidMass.md'
  issues = '#13155'
[../]


[./mass08]
  type = 'RunException'
  input = 'mass08.i'
  expect_err = 'The Dictator proclaims that the phase index 2 is greater than the largest phase index possible, which is 1'
  threading = '!pthreads'
  requirement = 'If the phase index exceeds the number of phases in the system, PorousFlow shall produce an appropriate error message and exit'
  design = 'porous_flow/tests/mass_conservation/mass_conservation_tests.md PorousFlowFluidMass.md'
  issues = '#13155'
[../]


[./mass09]
  type = 'RunException'
  input = 'mass09.i'
  expect_err = 'A single phase_index must be entered when prescribing a saturation_threshold'
  threading = '!pthreads'
  requirement = 'If a saturation threshold is used in computing the fluid mass, and a phase index is not provided, PorousFlow shall produce an appropriate error message and exit'
  design = 'porous_flow/tests/mass_conservation/mass_conservation_tests.md PorousFlowFluidMass.md'
  issues = '#13155'
[../]


[./mass10]
  type = 'RunException'
  input = 'mass10.i'
  expect_err = 'The Dictator pronounces that the number of PorousFlow variables is 2, however you have used 2. This is an error'
  threading = '!pthreads'
  requirement = 'If the user enters a PorousFlow variable number that is not less than the number of PorousFlow variables, PorousFlow shall produce an appropriate error message and exit'
  design = 'porous_flow/tests/mass_conservation/mass_conservation_tests.md PorousFlowFluidMass.md'
  issues = '#13155'
[../]


[./mass11]
  type = 'CSVDiff'
  input = 'mass11.i'
  csvdiff = 'mass11_csv.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall conserve mass in a material with impermeable boundaries that is allowed to expand mechanically while being injected with fluid'
  design = 'porous_flow/tests/mass_conservation/mass_conservation_tests.md PorousFlowFluidMass.md'
  issues = '#18324'
[../]


[./mass12]
  type = 'CSVDiff'
  input = 'mass12.i'
  csvdiff = 'mass12_csv.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall conserve mass in an annular material with impermeable boundaries that is compressed verticaly'
  design = 'porous_flow/tests/mass_conservation/mass_conservation_tests.md PorousFlowFluidMass.md'
  issues = '#18324'
[../]


[./mass13]
  type = 'CSVDiff'
  input = 'mass13.i'
  csvdiff = 'mass13_csv.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall conserve mass in an annular material with impermeable boundaries that is compressed radially'
  design = 'porous_flow/tests/mass_conservation/mass_conservation_tests.md PorousFlowFluidMass.md'
  issues = '#18324'
[../]

[nc01]
  type = 'CSVDiff'
  input = 'nc01.i'
  csvdiff = 'nc01_porepressure_0101.csv'
  rel_err = 1E-5
  heavy = True
  max_time = 1000
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model transient newton cooling acting on the fluid mass and agree with the analytic solution'
  issues = '#13155 #16953'
  design = 'porous_flow/tests/newton_cooling/newton_cooling_tests.md'
[]


[nc02]
  type = 'CSVDiff'
  input = 'nc02.i'
  csvdiff = 'nc02_porepressure_0001.csv'
  rel_err = 1E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model steady-state newton cooling acting on the fluid mass and agree with the analytic solution'
  issues = '#13155'
  design = 'porous_flow/tests/newton_cooling/newton_cooling_tests.md'
[]


[nc04]
  type = 'CSVDiff'
  input = 'nc04.i'
  csvdiff = 'nc04_temp_0001.csv'
  rel_err = 1E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model steady-state newton cooling acting on the temperature and agree with the analytic solution'
  issues = '#13155'
  design = 'porous_flow/tests/newton_cooling/newton_cooling_tests.md'
[]


[nc06]
  type = 'CSVDiff'
  input = 'nc06.i'
  csvdiff = 'nc06_porepressure_0001.csv nc06_temperature_0001.csv'
  rel_err = 1E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model newton cooling acting on the porepressure and at the same time extracting heat along with the extracted fluid and agree with the analytic solution'
  issues = '#13155'
  design = 'porous_flow/tests/newton_cooling/newton_cooling_tests.md'
[]


[nc08]
  type = 'CSVDiff'
  input = 'nc08.i'
  csvdiff = 'nc08_porepressure_0001.csv nc08_temperature_0001.csv'
  rel_err = 1E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model newton cooling acting on the porepressure of an ideal gas and at the same time extracting heat along with the extracted gas and agree with the analytic solution'
  issues = '#13155'
  design = 'porous_flow/tests/newton_cooling/newton_cooling_tests.md'
[]

[./framework]
  type = 'CSVDiff'
  input = 'framework.i'
  csvdiff = 'framework_out_tracer_0011.csv'
  abs_zero = 1.0E-5
  threading = '!pthreads'
  requirement = "The system shall be able to solve the advection equation"
  issues = '#12346'
  design = 'porous_flow/numerical_diffusion.md'
[../]


[./fully_saturated_action]
  type = 'CSVDiff'
  input = 'fully_saturated_action.i'
  csvdiff = 'fully_saturated_action_out_tracer_0011.csv'
  abs_zero = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to solve the advection of fluid species, using mass lumping and no upwinding, employing an Action"
  issues = '#11013'
  design = 'porous_flow/numerical_diffusion.md'
[../]


[./no_action]
  type = 'CSVDiff'
  input = 'no_action.i'
  csvdiff = 'no_action_out_tracer_0011.csv'
  abs_zero = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to solve the advection of fluid species, using mass lumping and full upwinding, without employing an action"
  issues = '#11013'
  design = 'porous_flow/numerical_diffusion.md'
[../]


[./fully_saturated_upwinded]
  type = 'CSVDiff'
  input = 'fully_saturated_action.i'
  cli_args = 'Outputs/file_base=no_action_out PorousFlowFullySaturated/stabilization=Full'
  prereq = no_action
  csvdiff = 'no_action_out_tracer_0011.csv'
  abs_zero = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to solve the advection of fluid species in a fully-saturated single-phase situation, using mass lumping and full upwinding, via employing an action"
  issues = '#16841'
  design = 'porous_flow/numerical_diffusion.md'
[../]


[./fully_saturated_KT]
  type = 'CSVDiff'
  input = 'fully_saturated_action.i'
  cli_args = 'Outputs/file_base=fully_saturated_action_KT PorousFlowFullySaturated/stabilization=KT'
  csvdiff = 'fully_saturated_action_KT_tracer_0011.csv'
  heavy = true
  abs_zero = 1.0E-5
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to solve the advection of fluid species in a fully-saturated single-phase situation, using mass lumping and KT upwinding, via employing an action"
  issues = '#16841'
  design = 'porous_flow/numerical_diffusion.md'
[../]


[./fltvd_no_antidiffusion]
  type = 'CSVDiff'
  input = 'fltvd_no_antidiffusion.i'
  csvdiff = 'fltvd_no_antidiffusion_out_tracer_0011.csv'
  abs_zero = 1.0E-5
  threading = '!pthreads'
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization, but be able to use no antidiffusion'
[../]


[./fltvd]
  type = 'CSVDiff'
  input = 'fltvd.i'
  csvdiff = 'fltvd_out_tracer_0101.csv'
  abs_zero = 1.0E-5
  threading = '!pthreads'
  issues = '#12370 #12118 #10426'
  design = 'porous_flow/numerical_diffusion.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization'
[../]


[./pffltvd]
  type = 'CSVDiff'
  input = 'pffltvd.i'
  csvdiff = 'pffltvd_out_tracer_0101.csv'
  abs_zero = 1.0E-5
  threading = '!pthreads'
  heavy = true
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization for PorousFlow simulations.  The advection via the Darcy velocity shall have the correct velocity.  With no flux-limiter the results should be the same as full upwinding.  The results for simulations involving PorousFlow Kernels and UserObjects when the Darcy velocity is constant shall be the same as the constant-velocity, non-PorousFlow case.'
[../]


[./pffltvd_action]
  type = 'CSVDiff'
  input = 'pffltvd_action.i'
  csvdiff = 'pffltvd_out_tracer_0101.csv'
  abs_zero = 1.0E-5
  threading = '!pthreads'
  prereq = 'pffltvd'
  heavy = true
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization for PorousFlow simulations and the user shall be able to use the PorousFlow Action system to choose the Kuzmin-Turek stabilization for single-phase, multi-component fluid flow'
[../]

[./tensile01]
  type = 'CSVDiff'
  input = 'tensile01.i'
  csvdiff = 'tensile01.csv'
  threading = '!pthreads'
  requirement = "PorousFlow shall model heat generated from plastic deformation, including tensile failure"
  issues = '#13155'
  design = 'porous_flow/tests/plastic_heating/plastic_heating_tests.md PorousFlowPlasticHeatEnergy.md'
[../]


[./compressive01]
  type = 'CSVDiff'
  input = 'compressive01.i'
  csvdiff = 'compressive01.csv'
  threading = '!pthreads'
  requirement = "PorousFlow shall model heat generated from plastic deformation, including compressive failure"
  issues = '#13155'
  design = 'porous_flow/tests/plastic_heating/plastic_heating_tests.md PorousFlowPlasticHeatEnergy.md'
[../]


[./shear01]
  type = 'CSVDiff'
  input = 'shear01.i'
  csvdiff = 'shear01.csv'
  threading = '!pthreads'
  requirement = "PorousFlow shall model heat generated from plastic deformation, including shear failure"
  issues = '#13155'
  design = 'porous_flow/tests/plastic_heating/plastic_heating_tests.md PorousFlowPlasticHeatEnergy.md'
[../]

[./vol_expansion]
  type = Exodiff
  input = vol_expansion.i
  exodiff = vol_expansion.e
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity in the situation where increasing porepressure leads to volumetric expansion'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./undrained_oedometer]
  type = CSVDiff
  input = undrained_oedometer.i
  csvdiff = undrained_oedometer.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to simulate an undrained oedometer test'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./pp_generation]
  type = CSVDiff
  input = pp_generation.i
  csvdiff = pp_generation.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-constrained solid'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./pp_generation_action]
  type = CSVDiff
  input = pp_generation_action.i
  csvdiff = pp_generation_action.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-constrained solid, using PorousFlow Actions'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./pp_generation_fullysat_action]
  type = CSVDiff
  input = pp_generation_fullysat_action.i
  csvdiff = pp_generation_fullysat_action.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-constrained solid, using a fully-saturated formulation'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./pp_generation_unconfined]
  type = CSVDiff
  input = pp_generation_unconfined.i
  csvdiff = pp_generation_unconfined.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-unconstrained solid'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./pp_generation_unconfined_constM]
  type = CSVDiff
  input = pp_generation_unconfined_constM.i
  csvdiff = pp_generation_unconfined_constM.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-unconstrained solid, using a constant Biot modulus'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./pp_generation_unconfined_constM_action]
  type = CSVDiff
  input = pp_generation_unconfined_constM_action.i
  prereq = pp_generation_unconfined_constM
  cli_args = 'Outputs/file_base=pp_generation_unconfined_constM'
  csvdiff = pp_generation_unconfined_constM.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-unconstrained solid, using a constant Biot modulus, and be able to simulate this using an Action'
  issues = '#16841'
  design = 'PorousFlowFullySaturated.md porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./pp_generation_unconfined_fully_saturated]
  type = CSVDiff
  input = pp_generation_unconfined_fully_saturated.i
  csvdiff = pp_generation_unconfined_fully_saturated.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-unconstrained solid, using a fully-saturated formulation'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./pp_generation_unconfined_fully_saturated_volume]
  type = CSVDiff
  input = pp_generation_unconfined_fully_saturated_volume.i
  csvdiff = pp_generation_unconfined_fully_saturated_volume.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-unconstrained solid, using a fully-saturated formulation, based on fluid volumes instead of fluid masses'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./pp_generation_unconfined_basicthm]
  type = CSVDiff
  input = pp_generation_unconfined_basicthm.i
  csvdiff = pp_generation_unconfined_basicthm.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate fluid injection into a mechanically-unconstrained solid, using a Actions'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./mandel]
  type = CSVDiff
  input = mandel.i
  csvdiff = mandel.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Mandel consolidation of a drained medium'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./mandel_constM]
  type = CSVDiff
  input = mandel_constM.i
  csvdiff = mandel_constM.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Mandel consolidation of a drained medium, using a constant Biot modulus'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./mandel_fully_saturated]
  type = CSVDiff
  input = mandel_fully_saturated.i
  csvdiff = mandel_fully_saturated.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Mandel consolidation of a drained medium, using a fully-saturated formalism'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./mandel_fully_saturated_volume]
  type = CSVDiff
  input = mandel_fully_saturated_volume.i
  csvdiff = mandel_fully_saturated_volume.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Mandel consolidation of a drained medium, using a fully-saturated formalism based on fluid volume instaed of the usual fluid mass'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./mandel_basicthm]
  type = CSVDiff
  input = mandel_basicthm.i
  csvdiff = mandel_basicthm.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Mandel consolidation of a drained medium, using Actions'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./terzaghi]
  type = CSVDiff
  input = terzaghi.i
  csvdiff = terzaghi.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Terzaghi consolidation of a drained medium'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./terzaghi_constM]
  type = CSVDiff
  input = terzaghi_constM.i
  csvdiff = terzaghi_constM.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Terzaghi consolidation of a drained medium, using a constant Biot modulus'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./terzaghi_fully_saturated_volume]
  type = CSVDiff
  input = terzaghi_fully_saturated_volume.i
  csvdiff = terzaghi_fully_saturated_volume.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Terzaghi consolidation of a drained medium, using a fully-saturated formalism'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./terzaghi_basicthm]
  type = CSVDiff
  input = terzaghi_basicthm.i
  csvdiff = terzaghi_basicthm.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to correctly simulate Terzaghi consolidation of a drained medium, using Actions'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]


[./vol_expansion_poroperm]
  type = CSVDiff
  input = vol_expansion_poroperm.i
  csvdiff = vol_expansion_poroperm.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model standard poroelasticity and be able to calculate porosity and permeability increases in an unconfined sample where porepressure is increased'
  issues = '#13155'
  design = 'porous_flow/tests/poro_elasticity/poro_elasticity_tests.md'
[../]

[PermFromPoro01]
  type = 'CSVDiff'
  input = 'PermFromPoro01.i'
  csvdiff = 'PermFromPoro01_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate permeability as a Kozeny-Carman function of porosity, where permeability is defined via setting a grain size'
  issues = '#7632'
  design = 'porous_flow/permeability.md PorousFlowPermeabilityKozenyCarman.md'
[]


[PermFromPoro02]
  type = 'CSVDiff'
  input = 'PermFromPoro02.i'
  csvdiff = 'PermFromPoro02_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate permeability as a Kozeny-Carman function of porosity, where permeability is defined via setting a reference value of porosity'
  issues = '#7632'
  design = 'porous_flow/permeability.md PorousFlowPermeabilityKozenyCarman.md'
[]


[PermFromPoro03]
  type = 'CSVDiff'
  input = 'PermFromPoro03.i'
  csvdiff = 'PermFromPoro03_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate permeability as an exponential function of porosity, where an anisotropy is specified, and k is defined through an exponential function'
  issues = '#7632'
  design = 'porous_flow/permeability.md PorousFlowPermeabilityExponential.md'
[]


[PermFromPoro04]
  type = 'CSVDiff'
  input = 'PermFromPoro04.i'
  csvdiff = 'PermFromPoro04_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate permeability as an exponential function of porosity, where an anisotropy is specified, and log(k) is defined through a linear function'
  issues = '#7632'
  design = 'porous_flow/permeability.md PorousFlowPermeabilityExponential.md'
[]


[PermFromPoro05]
  type = 'CSVDiff'
  input = 'PermFromPoro05.i'
  csvdiff = 'PermFromPoro05_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate permeability as an exponential function of porosity, where an anisotropy is specified, and ln(k) is defined through a linear function'
  issues = '#7632'
  design = 'porous_flow/permeability.md PorousFlowPermeabilityExponential.md'
[]


[poro_thm]
  type = CSVDiff
  input = poro_thm.i
  csvdiff = poro_thm_out.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate porosity for thermo-hydro-mechanical coupled models'
  issues = '#10847'
  design = 'porous_flow/porosity.md PorousFlowPorosity.md'
[]


[poro_tm]
  type = CSVDiff
  input = poro_tm.i
  csvdiff = poro_tm_out.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate porosity for thermo-mechanical coupled models'
  issues = '#10847'
  design = 'porous_flow/porosity.md PorousFlowPorosity.md'
[]


[poro_hm]
  type = CSVDiff
  input = poro_hm.i
  csvdiff = poro_hm_out.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate porosity for hydro-mechanical coupled models'
  issues = '#10847'
  design = 'porous_flow/porosity.md PorousFlowPorosity.md'
[]


[except1]
  type = RunException
  input = except1.i
  expect_err = 'PorousFlowPorosity: When thermal=true you must provide a thermal_expansion_coeff'
  threading = '!pthreads'
  requirement = 'PorousFlow shall produce an error if the porosity depends on temperature but no thermal expansion coefficient is provided'
  issues = '#10847'
  design = 'porous_flow/porosity.md PorousFlowPorosity.md'
[]


[except2]
  type = RunException
  input = except2.i
  expect_err = 'PorousFlowPorosity: When fluid=true you must provide a solid_bulk'
  threading = '!pthreads'
  requirement = 'PorousFlow shall produce an error if the porosity depends on porepressure but no solid bulk modulus is provided'
  issues = '#10847'
  design = 'porous_flow/porosity.md PorousFlowPorosity.md'
[]


[PermTensorFromVar01]
  type = 'CSVDiff'
  input = 'PermTensorFromVar01.i'
  csvdiff = 'PermTensorFromVar01_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate permeability as a product of an anisotropic tensor and a constant term'
  issues = '#8061'
  design = 'porous_flow/permeability.md PorousFlowPermeabilityConstFromVar.md'
[]


[PermTensorFromVar02]
  type = 'CSVDiff'
  input = 'PermTensorFromVar02.i'
  csvdiff = 'PermTensorFromVar02_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate permeability as a product of an anisotropic tensor and a spatially-varying variable'
  issues = '#8061'
  design = 'porous_flow/permeability.md PorousFlowPermeabilityConstFromVar.md'
[]


[PermTensorFromVar03]
  type = 'CSVDiff'
  input = 'PermTensorFromVar03.i'
  csvdiff = 'PermTensorFromVar03_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate isotropic, spatially-varying permeability'
  issues = '#8061'
  design = 'porous_flow/permeability.md PorousFlowPermeabilityConstFromVar.md'
[]


[linear_except1]
  type = RunException
  input = linear_except1.i
  cli_args = 'Materials/inactive=pf Materials/porosity/P_coeff=1'
  expect_err = 'PorousFlowPorosityLinear: When P_coeff is given you must have an effective fluid pressure Material'
  match_literal = true
  threading = '!pthreads'
  requirement = 'PorousFlow shall produce an error if a linear porosity relationship that depends on effective fluid pressure is used if there is no effective fluid pressure material'
  issues = '#18079'
  design = 'porous_flow/porosity.md PorousFlowPorosityLinear.md'
[]


[linear_except2]
  type = RunException
  input = linear_except1.i
  cli_args = 'Materials/inactive=temperature Materials/porosity/T_coeff=1'
  expect_err = 'PorousFlowPorosityLinear: When T_coeff is given you must have a temperature Material'
  match_literal = true
  threading = '!pthreads'
  requirement = 'PorousFlow shall produce an error if a linear porosity relationship that depends on temperature is used if there is no temperature material'
  issues = '#18079'
  design = 'porous_flow/porosity.md PorousFlowPorosityLinear.md'
[]


[linear_except3]
  type = RunException
  input = linear_except1.i
  cli_args = 'Materials/inactive=volstrain Materials/porosity/epv_coeff=1'
  expect_err = 'PorousFlowPorosityLinear: When epv_coeff is given you must have a volumetric-strain Material'
  match_literal = true
  threading = '!pthreads'
  requirement = 'PorousFlow shall produce an error if a linear porosity relationship that depends on volumetric strain is used if there is no volumetric-strain material'
  issues = '#18079'
  design = 'porous_flow/porosity.md PorousFlowPorosityLinear.md'
[]


[linear_test_vals1]
  type = CSVDiff
  input = linear_test_vals.i
  csvdiff = linear_test_vals_out.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate porosity as a linear function of effective porepressure, temperature and volumetric strain'
  issues = '#18079'
  design = 'porous_flow/porosity.md PorousFlowPorosityLinear.md'
[]


[linear_test_vals2]
  type = CSVDiff
  input = linear_test_vals.i
  prereq = linear_test_vals1
  cli_args = 'Materials/porosity/porosity_min=12 Outputs/file_base=linear_test_vals_min'
  csvdiff = linear_test_vals_min.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to calculate porosity as a linear function of effective porepressure, temperature and volumetric strain and place a lower bound on the resulting porosity'
  issues = '#18079'
  design = 'porous_flow/porosity.md PorousFlowPorosityLinear.md'
[]

[./pressure_pulse_1d]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d.i'
  csvdiff = 'pressure_pulse_1d.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#6845'
  design = 'porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D using 1 phase physics'
[../]


[./pressure_pulse_1d_action]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_action.i'
  prereq = pressure_pulse_1d
  csvdiff = 'pressure_pulse_1d.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#16841'
  design = 'PorousFlowFullySaturated.md porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D using 1 phase physics, and be able to employ the Action system in such settings'
[../]


[./pressure_pulse_1d_steady]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_steady.i'
  csvdiff = 'pressure_pulse_1d_steady.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#6845'
  design = 'porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall find the steady-state distribution resulting from a pressure pulse in 1D using 1 phase physics'
[../]


[./pressure_pulse_1d_steady_action]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_steady_action.i'
  prereq = pressure_pulse_1d_steady
  csvdiff = 'pressure_pulse_1d_steady.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#16841'
  design = 'PorousFlowFullySaturated.md porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall find the steady-state distribution resulting from a pressure pulse in 1D using 1 phase physics, and be able to employ the Action system in such settings'
[../]


[./pressure_pulse_1d_3comp]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_3comp.i'
  csvdiff = 'pressure_pulse_1d_3comp.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#6845'
  design = 'porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D using 1 fluid phase with multiple components'
[../]


[./pressure_pulse_1d_3comp_action]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_3comp_action.i'
  prereq = pressure_pulse_1d_3comp
  csvdiff = 'pressure_pulse_1d_3comp.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#16841'
  design = 'porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D using 1 fluid phase with multiple components, and be able to employ the Action system in such simulations'
[../]


[./pressure_pulse_1d_2phase]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_2phase.i'
  csvdiff = 'pressure_pulse_1d_2phase.csv'
  #skip = 'Must skip until YaqiHack (Issue #6774)'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#6845'
  design = 'porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 2 fluid phases, with 2 immiscible components, when one phase has zero saturation'
[../]


[./pressure_pulse_1d_2phasePS]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_2phasePS.i'
  csvdiff = 'pressure_pulse_1d_2phasePS_pp_0011.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#6845'
  design = 'porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 2 fluid phases, with 2 immiscible components, with constant capillary pressure'
[../]


[./pressure_pulse_1d_2phasePS_KT]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_2phasePS_KT.i'
  csvdiff = 'pressure_pulse_1d_2phasePS_KT_pp_0011.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#10426'
  design = 'porous_flow/numerical_diffusion.md porous_flow/kt_worked.md porous_flow/kt.md'
  requirement = 'PorousFlow shall implement Kuzmin-Turek stabilization for multi-phase, multi-component PorousFlow simulations, and illustrate this through the transient evolution of a pressure pulse'
[../]


[./pressure_pulse_1d_2phasePSVG]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_2phasePSVG.i'
  csvdiff = 'pressure_pulse_1d_2phasePSVG_pp_0011.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#6845'
  design = 'porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 2 fluid phases, with 2 immiscible components, with van-Genuchten capillary pressure'
[../]


[./pressure_pulse_1d_2phasePSVG2]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_2phasePSVG2.i'
  csvdiff = 'pressure_pulse_1d_2phasePSVG2_pp_0011.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#6845'
  design = 'porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 2 fluid phases, with 2 immiscible components, with van-Genuchten capillary pressure and a logarithmic extension'
[../]


[./pressure_pulse_1d_MD]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_MD.i'
  csvdiff = 'pressure_pulse_1d_MD.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#6845'
  design = 'porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 1 fluid phase in the MD formulation where the primary variable is log(mass-density)'
[../]


[./pressure_pulse_1d_fully_saturated]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_fully_saturated.i'
  csvdiff = 'pressure_pulse_1d_fully_saturated.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#6845'
  design = 'porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 1 fluid phase and employing the fully-saturated version of Darcy flow'
[../]


[./pressure_pulse_1d_3comp_fully_saturated]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_3comp_fully_saturated.i'
  csvdiff = 'pressure_pulse_1d_3comp_fully_saturated.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#6845'
  design = 'porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 1 fluid phase with 3 components and employing the fully-saturated version of Darcy flow'
[../]


[./pressure_pulse_1d_fully_saturated_2]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_fully_saturated_2.i'
  csvdiff = 'pressure_pulse_1d_fully_saturated_2.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#6845'
  design = 'porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall correctly simulate the transient evolution of a pressure pulse in 1D when using 1 fluid phase and employing the fully-saturated version of Darcy flow along with the fully-saturated version of the fluid-mass time derivative'
[../]


[./pressure_pulse_1d_adapt]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_adaptivity.i'
  csvdiff = 'pressure_pulse_1d_adaptivity_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#6845 #14035'
  design = 'porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall correctly simulate the transient evolution of a pressure pulse when mesh adaptivity is included'
[../]


[./pressure_pulse_1d_2comp_nodens_full]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_2comp_nodens.i'
  cli_args = 'PorousFlowFullySaturated/stabilization=Full Outputs/file_base=2comp_nodens_full_out'
  csvdiff = '2comp_nodens_full_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#16841'
  design = 'PorousFlowFullySaturated.md porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall be able to advect tracers in fully-saturated single-phase systems, using a fluid-volume conservation approach, and be able to use full-upwinding in such settings'
[../]


[./pressure_pulse_1d_2comp_nodens_none]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_2comp_nodens.i'
  cli_args = 'PorousFlowFullySaturated/stabilization=None Outputs/file_base=2comp_nodens_none_out'
  csvdiff = '2comp_nodens_none_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#16841'
  design = 'PorousFlowFullySaturated.md porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall be able to advect tracers in fully-saturated single-phase systems, using a fluid-volume conservation approach, and be able to use no upwinding in such settings'
[../]


[./pressure_pulse_1d_2comp_nodens_KT]
  type = 'CSVDiff'
  input = 'pressure_pulse_1d_2comp_nodens.i'
  cli_args = 'PorousFlowFullySaturated/stabilization=KT Outputs/file_base=2comp_nodens_KT_out'
  csvdiff = '2comp_nodens_KT_out.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  issues = '#16841'
  design = 'PorousFlowFullySaturated.md porous_flow/tests/pressure_pulse/pressure_pulse_tests.md'
  requirement = 'PorousFlow shall be able to advect tracers in fully-saturated single-phase systems, using a fluid-volume conservation approach, and be able to use KT stabilization in such settings'
[../]

[./theis_full]
  type = 'CSVDiff'
  input = 'theis.i'
  csvdiff = 'theis_out_line_0004.csv'
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to recover from a checkpoint save"
  issues = '#12927'
  design = 'porous_flow/restart.md'
[../]


[./theis_part1]
  type = 'CSVDiff'
  input = 'theis.i'
  csvdiff = 'theis_out_line_0002.csv'
  cli_args = '--half-transient Outputs/checkpoint=true'
  prereq = 'theis_full'
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to recover from a checkpoint save"
  issues = '#12927'
  design = 'porous_flow/restart.md'
[../]


[./theis_recover]
  type = 'CSVDiff'
  input = 'theis.i'
  csvdiff = 'theis_out_line_0004.csv'
  cli_args = '--recover'
  prereq = 'theis_part1'
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to recover from a checkpoint save"
  issues = '#12927'
  design = 'porous_flow/restart.md'
[../]


[./pffltvd_full]
  type = 'CSVDiff'
  input = 'pffltvd.i'
  csvdiff = 'pffltvd_out_tracer_0004.csv'
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to recover from a checkpoint save"
  issues = '#12927'
  design = 'porous_flow/restart.md'
[../]


[./pffltvd_part1]
  type = 'CSVDiff'
  input = 'pffltvd.i'
  csvdiff = 'pffltvd_out_tracer_0002.csv'
  cli_args = '--half-transient Outputs/checkpoint=true'
  prereq = 'pffltvd_full'
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to recover from a checkpoint save"
  issues = '#12927'
  design = 'porous_flow/restart.md'
[../]


[./pffltvd_recover]
  type = 'CSVDiff'
  input = 'pffltvd.i'
  csvdiff = 'pffltvd_out_tracer_0004.csv'
  cli_args = '--recover'
  prereq = 'pffltvd_part1'
  threading = '!pthreads'
  requirement = "PorousFlow shall be able to recover from a checkpoint save"
  issues = '#12927'
  design = 'porous_flow/restart.md'
[../]

[./s01]
  type = 'CSVDiff'
  input = 's01.i'
  csvdiff = 's01.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s02]
  type = 'CSVDiff'
  input = 's02.i'
  csvdiff = 's02.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow, when the source/sink strength is multiplied by the mobility'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s03]
  type = 'CSVDiff'
  input = 's03.i'
  csvdiff = 's03.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, unsaturated flow, when the source/sink strength is multiplied by the relative permeability'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s04]
  type = 'CSVDiff'
  input = 's04.i'
  csvdiff = 's04.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model source/sink boundary condition for single-phase, single-component flow, when the boundary flux is a piecewise-linear function of porepressure'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s05]
  type = 'CSVDiff'
  input = 's05.i'
  csvdiff = 's05.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model source/sink boundary condition for single-phase, single-component flow, when the boundary flux is a half-gaussian function of porepressure'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s06]
  type = 'CSVDiff'
  input = 's06.i'
  csvdiff = 's06.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model source/sink boundary condition for single-phase, single-component flow, when the boundary flux is a half-cubic function of porepressure'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s07]
  type = 'CSVDiff'
  input = 's07.i'
  csvdiff = 's07.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a source/sink boundary condition for single-phase, multi-component, fully-saturated flow'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s08]
  type = 'CSVDiff'
  input = 's08.i'
  csvdiff = 's08.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a source/sink boundary condition for multi-phase, multi-component flow'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s09]
  type = CSVDiff
  input = s09.i
  csvdiff = 's09_mf_0100.csv s09_mf_0050.csv s09_mf_0010.csv'
  abs_zero = 1E-7
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a source/sink boundary condition that holds porepressures fixed and extracts fluid components from boundaries at a rate prescribed by the flow within the model at the boundary - viz, the sink should behave like a free boundary'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s09_fully_saturated]
  type = CSVDiff
  input = s09_fully_saturated.i
  csvdiff = 's09_fully_saturated_mf_0100.csv s09_fully_saturated_mf_0050.csv s09_fully_saturated_mf_0010.csv'
  abs_zero = 1E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a source/sink boundary condition that holds porepressures fixed and extracts fluid components from boundaries at a rate prescribed by the flow within the model at the boundary - viz, the sink should behave like a free boundary, and this feature shall be compatible with the fully-saturated formalism within PorousFlow'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s10_left]
  type = Exodiff
  input = s10.i
  cli_args = 'BCs/flux/boundary=left Outputs/file_base=s10_left'
  exodiff = s10_left.e
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow, and the source/sink shall remove fluid from the correct node in a mesh: the left-side nodes in this case'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s10_right]
  type = Exodiff
  input = s10.i
  cli_args = 'BCs/flux/boundary=right Outputs/file_base=s10_right'
  exodiff = s10_right.e
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow, and the source/sink shall remove fluid from the correct node in a mesh: the right-side nodes in this case'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s10_top]
  type = Exodiff
  input = s10.i
  cli_args = 'BCs/flux/boundary=top Outputs/file_base=s10_top'
  exodiff = s10_top.e
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow, and the source/sink shall remove fluid from the correct node in a mesh: the top-side nodes in this case'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s10_bottom]
  type = Exodiff
  input = s10.i
  cli_args = 'BCs/flux/boundary=bottom Outputs/file_base=s10_bottom'
  exodiff = s10_bottom.e
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow, and the source/sink shall remove fluid from the correct node in a mesh: the bottom-side nodes in this case'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s10_front]
  type = Exodiff
  input = s10.i
  cli_args = 'BCs/flux/boundary=front Outputs/file_base=s10_front'
  exodiff = s10_front.e
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow, and the source/sink shall remove fluid from the correct node in a mesh: the front-side nodes in this case'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s10_back]
  type = Exodiff
  input = s10.i
  cli_args = 'BCs/flux/boundary=back Outputs/file_base=s10_back'
  exodiff = s10_back.e
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a source/sink boundary condition for single-phase, single-component, fully-saturated flow, and the source/sink shall remove fluid from the correct node in a mesh: the back-side nodes in this case'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./s11]
  type = Exodiff
  input = s11.i
  exodiff = s11.e
  threading = '!pthreads'
  cli_args = 'BCs/left_T/fluid_phase=0'
  requirement = 'PorousFlow shall be able to inject fluid at user specified temperature.'
  design = 'PorousFlowEnthalpySink.md'
  issues = '#15742'
[../]


[./s11_act]
  type = Exodiff
  input = s11_act.i
  exodiff = s11.e
  prereq = 's11'
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to setup fluid injection at user specified temperature using a simplified syntax.'
  issues = '#15742'
  design = 'PorousFlowEnthalpySink.md PorousFlowSinkBC.md'
[../]


[./s11_act_too_many_vars]
  type = RunException
  input = s11_act.i
  threading = '!pthreads'
  cli_args = 'Variables/pp1/initial_condition=3 Kernels/td_pp1/type=TimeDerivative Kernels/td_pp1/variable=pp1 UserObjects/dictator/porous_flow_vars="pp pp1 temp"'
  expect_err = "Number of porous flow variables in simulation is '3', but this BC can be used only with pressure and temperature."
  requirement = 'PorousFlow shall report an error when incorrect number of variables is used when using a simplified enthalpy sink BC syntax.'
  issues = '#15742'
  design = 'PorousFlowEnthalpySink.md PorousFlowSinkBC.md'
[../]


[./s11_act_too_many_pressure_vars]
  type = RunException
  input = s11_act.i
  threading = '!pthreads'
  cli_args = 'Variables/pp1/initial_condition=3 Kernels/td_pp1/type=TimeDerivative Kernels/td_pp1/variable=pp1 UserObjects/dictator/porous_flow_vars="pp temp" Modules/PorousFlow/BCs/left/porepressure_var="pp pp1"'
  expect_err = "'porepressure_var' parameter can currently take only a single value"
  requirement = 'PorousFlow shall report an error when more than 2 porepressure variables are specified when using a simplified BC syntax.'
  issues = '#15742'
  design = 'PorousFlowEnthalpySink.md PorousFlowSinkBC.md'
[../]


[./s11_overspecified_pressure]
  type = RunException
  input = s11.i
  threading = '!pthreads'
  cli_args = 'AuxVariables/press/initial_condition=3 BCs/left_T/porepressure_var=press BCs/left_T/fluid_phase=0'
  expect_err = "Cannot specify both pressure and pore pressure."
  requirement = 'PorousFlow shall report an error when both external and pore pressures are specified.'
  issues = '#15742'
  design = 'PorousFlowEnthalpySink.md PorousFlowSinkBC.md'
[../]


[./s11_underspecified_pressure]
  type = RunException
  input = s11.i
  threading = '!pthreads'
  expect_err = "You have to specify either 'pressure' or 'fluid_phase'."
  requirement = 'PorousFlow shall report an error when neither external and pore pressures are specified.'
  issues = '#15742'
  design = 'PorousFlowEnthalpySink.md PorousFlowSinkBC.md'
[../]


[./s11_incorrect_fluid_phase]
  type = RunException
  input = s11.i
  threading = '!pthreads'
  cli_args = "BCs/left_T/fluid_phase=2"
  expect_err = "Specified 'fluid_phase' is larger than the number of phases available in the simulation \(1\)."
  requirement = 'PorousFlow shall report an error when incorrect fluid phase is specified in a BC for injecting fluid at user specified temperature.'
  issues = '#15742'
  design = 'PorousFlowEnthalpySink.md PorousFlowSinkBC.md'
[../]


[./s12]
  type = CSVDiff
  input = s12.i
  csvdiff = s12.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to inject fluid at user specified pressure and temperature.'
  design = 'PorousFlowEnthalpySink.md'
  issues = '#15742'
[../]


[./injection_production_eg]
  type = 'CSVDiff'
  input = 'injection_production_eg.i'
  csvdiff = 'injection_production_eg_out_pps_0002.csv'
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a free boundary condition for multi-phase, multi-component fluids, and a clear example showing how this is possible shall be given'
  issues = '#7333'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./PorousFlowPiecewiseLinearSink_BC_eg1]
  type = 'CSVDiff'
  input = 'PorousFlowPiecewiseLinearSink_BC_eg1.i'
  csvdiff = 'PorousFlowPiecewiseLinearSink_BC_eg1_out.csv'
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a source/sink boundary condition, and a clear example showing how these boundary conditions can be used to fix porepressures shall be given'
  issues = '#12769'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md porous_flow/sinks.md'
[../]


[./outflow_except1]
  type = RunException
  input = outflow_except1.i
  threading = '!pthreads'
  expect_err = "The Dictator declares that the maximum fluid component index is 0, but you have set mass_fraction_component to 1. Remember that indexing starts at 0"
  match_literal = true
  requirement = 'PorousFlow shall report an error for an incorrect mass-fraction specification in PorousFlowOutflowBC'
  issues = '#18037'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md PorousFlowOutflowBC.md'
[../]


[./outflow_except2_dens]
  type = RunException
  input = outflow_except2.i
  cli_args = 'Materials/fluid_props/at_nodes=false'
  threading = '!pthreads'
  expect_err = "PorousFlowOutflowBC: You requested to multiply_by_density, but you have no nodal fluid density Material"
  match_literal = true
  requirement = 'PorousFlow shall report an error if there is no nodal density Material when using PorousFlowOutflowBC'
  issues = '#18037'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md PorousFlowOutflowBC.md'
[../]


[./outflow_except2_relperm]
  type = RunException
  input = outflow_except2.i
  cli_args = 'Materials/inactive=relperm'
  threading = '!pthreads'
  expect_err = "PorousFlowOutflowBC: You requested to include the relative permeability, but you have no nodal relative permeability Material"
  match_literal = true
  requirement = 'PorousFlow shall report an error if there is no nodal relative-permeability Material when using PorousFlowOutflowBC'
  issues = '#18037'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md PorousFlowOutflowBC.md'
[../]


[./outflow_except2_massfrac]
  type = RunException
  input = outflow_except2.i
  cli_args = 'Materials/inactive=massfrac'
  threading = '!pthreads'
  expect_err = "PorousFlowOutflowBC: For flux_type = fluid, you need a nodal mass-fraction Material"
  match_literal = true
  requirement = 'PorousFlow shall report an error if there is no nodal mass-fraction Material when using PorousFlowOutflowBC'
  issues = '#18037'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md PorousFlowOutflowBC.md'
[../]


[./outflow_except2_thermal_cond]
  type = RunException
  input = outflow_except2.i
  cli_args = 'BCs/outflow/flux_type=heat Materials/inactive=thermal_conductivity'
  threading = '!pthreads'
  expect_err = "PorousFlowOutflowBC: For flux_type = heat, you need a thermal conductivity Material"
  match_literal = true
  requirement = 'PorousFlow shall report an error if there is no thermal conductivity Material when using PorousFlowOutflowBC'
  issues = '#18037'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md PorousFlowOutflowBC.md'
[../]


[./outflow_except2_enthalpy]
  type = RunException
  input = outflow_except2.i
  cli_args = 'BCs/outflow/flux_type=heat Materials/fluid_props/compute_enthalpy=false'
  threading = '!pthreads'
  expect_err = "PorousFlowOutflowBC: For flux_type = heat, you need a nodal fluid enthalpy Material"
  match_literal = true
  requirement = 'PorousFlow shall report an error if there is no enthalpy Material when using PorousFlowOutflowBC'
  issues = '#18037'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md PorousFlowOutflowBC.md'
[../]


[./outflow_except2_T]
  type = RunException
  input = outflow_except2.i
  cli_args = 'BCs/outflow/flux_type=heat Materials/inactive=temperature'
  threading = '!pthreads'
  expect_err = "PorousFlowOutflowBC: For flux_type = heat, you need a temperature Material"
  match_literal = true
  requirement = 'PorousFlow shall report an error if there is no temperature Material when using PorousFlowOutflowBC'
  issues = '#18037'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md PorousFlowOutflowBC.md'
[../]


[./s13]
  type = CSVDiff
  input = s13.i
  csvdiff = 's13_csv_mf_0100.csv s13_csv_mf_0050.csv s13_csv_mf_0010.csv'
  abs_zero = 1E-7
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model an outflow boundary condition in single-phase, fully-saturated, multi-component cases'
  issues = '#18037'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md PorousFlowOutflowBC.md'
[../]


[./s14]
  type = CSVDiff
  input = s14.i
  csvdiff = s14_out.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model an outflow boundary condition in single-phase, fully-saturated, single-component case and record the total mass outflow'
  issues = '#18037'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md PorousFlowOutflowBC.md'
[../]


[./s15]
  type = CSVDiff
  input = s15.i
  csvdiff = s15_out.csv
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a heat-energy outflow boundary condition in single-phase, fully-saturated, single-component case and record the total heat-energy outflow'
  issues = '#18037'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md PorousFlowOutflowBC.md'
[../]


[./injection_production_eg_outflowBC]
  type = CSVDiff
  input = injection_production_eg_outflowBC.i
  csvdiff = injection_production_eg_outflowBC_out_pps_0002.csv
  rel_err = 1.0E-5
  threading = '!pthreads'
  requirement = 'PorousFlow shall be able to model a free, outflow boundary condition for multi-phase, multi-component fluids'
  issues = '#18037'
  design = 'porous_flow/tests/sinks/sinks_tests.md porous_flow/boundaries.md PorousFlowOutflowBC.md'
[../]

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