- mass_fluxThe postprocessor name holding the mass flux at this point in kg/s (positive is flux in, negative is flux out)
C++ Type:PostprocessorName
Unit:(no unit assumed)
Controllable:No
Description:The postprocessor name holding the mass flux at this point in kg/s (positive is flux in, negative is flux out)
- pointThe x,y,z coordinates of the point source (or sink)
C++ Type:libMesh::Point
Controllable:No
Description:The x,y,z coordinates of the point source (or sink)
- variableThe name of the variable that this residual object operates on
C++ Type:NonlinearVariableName
Unit:(no unit assumed)
Controllable:No
Description:The name of the variable that this residual object operates on
PorousFlowPointSourceFromPostprocessor
PorousFlowPointSourceFromPostprocessor implements a mass point source that adds (or removes) fluid at a mass flux rate that was computed by a postprocessor.
For instance:
[DiracKernels<<<{"href": "../../syntax/DiracKernels/index.html"}>>>]
[source]
type = PorousFlowPointSourceFromPostprocessor<<<{"description": "Point source (or sink) that adds (or removes) fluid at a mass flux rate specified by a postprocessor.", "href": "PorousFlowPointSourceFromPostprocessor.html"}>>>
variable<<<{"description": "The name of the variable that this residual object operates on"}>>> = pp
mass_flux<<<{"description": "The postprocessor name holding the mass flux at this point in kg/s (positive is flux in, negative is flux out)"}>>> = mass_flux_in
point<<<{"description": "The x,y,z coordinates of the point source (or sink)"}>>> = '0.5 0.5 0'
[]
[]Note that the execute_on parameter is set to timestep_begin so that the correct value is being used within the timestep.
[Postprocessors<<<{"href": "../../syntax/Postprocessors/index.html"}>>>]
[total_mass]
type = PorousFlowFluidMass<<<{"description": "Calculates the mass of a fluid component in a region", "href": "../postprocessors/PorousFlowFluidMass.html"}>>>
execute_on<<<{"description": "The list of flag(s) indicating when this object should be executed. For a description of each flag, see https://mooseframework.inl.gov/source/interfaces/SetupInterface.html."}>>> = 'initial timestep_end'
[]
[mass_flux_in]
type = FunctionValuePostprocessor<<<{"description": "Computes the value of a supplied function at a single point (scalable)", "href": "../postprocessors/FunctionValuePostprocessor.html"}>>>
function<<<{"description": "The function which supplies the postprocessor value."}>>> = mass_flux_fn
execute_on<<<{"description": "The list of flag(s) indicating when this object should be executed. For a description of each flag, see https://mooseframework.inl.gov/source/interfaces/SetupInterface.html."}>>> = 'initial timestep_begin'
[]
[]Input Parameters
- allow_moving_sourcesFalseIf true, allow Dirac sources to move, even if the mesh does not move, during the simulation.
Default:False
C++ Type:bool
Controllable:No
Description:If true, allow Dirac sources to move, even if the mesh does not move, during the simulation.
- blockThe list of blocks (ids or names) that this object will be applied
C++ Type:std::vector<SubdomainName>
Controllable:No
Description:The list of blocks (ids or names) that this object will be applied
- matrix_onlyFalseWhether this object is only doing assembly to matrices (no vectors)
Default:False
C++ Type:bool
Controllable:No
Description:Whether this object is only doing assembly to matrices (no vectors)
- point_not_found_behaviorIGNOREBy default (IGNORE), it is ignored if an added point cannot be located in the specified subdomains. If this option is set to ERROR, this situation will result in an error. If this option is set to WARNING, then a warning will be issued.
Default:IGNORE
C++ Type:MooseEnum
Options:ERROR, WARNING, IGNORE
Controllable:No
Description:By default (IGNORE), it is ignored if an added point cannot be located in the specified subdomains. If this option is set to ERROR, this situation will result in an error. If this option is set to WARNING, then a warning will be issued.
Optional Parameters
- absolute_value_vector_tagsThe tags for the vectors this residual object should fill with the absolute value of the residual contribution
C++ Type:std::vector<TagName>
Controllable:No
Description:The tags for the vectors this residual object should fill with the absolute value of the residual contribution
- extra_matrix_tagsThe extra tags for the matrices this Kernel should fill
C++ Type:std::vector<TagName>
Controllable:No
Description:The extra tags for the matrices this Kernel should fill
- extra_vector_tagsThe extra tags for the vectors this Kernel should fill
C++ Type:std::vector<TagName>
Controllable:No
Description:The extra tags for the vectors this Kernel should fill
- matrix_tagssystemThe tag for the matrices this Kernel should fill
Default:system
C++ Type:MultiMooseEnum
Options:nontime, system
Controllable:No
Description:The tag for the matrices this Kernel should fill
- vector_tagsnontimeThe tag for the vectors this Kernel should fill
Default:nontime
C++ Type:MultiMooseEnum
Options:nontime, time
Controllable:No
Description:The tag for the vectors this Kernel should fill
Contribution To Tagged Field Data Parameters
- control_tagsAdds user-defined labels for accessing object parameters via control logic.
C++ Type:std::vector<std::string>
Controllable:No
Description:Adds user-defined labels for accessing object parameters via control logic.
- drop_duplicate_pointsTrueBy default points added to a DiracKernel are dropped if a point at the same locationhas been added before. If this option is set to false duplicate points are retainedand contribute to residual and Jacobian.
Default:True
C++ Type:bool
Controllable:No
Description:By default points added to a DiracKernel are dropped if a point at the same locationhas been added before. If this option is set to false duplicate points are retainedand contribute to residual and Jacobian.
- enableTrueSet the enabled status of the MooseObject.
Default:True
C++ Type:bool
Controllable:Yes
Description:Set the enabled status of the MooseObject.
- implicitTrueDetermines whether this object is calculated using an implicit or explicit form
Default:True
C++ Type:bool
Controllable:No
Description:Determines whether this object is calculated using an implicit or explicit form
- search_methodnearest_node_connected_sidesChoice of search algorithm. All options begin by finding the nearest node in the primary boundary to a query point in the secondary boundary. In the default nearest_node_connected_sides algorithm, primary boundary elements are searched iff that nearest node is one of their nodes. This is fast to determine via a pregenerated node-to-elem map and is robust on conforming meshes. In the optional all_proximate_sides algorithm, primary boundary elements are searched iff they touch that nearest node, even if they are not topologically connected to it. This is more CPU-intensive but is necessary for robustness on any boundary surfaces which has disconnections (such as Flex IGA meshes) or non-conformity (such as hanging nodes in adaptively h-refined meshes).
Default:nearest_node_connected_sides
C++ Type:MooseEnum
Options:nearest_node_connected_sides, all_proximate_sides
Controllable:No
Description:Choice of search algorithm. All options begin by finding the nearest node in the primary boundary to a query point in the secondary boundary. In the default nearest_node_connected_sides algorithm, primary boundary elements are searched iff that nearest node is one of their nodes. This is fast to determine via a pregenerated node-to-elem map and is robust on conforming meshes. In the optional all_proximate_sides algorithm, primary boundary elements are searched iff they touch that nearest node, even if they are not topologically connected to it. This is more CPU-intensive but is necessary for robustness on any boundary surfaces which has disconnections (such as Flex IGA meshes) or non-conformity (such as hanging nodes in adaptively h-refined meshes).
- seed0The seed for the master random number generator
Default:0
C++ Type:unsigned int
Controllable:No
Description:The seed for the master random number generator
- use_displaced_meshFalseWhether or not this object should use the displaced mesh for computation. Note that in the case this is true but no displacements are provided in the Mesh block the undisplaced mesh will still be used.
Default:False
C++ Type:bool
Controllable:No
Description:Whether or not this object should use the displaced mesh for computation. Note that in the case this is true but no displacements are provided in the Mesh block the undisplaced mesh will still be used.
Advanced Parameters
- prop_getter_suffixAn optional suffix parameter that can be appended to any attempt to retrieve/get material properties. The suffix will be prepended with a '_' character.
C++ Type:MaterialPropertyName
Unit:(no unit assumed)
Controllable:No
Description:An optional suffix parameter that can be appended to any attempt to retrieve/get material properties. The suffix will be prepended with a '_' character.
- use_interpolated_stateFalseFor the old and older state use projected material properties interpolated at the quadrature points. To set up projection use the ProjectedStatefulMaterialStorageAction.
Default:False
C++ Type:bool
Controllable:No
Description:For the old and older state use projected material properties interpolated at the quadrature points. To set up projection use the ProjectedStatefulMaterialStorageAction.
Material Property Retrieval Parameters
Input Files
- (modules/combined/examples/geochem-porous_flow/forge/porous_flow.i)
- (modules/porous_flow/test/tests/hysteresis/2phasePS.i)
- (modules/porous_flow/examples/multiapp_fracture_flow/3dFracture/fracture_only_aperture_changing.i)
- (modules/porous_flow/test/tests/hysteresis/hys_order_09.i)
- (modules/porous_flow/test/tests/hysteresis/hys_order_06.i)
- (modules/porous_flow/test/tests/hysteresis/2phasePS_relperm.i)
- (modules/porous_flow/test/tests/hysteresis/1phase_3rd.i)
- (modules/porous_flow/test/tests/dirackernels/frompps.i)
- (modules/porous_flow/test/tests/hysteresis/2phasePS_relperm_2.i)
- (modules/porous_flow/test/tests/hysteresis/hys_order_03.i)
- (modules/porous_flow/test/tests/hysteresis/hys_order_04.i)
- (modules/porous_flow/test/tests/sinks/s14.i)
- (modules/porous_flow/test/tests/hysteresis/2phasePS_2.i)
- (modules/porous_flow/test/tests/energy_conservation/heat04_rz.i)
- (modules/porous_flow/test/tests/hysteresis/hys_order_07.i)
- (modules/porous_flow/test/tests/mass_conservation/mass11.i)
- (modules/porous_flow/test/tests/hysteresis/hys_order_01.i)
- (modules/porous_flow/test/tests/sinks/s15.i)
- (modules/porous_flow/test/tests/hysteresis/hys_order_02.i)
- (modules/porous_flow/test/tests/dirackernels/hfrompps.i)
- (modules/porous_flow/test/tests/hysteresis/hys_order_05.i)
- (modules/porous_flow/test/tests/hysteresis/hys_order_08.i)
- (modules/porous_flow/test/tests/hysteresis/1phase.i)
- (modules/porous_flow/test/tests/hysteresis/1phase_relperm.i)
- (modules/porous_flow/test/tests/hysteresis/2phasePP.i)
- (modules/porous_flow/test/tests/hysteresis/1phase_relperm_2.i)
- (modules/porous_flow/test/tests/hysteresis/2phasePP_2.i)
(modules/porous_flow/test/tests/dirackernels/frompps.i)
# Test PorousFlowPointSourceFromPostprocessor DiracKernel
[Mesh]
type = GeneratedMesh
dim = 2
bias_x = 1.1
bias_y = 1.1
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Functions]
[mass_flux_fn]
type = PiecewiseConstant
direction = left
xy_data = '
0 0
100 -0.1
300 0
600 -0.1
1400 0
1500 0.2
2000 0.2'
[]
[]
[Variables]
[pp]
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = pp
number_fluid_phases = 1
number_fluid_components = 1
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 1000
thermal_expansion = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseFullySaturated
porepressure = pp
[]
[massfrac]
type = PorousFlowMassFraction
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.2
[]
[]
[Postprocessors]
[total_mass]
type = PorousFlowFluidMass
execute_on = 'initial timestep_end'
[]
[mass_flux_in]
type = FunctionValuePostprocessor
function = mass_flux_fn
execute_on = 'initial timestep_begin'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
nl_abs_tol = 1e-14
dt = 100
end_time = 2000
[]
[Outputs]
perf_graph = true
csv = true
execute_on = 'initial timestep_end'
file_base = frompps
[]
[ICs]
[PressureIC]
variable = pp
type = ConstantIC
value = 20e6
[]
[]
[DiracKernels]
[source]
type = PorousFlowPointSourceFromPostprocessor
variable = pp
mass_flux = mass_flux_in
point = '0.5 0.5 0'
[]
[]
(modules/porous_flow/test/tests/dirackernels/frompps.i)
# Test PorousFlowPointSourceFromPostprocessor DiracKernel
[Mesh]
type = GeneratedMesh
dim = 2
bias_x = 1.1
bias_y = 1.1
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Functions]
[mass_flux_fn]
type = PiecewiseConstant
direction = left
xy_data = '
0 0
100 -0.1
300 0
600 -0.1
1400 0
1500 0.2
2000 0.2'
[]
[]
[Variables]
[pp]
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = pp
number_fluid_phases = 1
number_fluid_components = 1
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 1000
thermal_expansion = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseFullySaturated
porepressure = pp
[]
[massfrac]
type = PorousFlowMassFraction
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.2
[]
[]
[Postprocessors]
[total_mass]
type = PorousFlowFluidMass
execute_on = 'initial timestep_end'
[]
[mass_flux_in]
type = FunctionValuePostprocessor
function = mass_flux_fn
execute_on = 'initial timestep_begin'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
nl_abs_tol = 1e-14
dt = 100
end_time = 2000
[]
[Outputs]
perf_graph = true
csv = true
execute_on = 'initial timestep_end'
file_base = frompps
[]
[ICs]
[PressureIC]
variable = pp
type = ConstantIC
value = 20e6
[]
[]
[DiracKernels]
[source]
type = PorousFlowPointSourceFromPostprocessor
variable = pp
mass_flux = mass_flux_in
point = '0.5 0.5 0'
[]
[]
(modules/combined/examples/geochem-porous_flow/forge/porous_flow.i)
# Input file modified from RobPodgorney version
# - 2D instead of 3D with different resolution. Effectively this means a 1m height of RobPodgorney aquifer is simulated. RobPodgorney total mass flux is 2.5kg/s meaning 0.25kg/s is appropriate here
# - Celsius instead of Kelvin
# - no use of PorousFlowPointEnthalpySourceFromPostprocessor since that is not yet merged into MOOSE: a DirichletBC is used instead
# - Use of PorousFlowFullySaturated instead of PorousFlowUnsaturated, and the save_component_rate_in feature to record the change in kg of each species at each node for passing to the Geochem simulation
# - MultiApps and Transfers to transfer information between this simulation and the aquifer_geochemistry.i simulation
[Mesh]
[gen]
type = GeneratedMeshGenerator
dim = 2
nx = 225
ny = 200
xmin = -400
xmax = 500
ymin = -400
ymax = 400
[]
[injection_node]
input = gen
type = ExtraNodesetGenerator
new_boundary = injection_node
coord = '0 0 0'
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[f_H]
initial_condition = 8.201229858451E-07
[]
[f_Na]
initial_condition = 2.281094143525E-03
[]
[f_K]
initial_condition = 2.305489507836E-04
[]
[f_Ca]
initial_condition = 5.818776782059E-04
[]
[f_Mg]
initial_condition = 1.539513498238E-07
[]
[f_SiO2]
initial_condition = 2.691822196469E-04
[]
[f_Al]
initial_condition = 4.457519474122E-08
[]
[f_Cl]
initial_condition = 4.744309776594E-03
[]
[f_SO4]
initial_condition = 9.516650880811E-06
[]
[f_HCO3]
initial_condition = 5.906126982324E-05
[]
[porepressure]
initial_condition = 20E6
[]
[temperature]
initial_condition = 220 # degC
scaling = 1E-6 # fluid enthalpy is roughly 1E6
[]
[]
[BCs]
[source_temperature]
type = DirichletBC
boundary = injection_node
variable = temperature
value = 70 # degC
[]
[]
[DiracKernels]
[inject_H]
type = PorousFlowPointSourceFromPostprocessor
point = ' 0 0 0'
mass_flux = 4.790385871045E-08
variable = f_H
[]
[inject_Na]
type = PorousFlowPointSourceFromPostprocessor
point = ' 0 0 0'
mass_flux = 7.586252963780E-07
variable = f_Na
[]
[inject_K]
type = PorousFlowPointSourceFromPostprocessor
point = ' 0 0 0'
mass_flux = 2.746517625125E-07
variable = f_K
[]
[inject_Ca]
type = PorousFlowPointSourceFromPostprocessor
point = ' 0 0 0'
mass_flux = 7.775129478597E-07
variable = f_Ca
[]
[inject_Mg]
type = PorousFlowPointSourceFromPostprocessor
point = ' 0 0 0'
mass_flux = 1.749872109005E-07
variable = f_Mg
[]
[inject_SiO2]
type = PorousFlowPointSourceFromPostprocessor
point = ' 0 0 0'
mass_flux = 4.100547515915E-06
variable = f_SiO2
[]
[inject_Al]
type = PorousFlowPointSourceFromPostprocessor
point = ' 0 0 0'
mass_flux = 2.502408592080E-08
variable = f_Al
[]
[inject_Cl]
type = PorousFlowPointSourceFromPostprocessor
point = ' 0 0 0'
mass_flux = 1.997260386272E-06
variable = f_Cl
[]
[inject_SO4]
type = PorousFlowPointSourceFromPostprocessor
point = ' 0 0 0'
mass_flux = 2.497372164191E-07
variable = f_SO4
[]
[inject_HCO3]
type = PorousFlowPointSourceFromPostprocessor
point = ' 0 0 0'
mass_flux = 5.003150992902E-06
variable = f_HCO3
[]
[inject_H2O]
type = PorousFlowPointSourceFromPostprocessor
point = ' 0 0 0'
mass_flux = 2.499865905987E-01
variable = porepressure
[]
[produce_H]
type = PorousFlowPeacemanBorehole
variable = f_H
SumQuantityUO = produced_mass_H
mass_fraction_component = 0
point_file = production.bh
line_length = 1
bottom_p_or_t = 20E6
unit_weight = '0 0 0'
use_mobility = true
character = 1
[]
[produce_Na]
type = PorousFlowPeacemanBorehole
variable = f_Na
SumQuantityUO = produced_mass_Na
mass_fraction_component = 1
point_file = production.bh
line_length = 1
bottom_p_or_t = 20E6
unit_weight = '0 0 0'
use_mobility = true
character = 1
[]
[produce_K]
type = PorousFlowPeacemanBorehole
variable = f_K
SumQuantityUO = produced_mass_K
mass_fraction_component = 2
point_file = production.bh
line_length = 1
bottom_p_or_t = 20E6
unit_weight = '0 0 0'
use_mobility = true
character = 1
[]
[produce_Ca]
type = PorousFlowPeacemanBorehole
variable = f_Ca
SumQuantityUO = produced_mass_Ca
mass_fraction_component = 3
point_file = production.bh
line_length = 1
bottom_p_or_t = 20E6
unit_weight = '0 0 0'
use_mobility = true
character = 1
[]
[produce_Mg]
type = PorousFlowPeacemanBorehole
variable = f_Mg
SumQuantityUO = produced_mass_Mg
mass_fraction_component = 4
point_file = production.bh
line_length = 1
bottom_p_or_t = 20E6
unit_weight = '0 0 0'
use_mobility = true
character = 1
[]
[produce_SiO2]
type = PorousFlowPeacemanBorehole
variable = f_SiO2
SumQuantityUO = produced_mass_SiO2
mass_fraction_component = 5
point_file = production.bh
line_length = 1
bottom_p_or_t = 20E6
unit_weight = '0 0 0'
use_mobility = true
character = 1
[]
[produce_Al]
type = PorousFlowPeacemanBorehole
variable = f_Al
SumQuantityUO = produced_mass_Al
mass_fraction_component = 6
point_file = production.bh
line_length = 1
bottom_p_or_t = 20E6
unit_weight = '0 0 0'
use_mobility = true
character = 1
[]
[produce_Cl]
type = PorousFlowPeacemanBorehole
variable = f_Cl
SumQuantityUO = produced_mass_Cl
mass_fraction_component = 7
point_file = production.bh
line_length = 1
bottom_p_or_t = 20E6
unit_weight = '0 0 0'
use_mobility = true
character = 1
[]
[produce_SO4]
type = PorousFlowPeacemanBorehole
variable = f_SO4
SumQuantityUO = produced_mass_SO4
mass_fraction_component = 8
point_file = production.bh
line_length = 1
bottom_p_or_t = 20E6
unit_weight = '0 0 0'
use_mobility = true
character = 1
[]
[produce_HCO3]
type = PorousFlowPeacemanBorehole
variable = f_HCO3
SumQuantityUO = produced_mass_HCO3
mass_fraction_component = 9
point_file = production.bh
line_length = 1
bottom_p_or_t = 20E6
unit_weight = '0 0 0'
use_mobility = true
character = 1
[]
[produce_H2O]
type = PorousFlowPeacemanBorehole
variable = porepressure
SumQuantityUO = produced_mass_H2O
mass_fraction_component = 10
point_file = production.bh
line_length = 1
bottom_p_or_t = 20E6
unit_weight = '0 0 0'
use_mobility = true
character = 1
[]
[remove_heat_at_production_well]
type = PorousFlowPeacemanBorehole
variable = temperature
SumQuantityUO = produced_heat
point_file = production.bh
line_length = 1
bottom_p_or_t = 20E6
unit_weight = '0 0 0'
use_mobility = true
use_enthalpy = true
character = 1
[]
[]
[UserObjects]
[produced_mass_H]
type = PorousFlowSumQuantity
[]
[produced_mass_Na]
type = PorousFlowSumQuantity
[]
[produced_mass_K]
type = PorousFlowSumQuantity
[]
[produced_mass_Ca]
type = PorousFlowSumQuantity
[]
[produced_mass_Mg]
type = PorousFlowSumQuantity
[]
[produced_mass_SiO2]
type = PorousFlowSumQuantity
[]
[produced_mass_Al]
type = PorousFlowSumQuantity
[]
[produced_mass_Cl]
type = PorousFlowSumQuantity
[]
[produced_mass_SO4]
type = PorousFlowSumQuantity
[]
[produced_mass_HCO3]
type = PorousFlowSumQuantity
[]
[produced_mass_H2O]
type = PorousFlowSumQuantity
[]
[produced_heat]
type = PorousFlowSumQuantity
[]
[]
[Postprocessors]
[heat_extracted]
type = PorousFlowPlotQuantity
uo = produced_heat
[]
[approx_production_temperature]
type = PointValue
point = '100 0 0'
variable = temperature
[]
[mass_extracted_H]
type = PorousFlowPlotQuantity
uo = produced_mass_H
execute_on = 'initial timestep_end'
[]
[mass_extracted_Na]
type = PorousFlowPlotQuantity
uo = produced_mass_Na
execute_on = 'initial timestep_end'
[]
[mass_extracted_K]
type = PorousFlowPlotQuantity
uo = produced_mass_K
execute_on = 'initial timestep_end'
[]
[mass_extracted_Ca]
type = PorousFlowPlotQuantity
uo = produced_mass_Ca
execute_on = 'initial timestep_end'
[]
[mass_extracted_Mg]
type = PorousFlowPlotQuantity
uo = produced_mass_Mg
execute_on = 'initial timestep_end'
[]
[mass_extracted_SiO2]
type = PorousFlowPlotQuantity
uo = produced_mass_SiO2
execute_on = 'initial timestep_end'
[]
[mass_extracted_Al]
type = PorousFlowPlotQuantity
uo = produced_mass_Al
execute_on = 'initial timestep_end'
[]
[mass_extracted_Cl]
type = PorousFlowPlotQuantity
uo = produced_mass_Cl
execute_on = 'initial timestep_end'
[]
[mass_extracted_SO4]
type = PorousFlowPlotQuantity
uo = produced_mass_SO4
execute_on = 'initial timestep_end'
[]
[mass_extracted_HCO3]
type = PorousFlowPlotQuantity
uo = produced_mass_HCO3
execute_on = 'initial timestep_end'
[]
[mass_extracted_H2O]
type = PorousFlowPlotQuantity
uo = produced_mass_H2O
execute_on = 'initial timestep_end'
[]
[mass_extracted]
type = LinearCombinationPostprocessor
pp_names = 'mass_extracted_H mass_extracted_Na mass_extracted_K mass_extracted_Ca mass_extracted_Mg mass_extracted_SiO2 mass_extracted_Al mass_extracted_Cl mass_extracted_SO4 mass_extracted_HCO3 mass_extracted_H2O'
pp_coefs = '1 1 1 1 1 1 1 1 1 1 1'
execute_on = 'initial timestep_end'
[]
[dt]
type = TimestepSize
execute_on = 'timestep_begin'
[]
[]
[FluidProperties]
[the_simple_fluid]
type = SimpleFluidProperties
thermal_expansion = 2E-4
bulk_modulus = 2E9
viscosity = 1E-3
density0 = 980
cv = 4000.0
cp = 4000.0
porepressure_coefficient = 0
[]
[]
[PorousFlowFullySaturated]
coupling_type = ThermoHydro
porepressure = porepressure
temperature = temperature
mass_fraction_vars = 'f_H f_Na f_K f_Ca f_Mg f_SiO2 f_Al f_Cl f_SO4 f_HCO3'
save_component_rate_in = 'rate_H rate_Na rate_K rate_Ca rate_Mg rate_SiO2 rate_Al rate_Cl rate_SO4 rate_HCO3 rate_H2O' # change in kg at every node / dt
fp = the_simple_fluid
temperature_unit = Celsius
[]
[AuxVariables]
[rate_H]
[]
[rate_Na]
[]
[rate_K]
[]
[rate_Ca]
[]
[rate_Mg]
[]
[rate_SiO2]
[]
[rate_Al]
[]
[rate_Cl]
[]
[rate_SO4]
[]
[rate_HCO3]
[]
[rate_H2O]
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.01
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1E-14 0 0 0 1E-14 0 0 0 1E-14'
[]
[thermal_conductivity]
type = PorousFlowThermalConductivityIdeal
dry_thermal_conductivity = '2.5 0 0 0 2.5 0 0 0 2.5'
[]
[rock_heat]
type = PorousFlowMatrixInternalEnergy
density = 2750.0
specific_heat_capacity = 900.0
[]
[]
[Preconditioning]
active = typically_efficient
[typically_efficient]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_hypre_type'
petsc_options_value = ' hypre boomeramg'
[]
[strong]
type = SMP
full = true
petsc_options = '-ksp_diagonal_scale -ksp_diagonal_scale_fix'
petsc_options_iname = '-pc_type -sub_pc_type -sub_pc_factor_shift_type -pc_asm_overlap'
petsc_options_value = ' asm ilu NONZERO 2'
[]
[probably_too_strong]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_mat_solver_package'
petsc_options_value = ' lu mumps'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
end_time = 31536000 #1 year
[TimeStepper]
type = SolutionTimeAdaptiveDT
dt = 500
[]
[]
[Outputs]
exodus = true
csv = true
[]
[MultiApps]
[react]
type = TransientMultiApp
input_files = aquifer_geochemistry.i
clone_master_mesh = true
execute_on = 'timestep_end'
[]
[]
[Transfers]
[changes_due_to_flow]
type = MultiAppCopyTransfer
source_variable = 'rate_H rate_Na rate_K rate_Ca rate_Mg rate_SiO2 rate_Al rate_Cl rate_SO4 rate_HCO3 rate_H2O temperature'
variable = 'pf_rate_H pf_rate_Na pf_rate_K pf_rate_Ca pf_rate_Mg pf_rate_SiO2 pf_rate_Al pf_rate_Cl pf_rate_SO4 pf_rate_HCO3 pf_rate_H2O temperature'
to_multi_app = react
[]
[massfrac_from_geochem]
type = MultiAppCopyTransfer
source_variable = 'massfrac_H massfrac_Na massfrac_K massfrac_Ca massfrac_Mg massfrac_SiO2 massfrac_Al massfrac_Cl massfrac_SO4 massfrac_HCO3'
variable = 'f_H f_Na f_K f_Ca f_Mg f_SiO2 f_Al f_Cl f_SO4 f_HCO3'
from_multi_app = react
[]
[]
(modules/porous_flow/test/tests/hysteresis/2phasePS.i)
# Simple example of a 2-phase situation with hysteretic capillary pressure. Gas is added to and removed from the system in order to observe the hysteresis
# All liquid water exists in component 0
# All gas exists in component 1
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
number_fluid_phases = 2
number_fluid_components = 2
porous_flow_vars = 'pp0 sat1'
[]
[]
[Variables]
[pp0]
[]
[sat1]
initial_condition = 0
[]
[]
[Kernels]
[mass_conservation0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pp0
[]
[mass_conservation1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = sat1
[]
[]
[DiracKernels]
[pump]
type = PorousFlowPointSourceFromPostprocessor
mass_flux = flux
point = '0.5 0 0'
variable = sat1
[]
[]
[AuxVariables]
[massfrac_ph0_sp0]
initial_condition = 1
[]
[massfrac_ph1_sp0]
initial_condition = 0
[]
[sat0]
family = MONOMIAL
order = CONSTANT
[]
[pp1]
family = MONOMIAL
order = CONSTANT
[]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[sat0]
type = PorousFlowPropertyAux
variable = sat0
phase = 0
property = saturation
[]
[pp1]
type = PorousFlowPropertyAux
variable = pp1
phase = 1
property = pressure
[]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[]
[FluidProperties]
[simple_fluid] # same properties used for both phases
type = SimpleFluidProperties
bulk_modulus = 10 # so pumping does not result in excessive porepressure
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[temperature]
type = PorousFlowTemperature
temperature = 20
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 1
[]
[hys_order_material]
type = PorousFlowHysteresisOrder
[]
[pc_calculator]
type = PorousFlow2PhaseHysPS
alpha_d = 10.0
alpha_w = 7.0
n_d = 1.5
n_w = 1.9
S_l_min = 0.1
S_lr = 0.2
S_gr_max = 0.3
Pc_max = 12.0
high_ratio = 0.9
low_extension_type = quadratic
high_extension_type = power
phase0_porepressure = pp0
phase1_saturation = sat1
[]
[]
[Postprocessors]
[flux]
type = FunctionValuePostprocessor
function = 'if(t <= 9, 10, -10)'
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[sat0]
type = PointValue
point = '0 0 0'
variable = sat0
[]
[sat1]
type = PointValue
point = '0 0 0'
variable = sat1
[]
[pp0]
type = PointValue
point = '0 0 0'
variable = pp0
[]
[pp1]
type = PointValue
point = '0 0 0'
variable = pp1
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_shift_type'
petsc_options_value = ' lu NONZERO'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 0.5
end_time = 18
nl_abs_tol = 1E-10
[]
[Outputs]
csv = true
[]
(modules/porous_flow/examples/multiapp_fracture_flow/3dFracture/fracture_only_aperture_changing.i)
# Cold water injection into one side of the fracture network, and production from the other side
injection_rate = 10 # kg/s
[Mesh]
uniform_refine = 0
[cluster34]
type = FileMeshGenerator
file = 'Cluster_34.exo'
[]
[injection_node]
type = BoundingBoxNodeSetGenerator
input = cluster34
bottom_left = '-1000 0 -1000'
top_right = '1000 0.504 1000'
new_boundary = injection_node
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 -9.81E-6' # Note the value, because of pressure_unit
[]
[Variables]
[frac_P]
scaling = 1E6
[]
[frac_T]
initial_condition = 473
[]
[]
[ICs]
[frac_P]
type = FunctionIC
variable = frac_P
function = insitu_pp
[]
[]
[PorousFlowFullySaturated]
coupling_type = ThermoHydro
porepressure = frac_P
temperature = frac_T
fp = water
pressure_unit = MPa
[]
[Kernels]
[toMatrix]
type = PorousFlowHeatMassTransfer
variable = frac_T
v = transferred_matrix_T
transfer_coefficient = heat_transfer_coefficient
save_in = joules_per_s
[]
[]
[AuxVariables]
[heat_transfer_coefficient]
family = MONOMIAL
order = CONSTANT
initial_condition = 0.0
[]
[transferred_matrix_T]
initial_condition = 473
[]
[joules_per_s]
[]
[normal_dirn_x]
family = MONOMIAL
order = CONSTANT
[]
[normal_dirn_y]
family = MONOMIAL
order = CONSTANT
[]
[normal_dirn_z]
family = MONOMIAL
order = CONSTANT
[]
[enclosing_element_normal_length]
family = MONOMIAL
order = CONSTANT
[]
[enclosing_element_normal_thermal_cond]
family = MONOMIAL
order = CONSTANT
[]
[aperture]
family = MONOMIAL
order = CONSTANT
[]
[perm_times_app]
family = MONOMIAL
order = CONSTANT
[]
[density]
family = MONOMIAL
order = CONSTANT
[]
[viscosity]
family = MONOMIAL
order = CONSTANT
[]
[insitu_pp]
[]
[]
[AuxKernels]
[normal_dirn_x_auxk]
type = PorousFlowElementNormal
variable = normal_dirn_x
component = x
[]
[normal_dirn_y]
type = PorousFlowElementNormal
variable = normal_dirn_y
component = y
[]
[normal_dirn_z]
type = PorousFlowElementNormal
variable = normal_dirn_z
component = z
[]
[heat_transfer_coefficient_auxk]
type = ParsedAux
variable = heat_transfer_coefficient
coupled_variables = 'enclosing_element_normal_length enclosing_element_normal_thermal_cond'
constant_names = h_s
constant_expressions = 1E3 # should be much bigger than thermal_conductivity / L ~ 1
expression = 'if(enclosing_element_normal_length = 0, 0, h_s * enclosing_element_normal_thermal_cond * 2 * enclosing_element_normal_length / (h_s * enclosing_element_normal_length * enclosing_element_normal_length + enclosing_element_normal_thermal_cond * 2 * enclosing_element_normal_length))'
[]
[aperture]
type = PorousFlowPropertyAux
variable = aperture
property = porosity
[]
[perm_times_app]
type = PorousFlowPropertyAux
variable = perm_times_app
property = permeability
row = 0
column = 0
[]
[density]
type = PorousFlowPropertyAux
variable = density
property = density
phase = 0
[]
[viscosity]
type = PorousFlowPropertyAux
variable = viscosity
property = viscosity
phase = 0
[]
[insitu_pp]
type = FunctionAux
execute_on = initial
variable = insitu_pp
function = insitu_pp
[]
[]
[BCs]
[inject_heat]
type = DirichletBC
boundary = injection_node
variable = frac_T
value = 373
[]
[]
[DiracKernels]
[inject_fluid]
type = PorousFlowPointSourceFromPostprocessor
mass_flux = ${injection_rate}
point = '58.8124 0.50384 74.7838'
variable = frac_P
[]
[withdraw_fluid]
type = PorousFlowPeacemanBorehole
SumQuantityUO = kg_out_uo
bottom_p_or_t = 10.6 # 1MPa + approx insitu at production point, to prevent aperture closing due to low porepressures
character = 1
line_length = 1
point_file = production.xyz
unit_weight = '0 0 0'
fluid_phase = 0
use_mobility = true
variable = frac_P
[]
[withdraw_heat]
type = PorousFlowPeacemanBorehole
SumQuantityUO = J_out_uo
bottom_p_or_t = 10.6 # 1MPa + approx insitu at production point, to prevent aperture closing due to low porepressures
character = 1
line_length = 1
point_file = production.xyz
unit_weight = '0 0 0'
fluid_phase = 0
use_mobility = true
use_enthalpy = true
variable = frac_T
[]
[]
[UserObjects]
[kg_out_uo]
type = PorousFlowSumQuantity
[]
[J_out_uo]
type = PorousFlowSumQuantity
[]
[]
[FluidProperties]
[true_water]
type = Water97FluidProperties
[]
[water]
type = TabulatedBicubicFluidProperties
fp = true_water
temperature_min = 275 # K
temperature_max = 600
interpolated_properties = 'density viscosity enthalpy internal_energy'
fluid_property_output_file = water97_tabulated.csv
# Comment out the fp parameter and uncomment below to use the newly generated tabulation
# fluid_property_file = water97_tabulated.csv
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityLinear
porosity_ref = 1E-4 # fracture porosity = 1.0, but must include fracture aperture of 1E-4 at P = insitu_pp
P_ref = insitu_pp
P_coeff = 1E-3 # this is in metres/MPa, ie for P_ref = 1/P_coeff, the aperture becomes 1 metre
porosity_min = 1E-5
[]
[permeability]
type = PorousFlowPermeabilityKozenyCarman
k0 = 1E-15 # fracture perm = 1E-11 m^2, but must include fracture aperture of 1E-4
poroperm_function = kozeny_carman_phi0
m = 0
n = 3
phi0 = 1E-4
[]
[internal_energy]
type = PorousFlowMatrixInternalEnergy
density = 2700 # kg/m^3
specific_heat_capacity = 0 # basically no rock inside the fracture
[]
[aq_thermal_conductivity]
type = PorousFlowThermalConductivityIdeal
dry_thermal_conductivity = '0.6E-4 0 0 0 0.6E-4 0 0 0 0.6E-4' # thermal conductivity of water times fracture aperture. This should increase linearly with aperture, but is set constant in this model
[]
[]
[Functions]
[kg_rate]
type = ParsedFunction
symbol_values = 'dt kg_out'
symbol_names = 'dt kg_out'
expression = 'kg_out/dt'
[]
[insitu_pp]
type = ParsedFunction
expression = '10 - 0.847E-2 * z' # Approximate hydrostatic in MPa
[]
[]
[Postprocessors]
[dt]
type = TimestepSize
outputs = 'none'
[]
[kg_out]
type = PorousFlowPlotQuantity
uo = kg_out_uo
[]
[kg_per_s]
type = FunctionValuePostprocessor
function = kg_rate
[]
[J_out]
type = PorousFlowPlotQuantity
uo = J_out_uo
[]
[TK_out]
type = PointValue
variable = frac_T
point = '101.705 160.459 39.5722'
[]
[P_out]
type = PointValue
variable = frac_P
point = '101.705 160.459 39.5722'
[]
[P_in]
type = PointValue
variable = frac_P
point = '58.8124 0.50384 74.7838'
[]
[]
[VectorPostprocessors]
[heat_transfer_rate]
type = NodalValueSampler
outputs = none
sort_by = id
variable = joules_per_s
[]
[]
[Preconditioning]
[entire_jacobian]
type = SMP
full = true
petsc_options_iname = '-pc_type -sub_pc_type -sub_pc_factor_shift_type -pc_asm_overlap'
petsc_options_value = ' asm lu NONZERO 2 '
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
[TimeStepper]
type = IterationAdaptiveDT
dt = 1
optimal_iterations = 10
growth_factor = 1.5
[]
dtmax = 1E8
end_time = 1E8
nl_abs_tol = 1E-3
nl_max_its = 20
[]
[Outputs]
print_linear_residuals = false
csv = true
[ex]
type = Exodus
sync_times = '1 10 100 200 300 400 500 600 700 800 900 1000 1100 1200 1300 1400 1500 1600 1700 1800 1900 2000 2100 2200 2300 2400 2500 2600 2700 2800 2900 3000 3100 3200 3300 3400 3500 3600 3700 3800 3900 4000 4100 4200 4300 4400 4500 4600 4700 4800 4900 5000 5100 5200 5300 5400 5500 5600 5700 5800 5900 6000 6100 6200 6300 6400 6500 6600 6700 6800 6900 7000 7100 7200 7300 7400 7500 7600 7700 7800 7900 8000 8100 8200 8300 8400 8500 8600 8700 8800 8900 9000 10000 11000 12000 13000 14000 15000 16000 17000 18000 19000 20000 30000 50000 70000 100000 200000 300000 400000 500000 600000 700000 800000 900000 1000000 1100000 1200000 1300000 1400000 1500000 1600000 1700000 1800000 1900000 2000000 2100000 2200000 2300000 2400000 2500000 2600000 2700000 2800000 2900000'
sync_only = true
[]
[]
(modules/porous_flow/test/tests/hysteresis/hys_order_09.i)
# Test that PorousFlowHysteresisOrder correctly calculates hysteresis order
# Hysteresis order is initialised = 3, with turning points = (0.5, 0.8, 0.66)
# Initial saturation is 0.71
# A large amount of water is removed in one timestep so the saturation becomes 0.58 (and order = 0)
# Then, water is added to the system (order = 1, with turning point = 0.58) until saturation = 0.67
# Then, water is removed from the system so order becomes 2 with turning point = 0.67
# Then, water is removed from the system until saturation < 0.58 and order = 0
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pp]
initial_condition = -9E5
[]
[]
[PorousFlowUnsaturated]
porepressure = pp
fp = simple_fluid
[]
[DiracKernels]
[source_sink_0]
type = PorousFlowPointSourceFromPostprocessor
point = '0 0 0'
mass_flux = sink_strength
variable = pp
[]
[source_sink_1]
type = PorousFlowPointSourceFromPostprocessor
point = '1 0 0'
mass_flux = sink_strength
variable = pp
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 1.0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '0 0 0 0 0 0 0 0 0'
[]
[hys_order]
type = PorousFlowHysteresisOrder
initial_order = 3
previous_turning_points = '0.6 0.8 0.66'
[]
[]
[AuxVariables]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[tp0]
family = MONOMIAL
order = CONSTANT
[]
[tp1]
family = MONOMIAL
order = CONSTANT
[]
[tp2]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[tp0]
type = PorousFlowPropertyAux
variable = tp0
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 0
[]
[tp1]
type = PorousFlowPropertyAux
variable = tp1
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 1
[]
[tp2]
type = PorousFlowPropertyAux
variable = tp2
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 2
[]
[]
[Functions]
[sink_strength_fcn]
type = ParsedFunction
expression = '30 * if(t <= 1, -2, if(t <= 2, 1.5, -1))'
[]
[]
[Postprocessors]
[sink_strength]
type = FunctionValuePostprocessor
function = sink_strength_fcn
outputs = 'none'
[]
[saturation]
type = PointValue
point = '0 0 0'
variable = saturation0
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[tp0]
type = PointValue
point = '0 0 0'
variable = tp0
[]
[tp1]
type = PointValue
point = '0 0 0'
variable = tp1
[]
[tp2]
type = PointValue
point = '0 0 0'
variable = tp2
[]
[]
[Preconditioning]
[basic]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 6
nl_abs_tol = 1E-7
[]
[Outputs]
[csv]
type = CSV
[]
[]
(modules/porous_flow/test/tests/hysteresis/hys_order_06.i)
# Test that PorousFlowHysteresisOrder correctly calculates hysteresis order
# Hysteresis order is initialised = 2, with turning points = (0.6, 0.8)
# Initial saturation is 0.71
# Water is added to the system, so order = 3 with turning point = 0.71
# Then water is added to the system until saturation = 0.8, when order = 1
# Then water is added to the system until saturation = 1.0, when order becomes zero
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pp]
initial_condition = -9E5
[]
[]
[PorousFlowUnsaturated]
porepressure = pp
fp = simple_fluid
[]
[DiracKernels]
[source_sink_0]
type = PorousFlowPointSourceFromPostprocessor
point = '0 0 0'
mass_flux = sink_strength
variable = pp
[]
[source_sink_1]
type = PorousFlowPointSourceFromPostprocessor
point = '1 0 0'
mass_flux = sink_strength
variable = pp
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 1.0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '0 0 0 0 0 0 0 0 0'
[]
[hys_order]
type = PorousFlowHysteresisOrder
initial_order = 2
previous_turning_points = '0.6 0.8'
[]
[]
[AuxVariables]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[tp0]
family = MONOMIAL
order = CONSTANT
[]
[tp1]
family = MONOMIAL
order = CONSTANT
[]
[tp2]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[tp0]
type = PorousFlowPropertyAux
variable = tp0
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 0
[]
[tp1]
type = PorousFlowPropertyAux
variable = tp1
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 1
[]
[tp2]
type = PorousFlowPropertyAux
variable = tp2
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 2
[]
[]
[Functions]
[sink_strength_fcn]
type = ParsedFunction
expression = '30'
[]
[]
[Postprocessors]
[sink_strength]
type = FunctionValuePostprocessor
function = sink_strength_fcn
outputs = 'none'
[]
[saturation]
type = PointValue
point = '0 0 0'
variable = saturation0
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[tp0]
type = PointValue
point = '0 0 0'
variable = tp0
[]
[tp1]
type = PointValue
point = '0 0 0'
variable = tp1
[]
[tp2]
type = PointValue
point = '0 0 0'
variable = tp2
[]
[]
[Preconditioning]
[basic]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 7
nl_abs_tol = 1E-7
[]
[Outputs]
[csv]
type = CSV
[]
[]
(modules/porous_flow/test/tests/hysteresis/2phasePS_relperm.i)
# Simple example of a 2-phase situation with hysteretic relative permeability. Gas is added to and removed from the system in order to observe the hysteresis
# All liquid water exists in component 0
# All gas exists in component 1
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
number_fluid_phases = 2
number_fluid_components = 2
porous_flow_vars = 'pp0 sat1'
[]
[pc]
type = PorousFlowCapillaryPressureVG
alpha = 10.0
m = 0.33
[]
[]
[Variables]
[pp0]
[]
[sat1]
initial_condition = 0
[]
[]
[Kernels]
[mass_conservation0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pp0
[]
[mass_conservation1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = sat1
[]
[]
[DiracKernels]
[pump]
type = PorousFlowPointSourceFromPostprocessor
mass_flux = flux
point = '0.5 0 0'
variable = sat1
[]
[]
[AuxVariables]
[massfrac_ph0_sp0]
initial_condition = 1
[]
[massfrac_ph1_sp0]
initial_condition = 0
[]
[sat0]
family = MONOMIAL
order = CONSTANT
[]
[pp1]
family = MONOMIAL
order = CONSTANT
[]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[relperm_liquid]
family = MONOMIAL
order = CONSTANT
[]
[relperm_gas]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[sat0]
type = PorousFlowPropertyAux
variable = sat0
phase = 0
property = saturation
[]
[relperm_liquid]
type = PorousFlowPropertyAux
variable = relperm_liquid
property = relperm
phase = 0
[]
[relperm_gas]
type = PorousFlowPropertyAux
variable = relperm_gas
property = relperm
phase = 1
[]
[pp1]
type = PorousFlowPropertyAux
variable = pp1
phase = 1
property = pressure
[]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[]
[FluidProperties]
[simple_fluid] # same properties used for both phases
type = SimpleFluidProperties
bulk_modulus = 10 # so pumping does not result in excessive porepressure
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[temperature]
type = PorousFlowTemperature
temperature = 20
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 1
[]
[pc_calculator]
type = PorousFlow2PhasePS
capillary_pressure = pc
phase0_porepressure = pp0
phase1_saturation = sat1
[]
[hys_order_material]
type = PorousFlowHysteresisOrder
[]
[relperm_liquid]
type = PorousFlowHystereticRelativePermeabilityLiquid
phase = 0
S_lr = 0.1
S_gr_max = 0.2
m = 0.9
liquid_modification_range = 0.9
[]
[relperm_gas]
type = PorousFlowHystereticRelativePermeabilityGas
phase = 1
S_lr = 0.1
S_gr_max = 0.2
m = 0.9
gamma = 0.33
k_rg_max = 0.8
gas_low_extension_type = linear_like
[]
[]
[Postprocessors]
[flux]
type = FunctionValuePostprocessor
function = 'if(t <= 9, 10, -10)'
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[sat0]
type = PointValue
point = '0 0 0'
variable = sat0
[]
[sat1]
type = PointValue
point = '0 0 0'
variable = sat1
[]
[kr_liq]
type = PointValue
point = '0 0 0'
variable = relperm_liquid
[]
[kr_gas]
type = PointValue
point = '0 0 0'
variable = relperm_gas
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_shift_type'
petsc_options_value = ' lu NONZERO'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 0.5
end_time = 18
nl_abs_tol = 1E-10
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/hysteresis/1phase_3rd.i)
# Simple example of a 1-phase situation with hysteretic capillary pressure that involves a 3rd-order curve. Water is removed, added, removed and added to the system in order to observe the hysteresis
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
number_fluid_phases = 1
number_fluid_components = 1
porous_flow_vars = 'pp'
[]
[]
[Variables]
[pp]
initial_condition = 0
[]
[]
[Kernels]
[mass_conservation]
type = PorousFlowMassTimeDerivative
variable = pp
[]
[]
[DiracKernels]
[pump]
type = PorousFlowPointSourceFromPostprocessor
mass_flux = flux
point = '0.5 0 0'
variable = pp
[]
[]
[AuxVariables]
[sat]
family = MONOMIAL
order = CONSTANT
[]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[sat]
type = PorousFlowPropertyAux
variable = sat
property = saturation
[]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[temperature]
type = PorousFlowTemperature
temperature = 20
[]
[massfrac]
type = PorousFlowMassFraction
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[hys_order_material]
type = PorousFlowHysteresisOrder
[]
[pc_calculator]
type = PorousFlow1PhaseHysP
alpha_d = 10.0
alpha_w = 7.0
n_d = 1.5
n_w = 1.9
S_l_min = 0.1
S_lr = 0.2
S_gr_max = 0.3
Pc_max = 12.0
high_ratio = 0.9
low_extension_type = quadratic
high_extension_type = power
porepressure = pp
[]
[]
[Postprocessors]
[flux]
type = FunctionValuePostprocessor
function = 'if(t <= 9, -10, if(t <= 16, 10, if(t <= 22, -10, 10)))'
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[sat]
type = PointValue
point = '0 0 0'
variable = sat
[]
[pp]
type = PointValue
point = '0 0 0'
variable = pp
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 0.5
end_time = 30.5
nl_abs_tol = 1E-10
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/dirackernels/frompps.i)
# Test PorousFlowPointSourceFromPostprocessor DiracKernel
[Mesh]
type = GeneratedMesh
dim = 2
bias_x = 1.1
bias_y = 1.1
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Functions]
[mass_flux_fn]
type = PiecewiseConstant
direction = left
xy_data = '
0 0
100 -0.1
300 0
600 -0.1
1400 0
1500 0.2
2000 0.2'
[]
[]
[Variables]
[pp]
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = pp
number_fluid_phases = 1
number_fluid_components = 1
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 1000
thermal_expansion = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseFullySaturated
porepressure = pp
[]
[massfrac]
type = PorousFlowMassFraction
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.2
[]
[]
[Postprocessors]
[total_mass]
type = PorousFlowFluidMass
execute_on = 'initial timestep_end'
[]
[mass_flux_in]
type = FunctionValuePostprocessor
function = mass_flux_fn
execute_on = 'initial timestep_begin'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
nl_abs_tol = 1e-14
dt = 100
end_time = 2000
[]
[Outputs]
perf_graph = true
csv = true
execute_on = 'initial timestep_end'
file_base = frompps
[]
[ICs]
[PressureIC]
variable = pp
type = ConstantIC
value = 20e6
[]
[]
[DiracKernels]
[source]
type = PorousFlowPointSourceFromPostprocessor
variable = pp
mass_flux = mass_flux_in
point = '0.5 0.5 0'
[]
[]
(modules/porous_flow/test/tests/hysteresis/2phasePS_relperm_2.i)
# Simple example of a 2-phase situation with hysteretic relative permeability. Gas is added to and removed from the system in order to observe the hysteresis
# All liquid water exists in component 0
# All gas exists in component 1
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
number_fluid_phases = 2
number_fluid_components = 2
porous_flow_vars = 'pp0 sat1'
[]
[pc]
type = PorousFlowCapillaryPressureVG
alpha = 10.0
m = 0.33
[]
[]
[Variables]
[pp0]
[]
[sat1]
initial_condition = 0
[]
[]
[Kernels]
[mass_conservation0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pp0
[]
[mass_conservation1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = sat1
[]
[]
[DiracKernels]
[pump]
type = PorousFlowPointSourceFromPostprocessor
mass_flux = flux
point = '0.5 0 0'
variable = sat1
[]
[]
[AuxVariables]
[massfrac_ph0_sp0]
initial_condition = 1
[]
[massfrac_ph1_sp0]
initial_condition = 0
[]
[sat0]
family = MONOMIAL
order = CONSTANT
[]
[pp1]
family = MONOMIAL
order = CONSTANT
[]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[relperm_liquid]
family = MONOMIAL
order = CONSTANT
[]
[relperm_gas]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[sat0]
type = PorousFlowPropertyAux
variable = sat0
phase = 0
property = saturation
[]
[relperm_liquid]
type = PorousFlowPropertyAux
variable = relperm_liquid
property = relperm
phase = 0
[]
[relperm_gas]
type = PorousFlowPropertyAux
variable = relperm_gas
property = relperm
phase = 1
[]
[pp1]
type = PorousFlowPropertyAux
variable = pp1
phase = 1
property = pressure
[]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[]
[FluidProperties]
[simple_fluid] # same properties used for both phases
type = SimpleFluidProperties
bulk_modulus = 10 # so pumping does not result in excessive porepressure
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[temperature]
type = PorousFlowTemperature
temperature = 20
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 1
[]
[pc_calculator]
type = PorousFlow2PhasePS
capillary_pressure = pc
phase0_porepressure = pp0
phase1_saturation = sat1
[]
[hys_order_material]
type = PorousFlowHysteresisOrder
[]
[relperm_liquid]
type = PorousFlowHystereticRelativePermeabilityLiquid
phase = 0
S_lr = 0.4
S_gr_max = 0.2
m = 0.9
liquid_modification_range = 0.9
[]
[relperm_gas]
type = PorousFlowHystereticRelativePermeabilityGas
phase = 1
S_lr = 0.4
S_gr_max = 0.2
m = 0.9
gamma = 0.33
k_rg_max = 1.0
gas_low_extension_type = linear_like
[]
[]
[Postprocessors]
[flux]
type = FunctionValuePostprocessor
function = 'if(t <= 15, 20, -20)'
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[sat0]
type = PointValue
point = '0 0 0'
variable = sat0
[]
[sat1]
type = PointValue
point = '0 0 0'
variable = sat1
[]
[kr_liq]
type = PointValue
point = '0 0 0'
variable = relperm_liquid
[]
[kr_gas]
type = PointValue
point = '0 0 0'
variable = relperm_gas
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_shift_type'
petsc_options_value = ' lu NONZERO'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 5
end_time = 29
nl_abs_tol = 1E-10
[]
[Outputs]
[csv]
type = CSV
sync_times = '0 1 2 3 8 12 13 14 15 16 17 18 20 24 25 26 27 28 29'
sync_only = true
file_base = '2phasePS_relperm_2_none'
[]
[]
(modules/porous_flow/test/tests/hysteresis/hys_order_03.i)
# Test that PorousFlowHysteresisOrder correctly calculates hysteresis order
# Water is removed from the system (so order = 0) until saturation = 0.49
# Then, water is added to the system (so order = 1) until saturation = 0.94
# Then, water is removed from the system (so order = 2) until saturation = 0.62
# Then, water is added to the system (so order = 3) until saturation = 0.87
# Then, water is removed from the system (so order = 3, because max_order = 3) until saturation = 0.68
# Then, water is added to the system (so order = 3, because max_order = 3) until saturation = 0.87
# Then, water is removed from the system (so order = 3, because max_order = 3) until saturation = 0.62
# Then, water is removed from the system (so order = 2) until saturation = 0.49
# Then, water is removed from the system (so order = 0)
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pp]
initial_condition = 0.0
[]
[]
[PorousFlowUnsaturated]
porepressure = pp
fp = simple_fluid
[]
[DiracKernels]
[source_sink_0]
type = PorousFlowPointSourceFromPostprocessor
point = '0 0 0'
mass_flux = sink_strength
variable = pp
[]
[source_sink_1]
type = PorousFlowPointSourceFromPostprocessor
point = '1 0 0'
mass_flux = sink_strength
variable = pp
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 1.0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '0 0 0 0 0 0 0 0 0'
[]
[hys_order]
type = PorousFlowHysteresisOrder
[]
[]
[AuxVariables]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[tp0]
family = MONOMIAL
order = CONSTANT
[]
[tp1]
family = MONOMIAL
order = CONSTANT
[]
[tp2]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[tp0]
type = PorousFlowPropertyAux
variable = tp0
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 0
[]
[tp1]
type = PorousFlowPropertyAux
variable = tp1
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 1
[]
[tp2]
type = PorousFlowPropertyAux
variable = tp2
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 2
[]
[]
[Functions]
[sink_strength_fcn]
type = ParsedFunction
expression = '30 * if(t <= 8, -1, if(t <= 15, 1, if(t <= 20, -1, if(t <= 24, 1, if(t <= 27, -1, if(t <= 30, 1, -1))))))'
[]
[]
[Postprocessors]
[sink_strength]
type = FunctionValuePostprocessor
function = sink_strength_fcn
outputs = 'none'
[]
[saturation]
type = PointValue
point = '0 0 0'
variable = saturation0
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[tp0]
type = PointValue
point = '0 0 0'
variable = tp0
[]
[tp1]
type = PointValue
point = '0 0 0'
variable = tp1
[]
[tp2]
type = PointValue
point = '0 0 0'
variable = tp2
[]
[]
[Preconditioning]
[basic]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 40
nl_abs_tol = 1E-7
[]
[Outputs]
[csv]
type = CSV
sync_times = '0 1 2 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 37 40' # cut out the times around which order reductions occur becuase numerical roundoff might mean order is not reduced exactly at these times
sync_only = true
[]
[]
(modules/porous_flow/test/tests/hysteresis/hys_order_04.i)
# Test that PorousFlowHysteresisOrder correctly calculates hysteresis order
# Hysteresis order is initialised = 3, with turning points = (0.5, 0.9, 0.6)
# Initial saturation is 0.71
# Water is removed from the system (so order = 3) until saturation = 0.6
# Water is removed from the system (so order = 2) until saturation = 0.5
# Water is removed from the system (so order = 0)
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pp]
initial_condition = -9E5
[]
[]
[PorousFlowUnsaturated]
porepressure = pp
fp = simple_fluid
[]
[DiracKernels]
[source_sink_0]
type = PorousFlowPointSourceFromPostprocessor
point = '0 0 0'
mass_flux = sink_strength
variable = pp
[]
[source_sink_1]
type = PorousFlowPointSourceFromPostprocessor
point = '1 0 0'
mass_flux = sink_strength
variable = pp
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 1.0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '0 0 0 0 0 0 0 0 0'
[]
[hys_order]
type = PorousFlowHysteresisOrder
initial_order = 3
previous_turning_points = '0.5 0.9 0.6'
[]
[]
[AuxVariables]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[tp0]
family = MONOMIAL
order = CONSTANT
[]
[tp1]
family = MONOMIAL
order = CONSTANT
[]
[tp2]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[tp0]
type = PorousFlowPropertyAux
variable = tp0
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 0
[]
[tp1]
type = PorousFlowPropertyAux
variable = tp1
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 1
[]
[tp2]
type = PorousFlowPropertyAux
variable = tp2
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 2
[]
[]
[Functions]
[sink_strength_fcn]
type = ParsedFunction
expression = '-30'
[]
[]
[Postprocessors]
[sink_strength]
type = FunctionValuePostprocessor
function = sink_strength_fcn
outputs = 'none'
[]
[saturation]
type = PointValue
point = '0 0 0'
variable = saturation0
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[tp0]
type = PointValue
point = '0 0 0'
variable = tp0
[]
[tp1]
type = PointValue
point = '0 0 0'
variable = tp1
[]
[tp2]
type = PointValue
point = '0 0 0'
variable = tp2
[]
[]
[Preconditioning]
[basic]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 6
nl_abs_tol = 1E-7
[]
[Outputs]
[csv]
type = CSV
[]
[]
(modules/porous_flow/test/tests/sinks/s14.i)
# Apply a PorousFlowPointSourceFromPostprocessor that injects 1kg/s into a 2D model, and PorousFlowOutflowBCs to the outer boundaries to show that the PorousFlowOutflowBCs allow fluid to exit freely at the appropriate rate
[Mesh]
type = GeneratedMesh
dim = 2
nx = 3
xmin = -1
xmax = 1
ny = 2
ymin = -2
ymax = 2
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[pp]
[]
[]
[PorousFlowFullySaturated]
fp = simple_fluid
porepressure = pp
[]
[DiracKernels]
[injection]
type = PorousFlowPointSourceFromPostprocessor
mass_flux = 1
point = '0 0 0'
variable = pp
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 1
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.12
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '0.4 0 0 0 0.4 0 0 0 0.4'
[]
[]
[BCs]
[outflow]
type = PorousFlowOutflowBC
boundary = 'left right top bottom'
variable = pp
save_in = nodal_outflow
[]
[]
[AuxVariables]
[nodal_outflow]
[]
[]
[Postprocessors]
[outflow_kg_per_s]
type = NodalSum
boundary = 'left right top bottom'
variable = nodal_outflow
[]
[]
[Preconditioning]
[andy]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 3E-4
end_time = 30E-4
nl_abs_tol = 1E-9
nl_rel_tol = 1E-9
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/hysteresis/2phasePS_2.i)
# Simple example of a 2-phase situation with hysteretic capillary pressure. Gas is added to, removed from, and added to the system in order to observe the hysteresis
# All liquid water exists in component 0
# All gas exists in component 1
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
number_fluid_phases = 2
number_fluid_components = 2
porous_flow_vars = 'pp0 sat1'
[]
[]
[Variables]
[pp0]
[]
[sat1]
initial_condition = 0
[]
[]
[Kernels]
[mass_conservation0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pp0
[]
[mass_conservation1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = sat1
[]
[]
[DiracKernels]
[pump]
type = PorousFlowPointSourceFromPostprocessor
mass_flux = flux
point = '0.5 0 0'
variable = sat1
[]
[]
[AuxVariables]
[massfrac_ph0_sp0]
initial_condition = 1
[]
[massfrac_ph1_sp0]
initial_condition = 0
[]
[sat0]
family = MONOMIAL
order = CONSTANT
[]
[pp1]
family = MONOMIAL
order = CONSTANT
[]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[sat0]
type = PorousFlowPropertyAux
variable = sat0
phase = 0
property = saturation
[]
[pp1]
type = PorousFlowPropertyAux
variable = pp1
phase = 1
property = pressure
[]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[]
[FluidProperties]
[simple_fluid] # same properties used for both phases
type = SimpleFluidProperties
bulk_modulus = 10 # so pumping does not result in excessive porepressure
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[temperature]
type = PorousFlowTemperature
temperature = 20
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 1
[]
[hys_order_material]
type = PorousFlowHysteresisOrder
[]
[pc_calculator]
type = PorousFlow2PhaseHysPS
alpha_d = 10.0
alpha_w = 7.0
n_d = 1.5
n_w = 1.9
S_l_min = 0.1
S_lr = 0.2
S_gr_max = 0.3
Pc_max = 12.0
high_ratio = 0.9
low_extension_type = quadratic
high_extension_type = power
phase0_porepressure = pp0
phase1_saturation = sat1
[]
[]
[Postprocessors]
[flux]
type = FunctionValuePostprocessor
function = 'if(t <= 14, 10, if(t <= 25, -10, 10))'
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[sat0]
type = PointValue
point = '0 0 0'
variable = sat0
[]
[sat1]
type = PointValue
point = '0 0 0'
variable = sat1
[]
[pp0]
type = PointValue
point = '0 0 0'
variable = pp0
[]
[pp1]
type = PointValue
point = '0 0 0'
variable = pp1
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_shift_type'
petsc_options_value = ' lu NONZERO'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 4
end_time = 46
nl_abs_tol = 1E-10
[]
[Outputs]
csv = true
sync_times = '13 14 15 24 25 25.5 26 27 28 29'
[]
(modules/porous_flow/test/tests/energy_conservation/heat04_rz.i)
# The sample is a single unit element in RZ coordinates
# A constant velocity is applied to the outer boundary is free to move as a source injects heat and fluid into the system
# There is no fluid flow or heat flow.
# Heat energy conservation is checked.
# Mass conservation is checked
[Mesh]
type = GeneratedMesh
dim = 2
nx = 1
ny = 1
xmin = 1
xmax = 2
ymin = -0.5
ymax = 0.5
coord_type = RZ
[]
[GlobalParams]
displacements = 'disp_r disp_z'
PorousFlowDictator = dictator
block = 0
biot_coefficient = 0.3
[]
[Variables]
[disp_r]
[]
[disp_z]
[]
[pp]
initial_condition = 0.1
[]
[temp]
initial_condition = 10
[]
[]
[BCs]
[plane_strain]
type = DirichletBC
variable = disp_z
value = 0
boundary = 'bottom top'
[]
[rmin_fixed]
type = DirichletBC
variable = disp_r
value = 0
boundary = left
[]
[contract]
type = FunctionDirichletBC
variable = disp_r
function = -0.01*t
boundary = right
[]
[]
[PorousFlowFullySaturated]
coupling_type = ThermoHydroMechanical
porepressure = pp
temperature = temp
fp = simple_fluid
[]
[DiracKernels]
[heat_source]
type = PorousFlowPointSourceFromPostprocessor
point = '1.5 0 0'
variable = temp
mass_flux = 10
[]
[fluid_source]
type = PorousFlowPointSourceFromPostprocessor
point = '1.5 0 0'
variable = pp
mass_flux = 1
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 0.5
density0 = 1
viscosity = 1
thermal_expansion = 0
cv = 1.3
[]
[]
[Materials]
[elasticity_tensor]
type = ComputeElasticityTensor
C_ijkl = '1 1.5'
# bulk modulus is lambda + 2*mu/3 = 1 + 2*1.5/3 = 2
fill_method = symmetric_isotropic
[]
[strain]
type = ComputeAxisymmetricRZSmallStrain
[]
[stress]
type = ComputeLinearElasticStress
[]
[porosity]
type = PorousFlowPorosity
porosity_zero = 0.1
[]
[rock_heat]
type = PorousFlowMatrixInternalEnergy
specific_heat_capacity = 2.2
density = 0.5
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '0.5 0 0 0 0.5 0 0 0 0.5'
[]
[thermal_cond]
type = PorousFlowThermalConductivityIdeal
dry_thermal_conductivity = '1 0 0 0 1 0 0 0 1'
[]
[]
[Postprocessors]
[p0]
type = PointValue
outputs = 'console csv'
execute_on = 'initial timestep_end'
point = '1 0 0'
variable = pp
[]
[t0]
type = PointValue
outputs = 'console csv'
execute_on = 'initial timestep_end'
point = '1 0 0'
variable = temp
[]
[rdisp]
type = PointValue
outputs = 'csv console'
point = '2 0 0'
use_displaced_mesh = false
variable = disp_r
[]
[fluid_mass]
type = PorousFlowFluidMass
fluid_component = 0
execute_on = 'initial timestep_end'
outputs = 'console csv'
[]
[total_heat]
type = PorousFlowHeatEnergy
phase = 0
execute_on = 'initial timestep_end'
outputs = 'console csv'
[]
[rock_heat]
type = PorousFlowHeatEnergy
execute_on = 'initial timestep_end'
outputs = 'console csv'
[]
[fluid_heat]
type = PorousFlowHeatEnergy
include_porous_skeleton = false
phase = 0
execute_on = 'initial timestep_end'
outputs = 'console csv'
[]
[]
[Preconditioning]
[andy]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 2
end_time = 10
[]
[Outputs]
execute_on = 'initial timestep_end'
[csv]
type = CSV
[]
[]
(modules/porous_flow/test/tests/hysteresis/hys_order_07.i)
# Test that PorousFlowHysteresisOrder correctly calculates hysteresis order
# Hysteresis order is initialised = 3, with turning points = (0.5, 0.8, 0.66)
# Initial saturation is 0.71
# Water is removed from the system (so order = 3) until saturation = 0.66
# Then, water is removed from the system (so order = 2) until saturation = 0.65
# Then, water is added to the system (so order = 3 with turning point = 0.65) until saturation = 0.8
# Then, water is added to the system (so order = 1) until saturation = 1
# Then, water is added to the system (so order = 0)
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pp]
initial_condition = -9E5
[]
[]
[PorousFlowUnsaturated]
porepressure = pp
fp = simple_fluid
[]
[DiracKernels]
[source_sink_0]
type = PorousFlowPointSourceFromPostprocessor
point = '0 0 0'
mass_flux = sink_strength
variable = pp
[]
[source_sink_1]
type = PorousFlowPointSourceFromPostprocessor
point = '1 0 0'
mass_flux = sink_strength
variable = pp
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 1.0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '0 0 0 0 0 0 0 0 0'
[]
[hys_order]
type = PorousFlowHysteresisOrder
initial_order = 3
previous_turning_points = '0.6 0.8 0.66'
[]
[]
[AuxVariables]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[tp0]
family = MONOMIAL
order = CONSTANT
[]
[tp1]
family = MONOMIAL
order = CONSTANT
[]
[tp2]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[tp0]
type = PorousFlowPropertyAux
variable = tp0
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 0
[]
[tp1]
type = PorousFlowPropertyAux
variable = tp1
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 1
[]
[tp2]
type = PorousFlowPropertyAux
variable = tp2
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 2
[]
[]
[Functions]
[sink_strength_fcn]
type = ParsedFunction
expression = '30 * if(t <= 1, -1, 1)'
[]
[]
[Postprocessors]
[sink_strength]
type = FunctionValuePostprocessor
function = sink_strength_fcn
outputs = 'none'
[]
[saturation]
type = PointValue
point = '0 0 0'
variable = saturation0
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[tp0]
type = PointValue
point = '0 0 0'
variable = tp0
[]
[tp1]
type = PointValue
point = '0 0 0'
variable = tp1
[]
[tp2]
type = PointValue
point = '0 0 0'
variable = tp2
[]
[]
[Preconditioning]
[basic]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 9
nl_abs_tol = 1E-7
[]
[Outputs]
[csv]
type = CSV
[]
[]
(modules/porous_flow/test/tests/mass_conservation/mass11.i)
# The sample is a single unit element, with roller BCs on the sides and bottom.
# The top is free to move and fluid is injected at a constant rate of 1kg/s
# There is no fluid flow.
# Fluid mass conservation is checked.
# Under these conditions the fluid mass should increase at 1kg/s
# The porepressure should increase: rho0 * exp(P/bulk) = rho * exp(P0/bulk) + 1*t
# The stress_zz should be exactly biot * P since total stress is zero
[Mesh]
type = GeneratedMesh
dim = 3
nx = 1
ny = 1
nz = 1
xmin = -0.5
xmax = 0.5
ymin = -0.5
ymax = 0.5
zmin = -0.5
zmax = 0.5
[]
[GlobalParams]
displacements = 'disp_x disp_y disp_z'
PorousFlowDictator = dictator
block = 0
[]
[Variables]
[disp_x]
[]
[disp_y]
[]
[disp_z]
[]
[porepressure]
initial_condition = 0.1
[]
[]
[BCs]
[confinex]
type = DirichletBC
variable = disp_x
value = 0
boundary = 'left right'
[]
[confiney]
type = DirichletBC
variable = disp_y
value = 0
boundary = 'bottom top'
[]
[basefixed]
type = DirichletBC
variable = disp_z
value = 0
boundary = back
[]
[]
[Kernels]
[grad_stress_x]
type = StressDivergenceTensors
variable = disp_x
component = 0
[]
[grad_stress_y]
type = StressDivergenceTensors
variable = disp_y
component = 1
[]
[grad_stress_z]
type = StressDivergenceTensors
variable = disp_z
component = 2
[]
[poro_x]
type = PorousFlowEffectiveStressCoupling
biot_coefficient = 0.3
variable = disp_x
component = 0
[]
[poro_y]
type = PorousFlowEffectiveStressCoupling
biot_coefficient = 0.3
variable = disp_y
component = 1
[]
[poro_z]
type = PorousFlowEffectiveStressCoupling
biot_coefficient = 0.3
component = 2
variable = disp_z
[]
[poro_vol_exp]
type = PorousFlowMassVolumetricExpansion
variable = porepressure
fluid_component = 0
[]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = porepressure
[]
[]
[DiracKernels]
[inject]
type = PorousFlowPointSourceFromPostprocessor
point = '0 0 0'
mass_flux = 1.0
variable = porepressure
[]
[]
[AuxVariables]
[stress_xx]
order = CONSTANT
family = MONOMIAL
[]
[stress_xy]
order = CONSTANT
family = MONOMIAL
[]
[stress_xz]
order = CONSTANT
family = MONOMIAL
[]
[stress_yy]
order = CONSTANT
family = MONOMIAL
[]
[stress_yz]
order = CONSTANT
family = MONOMIAL
[]
[stress_zz]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[stress_xx]
type = RankTwoAux
rank_two_tensor = stress
variable = stress_xx
index_i = 0
index_j = 0
[]
[stress_xy]
type = RankTwoAux
rank_two_tensor = stress
variable = stress_xy
index_i = 0
index_j = 1
[]
[stress_xz]
type = RankTwoAux
rank_two_tensor = stress
variable = stress_xz
index_i = 0
index_j = 2
[]
[stress_yy]
type = RankTwoAux
rank_two_tensor = stress
variable = stress_yy
index_i = 1
index_j = 1
[]
[stress_yz]
type = RankTwoAux
rank_two_tensor = stress
variable = stress_yz
index_i = 1
index_j = 2
[]
[stress_zz]
type = RankTwoAux
rank_two_tensor = stress
variable = stress_zz
index_i = 2
index_j = 2
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 0.5
density0 = 1
thermal_expansion = 0
viscosity = 1
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[elasticity_tensor]
type = ComputeElasticityTensor
C_ijkl = '1 1.5'
# bulk modulus is lambda + 2*mu/3 = 1 + 2*1.5/3 = 2
fill_method = symmetric_isotropic
[]
[strain]
type = ComputeSmallStrain
[]
[stress]
type = ComputeLinearElasticStress
[]
[vol_strain]
type = PorousFlowVolumetricStrain
[]
[eff_fluid_pressure]
type = PorousFlowEffectiveFluidPressure
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '0.5 0 0 0 0.5 0 0 0 0.5'
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure disp_x disp_y disp_z'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureVG
m = 0.5
alpha = 1
[]
[]
[Postprocessors]
[p0]
type = PointValue
outputs = 'console csv'
execute_on = 'initial timestep_end'
point = '0 0 0'
variable = porepressure
[]
[zdisp]
type = PointValue
outputs = csv
point = '0 0 0.5'
use_displaced_mesh = false
variable = disp_z
[]
[stress_xx]
type = PointValue
outputs = csv
point = '0 0 0'
variable = stress_xx
[]
[stress_yy]
type = PointValue
outputs = csv
point = '0 0 0'
variable = stress_yy
[]
[stress_zz]
type = PointValue
outputs = csv
point = '0 0 0'
variable = stress_zz
[]
[fluid_mass]
type = PorousFlowFluidMass
fluid_component = 0
execute_on = 'initial timestep_end'
outputs = 'console csv'
[]
[]
[Preconditioning]
[andy]
type = SMP
full = true
petsc_options_iname = '-ksp_type -pc_type -snes_atol -snes_rtol -snes_max_it'
petsc_options_value = 'bcgs bjacobi 1E-14 1E-8 10000'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
start_time = 0
end_time = 10
dt = 2
[]
[Outputs]
execute_on = 'initial timestep_end'
[csv]
type = CSV
[]
[]
(modules/porous_flow/test/tests/hysteresis/hys_order_01.i)
# Test that PorousFlowHysteresisOrder correctly calculates hysteresis order
# Water is removed from the system (so order = 0) until saturation = S0
# Then, water is added to the system (so order = 1) until saturation = S1
# Then, water is removed from the system (so order = 2)
# More water is removed from the system so that the saturation < S0 (so order = 0)
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pp]
initial_condition = 0.0
[]
[]
[PorousFlowUnsaturated]
porepressure = pp
fp = simple_fluid
[]
[DiracKernels]
[source_sink_0]
type = PorousFlowPointSourceFromPostprocessor
point = '0 0 0'
mass_flux = sink_strength
variable = pp
[]
[source_sink_1]
type = PorousFlowPointSourceFromPostprocessor
point = '1 0 0'
mass_flux = sink_strength
variable = pp
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 1.0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '0 0 0 0 0 0 0 0 0'
[]
[hys_order]
type = PorousFlowHysteresisOrder
[]
[]
[AuxVariables]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[tp0]
family = MONOMIAL
order = CONSTANT
[]
[tp1]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[tp0]
type = PorousFlowPropertyAux
variable = tp0
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 0
[]
[tp1]
type = PorousFlowPropertyAux
variable = tp1
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 1
[]
[]
[Functions]
[sink_strength_fcn]
type = ParsedFunction
expression = '30 * if(t <= 4, -1, if(t <= 7, 1, -1))'
[]
[]
[Postprocessors]
[sink_strength]
type = FunctionValuePostprocessor
function = sink_strength_fcn
outputs = 'none'
[]
[saturation]
type = PointValue
point = '0 0 0'
variable = saturation0
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[tp0]
type = PointValue
point = '0 0 0'
variable = tp0
[]
[tp1]
type = PointValue
point = '0 0 0'
variable = tp1
[]
[]
[Preconditioning]
[basic]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 13
nl_abs_tol = 1E-7
[]
[Outputs]
[csv]
type = CSV
sync_times = '0 1 5 6 7 8 9 10 11 13' # cut out t=12 because numerical roundoff might mean order is not reduced exactly at t=12
sync_only = true
[]
[]
(modules/porous_flow/test/tests/sinks/s15.i)
# Apply a PorousFlowPointSourceFromPostprocessor that injects 1J/s into a 2D model, and PorousFlowOutflowBCs to the outer boundaries to show that the PorousFlowOutflowBCs allow heat-energy to exit freely at the appropriate rate
[Mesh]
type = GeneratedMesh
dim = 2
nx = 3
xmin = -1
xmax = 1
ny = 2
ymin = -2
ymax = 2
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[pp]
[]
[T]
scaling = 1E-7
[]
[]
[PorousFlowFullySaturated]
fp = simple_fluid
coupling_type = thermohydro
porepressure = pp
temperature = T
[]
[DiracKernels]
[injection]
type = PorousFlowPointSourceFromPostprocessor
mass_flux = 1
point = '0 0 0'
variable = T
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 1
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.12
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '0.4 0 0 0 0.4 0 0 0 0.4'
[]
[matrix]
type = PorousFlowMatrixInternalEnergy
density = 0.15
specific_heat_capacity = 1.5
[]
[thermal_cond]
type = PorousFlowThermalConductivityIdeal
dry_thermal_conductivity = '0.3 0 0 0 0.3 0 0 0 0.3'
[]
[]
[BCs]
[outflow]
type = PorousFlowOutflowBC
boundary = 'left right top bottom'
flux_type = heat
variable = T
save_in = nodal_outflow
[]
[]
[AuxVariables]
[nodal_outflow]
[]
[]
[Postprocessors]
[outflow_J_per_s]
type = NodalSum
boundary = 'left right top bottom'
variable = nodal_outflow
[]
[]
[Preconditioning]
[andy]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 2E6
end_time = 2E7
nl_abs_tol = 1E-14
# nl_rel_tol = 1E-12
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/hysteresis/hys_order_02.i)
# Test that PorousFlowHysteresisOrder correctly calculates hysteresis order
# Water is removed from the system (so order = 0) until saturation = 0.55
# Then, water is added to the system (so order = 1) until saturation = 0.74
# Then, water is removed from the system (so order = 2) until saturation = 0.62
# Then, water is added to the system (so order = 3)
# Then, water is added to the system so that saturation exceeds 0.74, so order = 1
# Then, water is added to the system to saturation becomes 1, so order = 0
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pp]
initial_condition = 0.0
[]
[]
[PorousFlowUnsaturated]
porepressure = pp
fp = simple_fluid
[]
[DiracKernels]
[source_sink_0]
type = PorousFlowPointSourceFromPostprocessor
point = '0 0 0'
mass_flux = sink_strength
variable = pp
[]
[source_sink_1]
type = PorousFlowPointSourceFromPostprocessor
point = '1 0 0'
mass_flux = sink_strength
variable = pp
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 1.0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '0 0 0 0 0 0 0 0 0'
[]
[hys_order]
type = PorousFlowHysteresisOrder
[]
[]
[AuxVariables]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[tp0]
family = MONOMIAL
order = CONSTANT
[]
[tp1]
family = MONOMIAL
order = CONSTANT
[]
[tp2]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[tp0]
type = PorousFlowPropertyAux
variable = tp0
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 0
[]
[tp1]
type = PorousFlowPropertyAux
variable = tp1
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 1
[]
[tp2]
type = PorousFlowPropertyAux
variable = tp2
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 2
[]
[]
[Functions]
[sink_strength_fcn]
type = ParsedFunction
expression = '30 * if(t <= 7, -1, if(t <= 10, 1, if(t <= 12, -1, 1)))'
[]
[]
[Postprocessors]
[sink_strength]
type = FunctionValuePostprocessor
function = sink_strength_fcn
outputs = 'none'
[]
[saturation]
type = PointValue
point = '0 0 0'
variable = saturation0
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[tp0]
type = PointValue
point = '0 0 0'
variable = tp0
[]
[tp1]
type = PointValue
point = '0 0 0'
variable = tp1
[]
[tp2]
type = PointValue
point = '0 0 0'
variable = tp2
[]
[]
[Preconditioning]
[basic]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 21
nl_abs_tol = 1E-7
[]
[Outputs]
[csv]
type = CSV
sync_times = '0 1 2 9 10 11 12 13 14 15 17 18 19 21' # cut out t=16 and t=20 because numerical roundoff might mean order is not reduced exactly at these times
sync_only = true
[]
[]
(modules/porous_flow/test/tests/dirackernels/hfrompps.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 3
ny = 3
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pressure]
[]
[temperature]
scaling = 1E-6
[]
[]
[ICs]
[pressure_ic]
type = ConstantIC
variable = pressure
value = 1e6
[]
[temperature_ic]
type = ConstantIC
variable = temperature
value = 400
[]
[]
[Kernels]
[P_time_deriv]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pressure
[]
[P_flux]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = pressure
gravity = '0 -9.8 0'
[]
[energy_dot]
type = PorousFlowEnergyTimeDerivative
variable = temperature
[]
[heat_conduction]
type = PorousFlowHeatConduction
variable = temperature
[]
[heat_advection]
type = PorousFlowHeatAdvection
variable = temperature
gravity = '0 -9.8 0'
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pressure temperature'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[Functions]
[mass_flux_in_fn]
type = PiecewiseConstant
direction = left
xy_data = '
0 0
100 0.1
300 0
600 0.1
1400 0
1500 0.2'
[]
[T_in_fn]
type = PiecewiseLinear
xy_data = '
0 400
600 450'
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 1000
thermal_expansion = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = temperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = pressure
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
at_nodes = true
[]
[fluid_props]
type = PorousFlowSingleComponentFluid
phase = 0
fp = simple_fluid
[]
[relperm]
type = PorousFlowRelativePermeabilityCorey
n = 1
phase = 0
[]
[fp_mat]
type = FluidPropertiesMaterialPT
pressure = pressure
temperature = temperature
fp = simple_fluid
[]
[rock_heat]
type = PorousFlowMatrixInternalEnergy
specific_heat_capacity = 830.0
density = 2750
[]
[thermal_conductivity]
type = PorousFlowThermalConductivityIdeal
dry_thermal_conductivity = '2.5 0 0 0 2.5 0 0 0 2.5'
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1.0E-15 0 0 0 1.0E-15 0 0 0 1.0E-14'
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[]
[DiracKernels]
[source]
type = PorousFlowPointSourceFromPostprocessor
variable = pressure
mass_flux = mass_flux_in
point = '0.5 0.5 0'
[]
[source_h]
type = PorousFlowPointEnthalpySourceFromPostprocessor
variable = temperature
mass_flux = mass_flux_in
point = '0.5 0.5 0'
T_in = T_in
pressure = pressure
fp = simple_fluid
[]
[]
[Preconditioning]
[preferred]
type = SMP
full = true
petsc_options_iname = '-pc_type'
petsc_options_value = ' lu '
[]
[]
[Postprocessors]
[total_mass]
type = PorousFlowFluidMass
execute_on = 'initial timestep_end'
[]
[total_heat]
type = PorousFlowHeatEnergy
[]
[mass_flux_in]
type = FunctionValuePostprocessor
function = mass_flux_in_fn
execute_on = 'initial timestep_end'
[]
[avg_temp]
type = ElementAverageValue
variable = temperature
execute_on = 'initial timestep_end'
[]
[T_in]
type = FunctionValuePostprocessor
function = T_in_fn
execute_on = 'initial timestep_end'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
nl_abs_tol = 1e-14
dt = 100
end_time = 2000
[]
[Outputs]
csv = true
execute_on = 'initial timestep_end'
file_base = hfrompps
[]
(modules/porous_flow/test/tests/hysteresis/hys_order_05.i)
# Test that PorousFlowHysteresisOrder correctly calculates hysteresis order
# Hysteresis order is initialised = 2, with turning points = (0.6, 0.8)
# Initial saturation is 0.71
# Water is removed from the system (so order = 2) until saturation = 0.6
# Then, water is removed from the system (so order = 0) until saturation = 0.58
# Then, water is added to the system (so order = 1 and turning point = 0.58) until saturation = 0.9
# Then, water is removed from the system (so order = 2 and turning point = 0.9)
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pp]
initial_condition = -9E5
[]
[]
[PorousFlowUnsaturated]
porepressure = pp
fp = simple_fluid
[]
[DiracKernels]
[source_sink_0]
type = PorousFlowPointSourceFromPostprocessor
point = '0 0 0'
mass_flux = sink_strength
variable = pp
[]
[source_sink_1]
type = PorousFlowPointSourceFromPostprocessor
point = '1 0 0'
mass_flux = sink_strength
variable = pp
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 1.0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '0 0 0 0 0 0 0 0 0'
[]
[hys_order]
type = PorousFlowHysteresisOrder
initial_order = 2
previous_turning_points = '0.6 0.8'
[]
[]
[AuxVariables]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[tp0]
family = MONOMIAL
order = CONSTANT
[]
[tp1]
family = MONOMIAL
order = CONSTANT
[]
[tp2]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[tp0]
type = PorousFlowPropertyAux
variable = tp0
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 0
[]
[tp1]
type = PorousFlowPropertyAux
variable = tp1
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 1
[]
[tp2]
type = PorousFlowPropertyAux
variable = tp2
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 2
[]
[]
[Functions]
[sink_strength_fcn]
type = ParsedFunction
expression = '30 * if(t <= 2, -1, if(t <= 7, 1, -1))'
[]
[]
[Postprocessors]
[sink_strength]
type = FunctionValuePostprocessor
function = sink_strength_fcn
outputs = 'none'
[]
[saturation]
type = PointValue
point = '0 0 0'
variable = saturation0
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[tp0]
type = PointValue
point = '0 0 0'
variable = tp0
[]
[tp1]
type = PointValue
point = '0 0 0'
variable = tp1
[]
[tp2]
type = PointValue
point = '0 0 0'
variable = tp2
[]
[]
[Preconditioning]
[basic]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 10
nl_abs_tol = 1E-7
[]
[Outputs]
[csv]
type = CSV
[]
[]
(modules/porous_flow/test/tests/hysteresis/hys_order_08.i)
# Test that PorousFlowHysteresisOrder correctly calculates hysteresis order
# Hysteresis order is initialised = 3, with turning points = (0.5, 0.8, 0.66)
# Initial saturation is 0.71
# A large amount of water is removed in one timestep so the saturation becomes 0.58 (and order = 0)
# Then, water is added to the system (order = 1, with turning point = 0.58) until saturation = 0.67
# Then, a large amount of water is removed from the system so order becomes 0
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pp]
initial_condition = -9E5
[]
[]
[PorousFlowUnsaturated]
porepressure = pp
fp = simple_fluid
[]
[DiracKernels]
[source_sink_0]
type = PorousFlowPointSourceFromPostprocessor
point = '0 0 0'
mass_flux = sink_strength
variable = pp
[]
[source_sink_1]
type = PorousFlowPointSourceFromPostprocessor
point = '1 0 0'
mass_flux = sink_strength
variable = pp
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 1.0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '0 0 0 0 0 0 0 0 0'
[]
[hys_order]
type = PorousFlowHysteresisOrder
initial_order = 3
previous_turning_points = '0.6 0.8 0.66'
[]
[]
[AuxVariables]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[tp0]
family = MONOMIAL
order = CONSTANT
[]
[tp1]
family = MONOMIAL
order = CONSTANT
[]
[tp2]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[tp0]
type = PorousFlowPropertyAux
variable = tp0
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 0
[]
[tp1]
type = PorousFlowPropertyAux
variable = tp1
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 1
[]
[tp2]
type = PorousFlowPropertyAux
variable = tp2
property = hysteresis_saturation_turning_point
hysteresis_turning_point = 2
[]
[]
[Functions]
[sink_strength_fcn]
type = ParsedFunction
expression = '30 * if(t <= 1, -2, if(t <= 2, 1.5, -2))'
[]
[]
[Postprocessors]
[sink_strength]
type = FunctionValuePostprocessor
function = sink_strength_fcn
outputs = 'none'
[]
[saturation]
type = PointValue
point = '0 0 0'
variable = saturation0
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[tp0]
type = PointValue
point = '0 0 0'
variable = tp0
[]
[tp1]
type = PointValue
point = '0 0 0'
variable = tp1
[]
[tp2]
type = PointValue
point = '0 0 0'
variable = tp2
[]
[]
[Preconditioning]
[basic]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 5
nl_abs_tol = 1E-7
[]
[Outputs]
[csv]
type = CSV
[]
[]
(modules/porous_flow/test/tests/hysteresis/1phase.i)
# Simple example of a 1-phase situation with hysteretic capillary pressure. Water is removed and added to the system in order to observe the hysteresis
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
number_fluid_phases = 1
number_fluid_components = 1
porous_flow_vars = 'pp'
[]
[]
[Variables]
[pp]
initial_condition = 0
[]
[]
[Kernels]
[mass_conservation]
type = PorousFlowMassTimeDerivative
variable = pp
[]
[]
[DiracKernels]
[pump]
type = PorousFlowPointSourceFromPostprocessor
mass_flux = flux
point = '0.5 0 0'
variable = pp
[]
[]
[AuxVariables]
[sat]
family = MONOMIAL
order = CONSTANT
[]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[sat]
type = PorousFlowPropertyAux
variable = sat
property = saturation
[]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[temperature]
type = PorousFlowTemperature
temperature = 20
[]
[massfrac]
type = PorousFlowMassFraction
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[hys_order_material]
type = PorousFlowHysteresisOrder
[]
[pc_calculator]
type = PorousFlow1PhaseHysP
alpha_d = 10.0
alpha_w = 7.0
n_d = 1.5
n_w = 1.9
S_l_min = 0.1
S_lr = 0.2
S_gr_max = 0.3
Pc_max = 12.0
high_ratio = 0.9
low_extension_type = quadratic
high_extension_type = power
porepressure = pp
[]
[]
[Postprocessors]
[flux]
type = FunctionValuePostprocessor
function = 'if(t <= 9, -10, 10)'
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[sat]
type = PointValue
point = '0 0 0'
variable = sat
[]
[pp]
type = PointValue
point = '0 0 0'
variable = pp
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 0.5
end_time = 19
nl_abs_tol = 1E-10
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/hysteresis/1phase_relperm.i)
# Simple example of a 1-phase situation with hysteretic relative permeability. Water is removed and added to the system in order to observe the hysteresis
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
number_fluid_phases = 1
number_fluid_components = 1
porous_flow_vars = 'pp'
[]
[pc]
type = PorousFlowCapillaryPressureVG
alpha = 10.0
m = 0.33
[]
[]
[Variables]
[pp]
initial_condition = 0
[]
[]
[Kernels]
[mass_conservation]
type = PorousFlowMassTimeDerivative
variable = pp
[]
[]
[DiracKernels]
[pump]
type = PorousFlowPointSourceFromPostprocessor
mass_flux = flux
point = '0.5 0 0'
variable = pp
[]
[]
[AuxVariables]
[sat]
family = MONOMIAL
order = CONSTANT
[]
[relperm]
family = MONOMIAL
order = CONSTANT
[]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[sat]
type = PorousFlowPropertyAux
variable = sat
property = saturation
[]
[relperm]
type = PorousFlowPropertyAux
variable = relperm
property = relperm
phase = 0
[]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[temperature]
type = PorousFlowTemperature
temperature = 20
[]
[massfrac]
type = PorousFlowMassFraction
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[pc_calculator]
type = PorousFlow1PhaseP
capillary_pressure = pc
porepressure = pp
[]
[hys_order_material]
type = PorousFlowHysteresisOrder
[]
[relperm_material]
type = PorousFlowHystereticRelativePermeabilityLiquid
phase = 0
S_lr = 0.1
S_gr_max = 0.2
m = 0.9
liquid_modification_range = 0.9
[]
[]
[Postprocessors]
[flux]
type = FunctionValuePostprocessor
function = 'if(t <= 5, -10, 10)'
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[sat]
type = PointValue
point = '0 0 0'
variable = sat
[]
[relperm]
type = PointValue
point = '0 0 0'
variable = relperm
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 0.5
end_time = 10
nl_abs_tol = 1E-10
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/hysteresis/2phasePP.i)
# Simple example of a 2-phase situation with hysteretic capillary pressure. Gas is added to and removed from the system in order to observe the hysteresis
# All liquid water exists in component 0
# All gas exists in component 1
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
number_fluid_phases = 2
number_fluid_components = 2
porous_flow_vars = 'pp0 pp1'
[]
[]
[Variables]
[pp0]
initial_condition = 0
[]
[pp1]
initial_condition = 1E-4
[]
[]
[Kernels]
[mass_conservation0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pp0
[]
[mass_conservation1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = pp1
[]
[]
[DiracKernels]
[pump]
type = PorousFlowPointSourceFromPostprocessor
mass_flux = flux
point = '0.5 0 0'
variable = pp1
[]
[]
[AuxVariables]
[massfrac_ph0_sp0]
initial_condition = 1
[]
[massfrac_ph1_sp0]
initial_condition = 0
[]
[sat0]
family = MONOMIAL
order = CONSTANT
[]
[sat1]
family = MONOMIAL
order = CONSTANT
[]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[sat0]
type = PorousFlowPropertyAux
variable = sat0
phase = 0
property = saturation
[]
[sat1]
type = PorousFlowPropertyAux
variable = sat1
phase = 1
property = saturation
[]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[]
[FluidProperties]
[simple_fluid] # same properties used for both phases
type = SimpleFluidProperties
bulk_modulus = 10 # so pumping does not result in excessive porepressure
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[temperature]
type = PorousFlowTemperature
temperature = 20
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 1
[]
[hys_order_material]
type = PorousFlowHysteresisOrder
[]
[pc_calculator]
type = PorousFlow2PhaseHysPP
alpha_d = 10.0
alpha_w = 7.0
n_d = 1.5
n_w = 1.9
S_l_min = 0.1
S_lr = 0.2
S_gr_max = 0.3
Pc_max = 12.0
high_ratio = 0.9
low_extension_type = quadratic
high_extension_type = power
phase0_porepressure = pp0
phase1_porepressure = pp1
[]
[]
[Postprocessors]
[flux]
type = FunctionValuePostprocessor
function = 'if(t <= 9, 10, -10)'
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[sat0]
type = PointValue
point = '0 0 0'
variable = sat0
[]
[sat1]
type = PointValue
point = '0 0 0'
variable = sat1
[]
[pp0]
type = PointValue
point = '0 0 0'
variable = pp0
[]
[pp1]
type = PointValue
point = '0 0 0'
variable = pp1
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_shift_type'
petsc_options_value = ' lu NONZERO'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 0.5
end_time = 18
nl_abs_tol = 1E-10
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/hysteresis/1phase_relperm_2.i)
# Simple example of a 1-phase situation with hysteretic relative permeability. Water is removed and added to the system in order to observe the hysteresis
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
number_fluid_phases = 1
number_fluid_components = 1
porous_flow_vars = 'pp'
[]
[pc]
type = PorousFlowCapillaryPressureVG
alpha = 10.0
m = 0.33
[]
[]
[Variables]
[pp]
initial_condition = 0
[]
[]
[Kernels]
[mass_conservation]
type = PorousFlowMassTimeDerivative
variable = pp
[]
[]
[DiracKernels]
[pump]
type = PorousFlowPointSourceFromPostprocessor
mass_flux = flux
point = '0.5 0 0'
variable = pp
[]
[]
[AuxVariables]
[sat]
family = MONOMIAL
order = CONSTANT
[]
[relperm]
family = MONOMIAL
order = CONSTANT
[]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[sat]
type = PorousFlowPropertyAux
variable = sat
property = saturation
[]
[relperm]
type = PorousFlowPropertyAux
variable = relperm
property = relperm
phase = 0
[]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[temperature]
type = PorousFlowTemperature
temperature = 20
[]
[massfrac]
type = PorousFlowMassFraction
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[pc_calculator]
type = PorousFlow1PhaseP
capillary_pressure = pc
porepressure = pp
[]
[hys_order_material]
type = PorousFlowHysteresisOrder
[]
[relperm_material]
type = PorousFlowHystereticRelativePermeabilityLiquid
phase = 0
S_lr = 0.1
S_gr_max = 0.2
m = 0.9
liquid_modification_range = 0.9
[]
[]
[Postprocessors]
[flux]
type = FunctionValuePostprocessor
function = 'if(t <= 3, -10, if(t <= 5, 10, if(t <= 13, -10, 10)))'
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[sat]
type = PointValue
point = '0 0 0'
variable = sat
[]
[relperm]
type = PointValue
point = '0 0 0'
variable = relperm
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 3
end_time = 25
nl_abs_tol = 1E-10
[]
[Outputs]
[csv]
type = CSV
sync_times = '1 2 2.75 3 4 4.5 5 5.25 6 7.5 9 12 13 13.25 13.5 13.75 14 14.25 15 16 19 22 25'
sync_only = true
[]
[]
(modules/porous_flow/test/tests/hysteresis/2phasePP_2.i)
# Simple example of a 2-phase situation with hysteretic capillary pressure. Gas is added to, removed from, and added to the system in order to observe the hysteresis
# All liquid water exists in component 0
# All gas exists in component 1
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
number_fluid_phases = 2
number_fluid_components = 2
porous_flow_vars = 'pp0 pp1'
[]
[]
[Variables]
[pp0]
initial_condition = 0
[]
[pp1]
initial_condition = 1E-4
[]
[]
[Kernels]
[mass_conservation0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pp0
[]
[mass_conservation1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = pp1
[]
[]
[DiracKernels]
[pump]
type = PorousFlowPointSourceFromPostprocessor
mass_flux = flux
point = '0.5 0 0'
variable = pp1
[]
[]
[AuxVariables]
[massfrac_ph0_sp0]
initial_condition = 1
[]
[massfrac_ph1_sp0]
initial_condition = 0
[]
[sat0]
family = MONOMIAL
order = CONSTANT
[]
[sat1]
family = MONOMIAL
order = CONSTANT
[]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[sat0]
type = PorousFlowPropertyAux
variable = sat0
phase = 0
property = saturation
[]
[sat1]
type = PorousFlowPropertyAux
variable = sat1
phase = 1
property = saturation
[]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[]
[FluidProperties]
[simple_fluid] # same properties used for both phases
type = SimpleFluidProperties
bulk_modulus = 10 # so pumping does not result in excessive porepressure
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[temperature]
type = PorousFlowTemperature
temperature = 20
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 1
[]
[hys_order_material]
type = PorousFlowHysteresisOrder
[]
[pc_calculator]
type = PorousFlow2PhaseHysPP
alpha_d = 10.0
alpha_w = 7.0
n_d = 1.5
n_w = 1.9
S_l_min = 0.1
S_lr = 0.2
S_gr_max = 0.3
Pc_max = 12.0
high_ratio = 0.9
low_extension_type = quadratic
high_extension_type = power
phase0_porepressure = pp0
phase1_porepressure = pp1
[]
[]
[Postprocessors]
[flux]
type = FunctionValuePostprocessor
function = 'if(t <= 14, 10, if(t <= 25, -10, 10))'
[]
[hys_order]
type = PointValue
point = '0 0 0'
variable = hys_order
[]
[sat0]
type = PointValue
point = '0 0 0'
variable = sat0
[]
[sat1]
type = PointValue
point = '0 0 0'
variable = sat1
[]
[pp0]
type = PointValue
point = '0 0 0'
variable = pp0
[]
[pp1]
type = PointValue
point = '0 0 0'
variable = pp1
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_shift_type'
petsc_options_value = ' lu NONZERO'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 4
end_time = 46
nl_abs_tol = 1E-10
[]
[Outputs]
csv = true
sync_times = '13 14 15 24 25 25.5 26 27 28 29'
[]