- 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
- log_extensionTrueUse a logarithmic extension for low saturation to avoid capillary pressure going to infinity. Default is true. Set to false if your capillary pressure depends on spatially-dependent variables other than saturation, as the log-extension C++ code for this case has yet to be implemented
Default:True
C++ Type:bool
Controllable:No
Description:Use a logarithmic extension for low saturation to avoid capillary pressure going to infinity. Default is true. Set to false if your capillary pressure depends on spatially-dependent variables other than saturation, as the log-extension C++ code for this case has yet to be implemented
- pc0Constant capillary pressure (Pa). Default is 0
Default:0
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Constant capillary pressure (Pa). Default is 0
- pc_max1e+09Maximum capillary pressure (Pa). Must be > 0. Default is 1e9
Default:1e+09
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Maximum capillary pressure (Pa). Must be > 0. Default is 1e9
- sat_lr0Liquid residual saturation. Must be between 0 and 1. Default is 0
Default:0
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Liquid residual saturation. Must be between 0 and 1. Default is 0
PorousFlowCapillaryPressureConst
Constant capillary pressure
This UserObject provides a constant capillary pressure This formulation is useful for testing purposes.
Input Parameters
- allow_duplicate_execution_on_initialFalseIn the case where this UserObject is depended upon by an initial condition, allow it to be executed twice during the initial setup (once before the IC and again after mesh adaptivity (if applicable).
Default:False
C++ Type:bool
Controllable:No
Description:In the case where this UserObject is depended upon by an initial condition, allow it to be executed twice during the initial setup (once before the IC and again after mesh adaptivity (if applicable).
- execution_order_group0Execution order groups are executed in increasing order (e.g., the lowest number is executed first). Note that negative group numbers may be used to execute groups before the default (0) group. Please refer to the user object documentation for ordering of user object execution within a group.
Default:0
C++ Type:int
Controllable:No
Description:Execution order groups are executed in increasing order (e.g., the lowest number is executed first). Note that negative group numbers may be used to execute groups before the default (0) group. Please refer to the user object documentation for ordering of user object execution within a group.
- force_postauxFalseForces the UserObject to be executed in POSTAUX
Default:False
C++ Type:bool
Controllable:No
Description:Forces the UserObject to be executed in POSTAUX
- force_preauxFalseForces the UserObject to be executed in PREAUX
Default:False
C++ Type:bool
Controllable:No
Description:Forces the UserObject to be executed in PREAUX
- force_preicFalseForces the UserObject to be executed in PREIC during initial setup
Default:False
C++ Type:bool
Controllable:No
Description:Forces the UserObject to be executed in PREIC during initial setup
Execution Scheduling 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.
- 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
- 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/porous_flow/test/tests/jacobian/esbc02.i)
- (modules/porous_flow/test/tests/fluidstate/brineco2_fv.i)
- (modules/porous_flow/examples/thm_example/2D_c.i)
- (modules/porous_flow/test/tests/hysteresis/except16.i)
- (modules/porous_flow/test/tests/flux_limited_TVD_pflow/pffltvd_2D.i)
- (modules/porous_flow/test/tests/heat_conduction/two_phase_fv.i)
- (modules/porous_flow/test/tests/recover/theis.i)
- (modules/porous_flow/test/tests/sinks/s11_act.i)
- (modules/porous_flow/test/tests/actions/block_restricted_and_not.i)
- (modules/porous_flow/test/tests/chemistry/precipitation_2phase.i)
- (modules/porous_flow/test/tests/pressure_pulse/pressure_pulse_1d_2phasePS.i)
- (modules/porous_flow/test/tests/mass_conservation/mass05.i)
- (modules/porous_flow/test/tests/numerical_diffusion/no_action.i)
- (modules/porous_flow/test/tests/dirackernels/hfrompps.i)
- (modules/porous_flow/test/tests/fluidstate/brineco2_ic.i)
- (modules/porous_flow/test/tests/actions/addjoiner_exception.i)
- (modules/porous_flow/test/tests/numerical_diffusion/pffltvd.i)
- (modules/porous_flow/test/tests/basic_advection/2phase.i)
- (modules/porous_flow/test/tests/sinks/s11.i)
- (modules/porous_flow/test/tests/poroperm/except2.i)
- (modules/porous_flow/test/tests/basic_advection/except2.i)
- (modules/porous_flow/test/tests/jacobian/diff02.i)
- (modules/porous_flow/test/tests/jacobian/esbc01.i)
- (modules/porous_flow/test/tests/poroperm/poro_hm.i)
- (modules/porous_flow/test/tests/relperm/corey4.i)
- (modules/porous_flow/test/tests/relperm/corey1.i)
- (modules/porous_flow/test/tests/heat_advection/except1.i)
- (modules/porous_flow/test/tests/fluidstate/brineco2.i)
- (modules/porous_flow/examples/fluidflower/fluidflower.i)
- (modules/porous_flow/test/tests/relperm/vangenuchten2.i)
- (modules/porous_flow/test/tests/relperm/vangenuchten1.i)
- (modules/porous_flow/test/tests/aux_kernels/darcy_velocity_lower_except.i)
- (modules/porous_flow/test/tests/fluidstate/theis_tabulated.i)
- (modules/porous_flow/test/tests/actions/block_restricted_materials.i)
- (modules/porous_flow/test/tests/fluidstate/brineco2_hightemp.i)
- (modules/porous_flow/test/tests/jacobian/fflux15.i)
- (modules/porous_flow/test/tests/fluidstate/theis_brineco2_nonisothermal.i)
- (modules/porous_flow/test/tests/jacobian/fflux14.i)
- (modules/porous_flow/test/tests/relperm/corey2.i)
- (modules/porous_flow/test/tests/fluidstate/theis_nonisothermal.i)
- (modules/porous_flow/test/tests/flux_limited_TVD_pflow/pffltvd_2D_angle.i)
- (modules/porous_flow/test/tests/relperm/brooks_corey1.i)
- (modules/porous_flow/test/tests/actions/addjoiner.i)
- (modules/porous_flow/test/tests/aux_kernels/darcy_velocity_lower.i)
- (modules/porous_flow/test/tests/gravity/grav02e_fv.i)
- (modules/porous_flow/test/tests/fluidstate/theis.i)
- (modules/porous_flow/test/tests/fluidstate/waterncg_nonisothermal.i)
- (modules/porous_flow/test/tests/poroperm/poro_hm_func.i)
- (modules/porous_flow/examples/lava_lamp/1phase_convection.i)
- (modules/porous_flow/examples/co2_intercomparison/1Dradial/properties.i)
- (modules/porous_flow/examples/thm_example/2D.i)
- (modules/porous_flow/test/tests/pressure_pulse/pressure_pulse_1d_2comp.i)
- (modules/porous_flow/test/tests/recover/pffltvd.i)
- (modules/porous_flow/test/tests/flux_limited_TVD_pflow/pffltvd_3D.i)
- (modules/porous_flow/test/tests/pressure_pulse/pressure_pulse_1d_2phasePS_fv.i)
- (modules/porous_flow/test/tests/relperm/corey3.i)
- (modules/porous_flow/test/tests/flux_limited_TVD_pflow/pffltvd_2D_trimesh.i)
- (modules/porous_flow/examples/lava_lamp/2phase_convection.i)
- (modules/porous_flow/test/tests/dirackernels/theis3.i)
- (modules/porous_flow/test/tests/fluidstate/theis_brineco2.i)
- (modules/porous_flow/test/tests/relperm/unity.i)
- (modules/porous_flow/test/tests/heat_conduction/two_phase.i)
- (modules/porous_flow/test/tests/poroperm/poro_thm.i)
- (modules/porous_flow/test/tests/chemistry/2species_equilibrium_2phase.i)
- (modules/porous_flow/test/tests/chemistry/dissolution_limited_2phase.i)
- (modules/porous_flow/test/tests/poroperm/poro_tm.i)
- (modules/porous_flow/test/tests/fluidstate/brineco2_nonisothermal.i)
- (modules/porous_flow/test/tests/mass_conservation/mass06.i)
- (modules/porous_flow/test/tests/jacobian/basic_advection1.i)
- (modules/porous_flow/test/tests/aux_kernels/darcy_velocity_lower_2D.i)
- (modules/porous_flow/test/tests/basic_advection/except1.i)
- (modules/porous_flow/test/tests/jacobian/diff03.i)
- (modules/porous_flow/test/tests/flux_limited_TVD_pflow/pffltvd_1D_adaptivity.i)
- (modules/porous_flow/test/tests/flux_limited_TVD_pflow/pffltvd_1D.i)
- (modules/porous_flow/test/tests/sinks/s12.i)
- (modules/porous_flow/test/tests/fluidstate/brineco2_2.i)
- (modules/porous_flow/test/tests/fluidstate/waterncg.i)
- (modules/porous_flow/test/tests/fluidstate/waterncg_ic.i)
- (modules/porous_flow/test/tests/pressure_pulse/pressure_pulse_1d_2phasePS_KT.i)
- (modules/porous_flow/test/tests/basic_advection/1phase.i)
- (modules/porous_flow/test/tests/flux_limited_TVD_pflow/jacobian_01.i)
- (modules/porous_flow/test/tests/gravity/grav02e.i)
- (modules/porous_flow/test/tests/relperm/brooks_corey2.i)
- (modules/porous_flow/test/tests/poroperm/except1.i)
(modules/porous_flow/test/tests/jacobian/esbc02.i)
# Tests the Jacobian of PorousFlowEnthalpySink when pressure
[Mesh]
type = GeneratedMesh
dim = 2
[]
[GlobalParams]
PorousFlowDictator = dictator
at_nodes = true
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp temp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0.1
[]
[]
[Variables]
[pp]
initial_condition = 1
[]
[temp]
initial_condition = 2
[]
[]
[AuxVariables]
[pressure]
[]
[]
[Kernels]
[mass0]
type = TimeDerivative
variable = pp
[]
[heat_conduction]
type = TimeDerivative
variable = temp
[]
[]
[FluidProperties]
[simple_fluid]
type = IdealGasFluidProperties
[]
[]
[Materials]
[ppss]
type = PorousFlow1PhaseFullySaturated
porepressure = pp
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[temperature]
type = PorousFlowTemperature
temperature = temp
[]
[]
[BCs]
[left]
type = PorousFlowEnthalpySink
variable = temp
boundary = left
porepressure_var = pressure
T_in = 300
fp = simple_fluid
flux_function = -23
[]
[]
[Preconditioning]
[andy]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 0.1
num_steps = 1
nl_rel_tol = 1E-12
nl_abs_tol = 1E-12
petsc_options_iname = '-snes_test_err'
petsc_options_value = '1e-1'
[]
(modules/porous_flow/test/tests/fluidstate/brineco2_fv.i)
# Tests correct calculation of properties in PorousFlowBrineCO2 using FV variables
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 2
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
temperature = 30
[]
[Variables]
[pg]
type = MooseVariableFVReal
initial_condition = 20e6
[]
[z]
type = MooseVariableFVReal
initial_condition = 0.2
[]
[]
[AuxVariables]
[xnacl]
type = MooseVariableFVReal
initial_condition = 0.1
[]
[pressure_gas]
type = MooseVariableFVReal
[]
[pressure_water]
type = MooseVariableFVReal
[]
[saturation_gas]
type = MooseVariableFVReal
[]
[saturation_water]
type = MooseVariableFVReal
[]
[density_water]
type = MooseVariableFVReal
[]
[density_gas]
type = MooseVariableFVReal
[]
[viscosity_water]
type = MooseVariableFVReal
[]
[viscosity_gas]
type = MooseVariableFVReal
[]
[enthalpy_water]
type = MooseVariableFVReal
[]
[enthalpy_gas]
type = MooseVariableFVReal
[]
[internal_energy_water]
type = MooseVariableFVReal
[]
[internal_energy_gas]
type = MooseVariableFVReal
[]
[x0_water]
type = MooseVariableFVReal
[]
[x0_gas]
type = MooseVariableFVReal
[]
[x1_water]
type = MooseVariableFVReal
[]
[x1_gas]
type = MooseVariableFVReal
[]
[]
[AuxKernels]
[pressure_water]
type = ADPorousFlowPropertyAux
variable = pressure_water
property = pressure
phase = 0
execute_on = 'timestep_end'
[]
[pressure_gas]
type = ADPorousFlowPropertyAux
variable = pressure_gas
property = pressure
phase = 1
execute_on = 'timestep_end'
[]
[saturation_water]
type = ADPorousFlowPropertyAux
variable = saturation_water
property = saturation
phase = 0
execute_on = 'timestep_end'
[]
[saturation_gas]
type = ADPorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = 'timestep_end'
[]
[density_water]
type = ADPorousFlowPropertyAux
variable = density_water
property = density
phase = 0
execute_on = 'timestep_end'
[]
[density_gas]
type = ADPorousFlowPropertyAux
variable = density_gas
property = density
phase = 1
execute_on = 'timestep_end'
[]
[viscosity_water]
type = ADPorousFlowPropertyAux
variable = viscosity_water
property = viscosity
phase = 0
execute_on = 'timestep_end'
[]
[viscosity_gas]
type = ADPorousFlowPropertyAux
variable = viscosity_gas
property = viscosity
phase = 1
execute_on = 'timestep_end'
[]
[enthalpy_water]
type = ADPorousFlowPropertyAux
variable = enthalpy_water
property = enthalpy
phase = 0
execute_on = 'timestep_end'
[]
[enthalpy_gas]
type = ADPorousFlowPropertyAux
variable = enthalpy_gas
property = enthalpy
phase = 1
execute_on = 'timestep_end'
[]
[internal_energy_water]
type = ADPorousFlowPropertyAux
variable = internal_energy_water
property = internal_energy
phase = 0
execute_on = 'timestep_end'
[]
[internal_energy_gas]
type = ADPorousFlowPropertyAux
variable = internal_energy_gas
property = internal_energy
phase = 1
execute_on = 'timestep_end'
[]
[x1_water]
type = ADPorousFlowPropertyAux
variable = x1_water
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = 'timestep_end'
[]
[x1_gas]
type = ADPorousFlowPropertyAux
variable = x1_gas
property = mass_fraction
phase = 1
fluid_component = 1
execute_on = 'timestep_end'
[]
[x0_water]
type = ADPorousFlowPropertyAux
variable = x0_water
property = mass_fraction
phase = 0
fluid_component = 0
execute_on = 'timestep_end'
[]
[x0_gas]
type = ADPorousFlowPropertyAux
variable = x0_gas
property = mass_fraction
phase = 1
fluid_component = 0
execute_on = 'timestep_end'
[]
[]
[FVKernels]
[mass0]
type = FVPorousFlowMassTimeDerivative
variable = pg
fluid_component = 0
[]
[mass1]
type = FVPorousFlowMassTimeDerivative
variable = z
fluid_component = 1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pg z'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2]
type = CO2FluidProperties
[]
[brine]
type = BrineFluidProperties
[]
[]
[Materials]
[temperature]
type = ADPorousFlowTemperature
[]
[brineco2]
type = ADPorousFlowFluidState
gas_porepressure = pg
z = z
temperature_unit = Celsius
xnacl = xnacl
capillary_pressure = pc
fluid_state = fs
[]
[permeability]
type = ADPorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm0]
type = ADPorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[relperm1]
type = ADPorousFlowRelativePermeabilityCorey
n = 3
phase = 1
[]
[porosity]
type = ADPorousFlowPorosityConst
porosity = 0.1
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
dt = 1
end_time = 1
nl_abs_tol = 1e-12
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Postprocessors]
[density_water]
type = ElementIntegralVariablePostprocessor
variable = density_water
execute_on = 'timestep_end'
[]
[density_gas]
type = ElementIntegralVariablePostprocessor
variable = density_gas
execute_on = 'timestep_end'
[]
[viscosity_water]
type = ElementIntegralVariablePostprocessor
variable = viscosity_water
execute_on = 'timestep_end'
[]
[viscosity_gas]
type = ElementIntegralVariablePostprocessor
variable = viscosity_gas
execute_on = 'timestep_end'
[]
[enthalpy_water]
type = ElementIntegralVariablePostprocessor
variable = enthalpy_water
execute_on = 'timestep_end'
[]
[enthalpy_gas]
type = ElementIntegralVariablePostprocessor
variable = enthalpy_gas
execute_on = 'timestep_end'
[]
[internal_energy_water]
type = ElementIntegralVariablePostprocessor
variable = internal_energy_water
execute_on = 'timestep_end'
[]
[internal_energy_gas]
type = ElementIntegralVariablePostprocessor
variable = internal_energy_gas
execute_on = 'timestep_end'
[]
[x1_water]
type = ElementIntegralVariablePostprocessor
variable = x1_water
execute_on = 'timestep_end'
[]
[x0_water]
type = ElementIntegralVariablePostprocessor
variable = x0_water
execute_on = 'timestep_end'
[]
[x1_gas]
type = ElementIntegralVariablePostprocessor
variable = x1_gas
execute_on = 'timestep_end'
[]
[x0_gas]
type = ElementIntegralVariablePostprocessor
variable = x0_gas
execute_on = 'timestep_end'
[]
[sg]
type = ElementIntegralVariablePostprocessor
variable = saturation_gas
execute_on = 'timestep_end'
[]
[sw]
type = ElementIntegralVariablePostprocessor
variable = saturation_water
execute_on = 'timestep_end'
[]
[pwater]
type = ElementIntegralVariablePostprocessor
variable = pressure_water
execute_on = 'timestep_end'
[]
[pgas]
type = ElementIntegralVariablePostprocessor
variable = pressure_gas
execute_on = 'timestep_end'
[]
[x0mass]
type = FVPorousFlowFluidMass
fluid_component = 0
phase = '0 1'
[]
[x1mass]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = '0 1'
[]
[]
[Outputs]
csv = true
file_base = brineco2
execute_on = 'timestep_end'
perf_graph = false
[]
(modules/porous_flow/examples/thm_example/2D_c.i)
# Two phase, temperature-dependent, with mechanics and chemistry, radial with fine mesh, constant injection of cold co2 into a overburden-reservoir-underburden containing mostly water
# species=0 is water
# species=1 is co2
# phase=0 is liquid, and since massfrac_ph0_sp0 = 1, this is all water
# phase=1 is gas, and since massfrac_ph1_sp0 = 0, this is all co2
#
# The mesh used below has very high resolution, so the simulation takes a long time to complete.
# Some suggested meshes of different resolution:
# nx=50, bias_x=1.2
# nx=100, bias_x=1.1
# nx=200, bias_x=1.05
# nx=400, bias_x=1.02
# nx=1000, bias_x=1.01
# nx=2000, bias_x=1.003
[Mesh]
type = GeneratedMesh
dim = 2
nx = 2000
bias_x = 1.003
xmin = 0.1
xmax = 5000
ny = 1
ymin = 0
ymax = 11
coord_type = RZ
[]
[GlobalParams]
displacements = 'disp_r disp_z'
PorousFlowDictator = dictator
gravity = '0 0 0'
biot_coefficient = 1.0
[]
[Variables]
[pwater]
initial_condition = 18.3e6
[]
[sgas]
initial_condition = 0.0
[]
[temp]
initial_condition = 358
[]
[disp_r]
[]
[]
[AuxVariables]
[rate]
[]
[disp_z]
[]
[massfrac_ph0_sp0]
initial_condition = 1 # all H20 in phase=0
[]
[massfrac_ph1_sp0]
initial_condition = 0 # no H2O in phase=1
[]
[pgas]
family = MONOMIAL
order = FIRST
[]
[swater]
family = MONOMIAL
order = FIRST
[]
[stress_rr]
order = CONSTANT
family = MONOMIAL
[]
[stress_tt]
order = CONSTANT
family = MONOMIAL
[]
[stress_zz]
order = CONSTANT
family = MONOMIAL
[]
[mineral_conc_m3_per_m3]
family = MONOMIAL
order = CONSTANT
initial_condition = 0.1
[]
[eqm_const]
initial_condition = 0.0
[]
[porosity]
family = MONOMIAL
order = CONSTANT
[]
[]
[Kernels]
[mass_water_dot]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pwater
[]
[flux_water]
type = PorousFlowAdvectiveFlux
fluid_component = 0
use_displaced_mesh = false
variable = pwater
[]
[mass_co2_dot]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = sgas
[]
[flux_co2]
type = PorousFlowAdvectiveFlux
fluid_component = 1
use_displaced_mesh = false
variable = sgas
[]
[energy_dot]
type = PorousFlowEnergyTimeDerivative
variable = temp
[]
[advection]
type = PorousFlowHeatAdvection
use_displaced_mesh = false
variable = temp
[]
[conduction]
type = PorousFlowExponentialDecay
use_displaced_mesh = false
variable = temp
reference = 358
rate = rate
[]
[grad_stress_r]
type = StressDivergenceRZTensors
temperature = temp
eigenstrain_names = thermal_contribution
variable = disp_r
use_displaced_mesh = false
component = 0
[]
[poro_r]
type = PorousFlowEffectiveStressCoupling
variable = disp_r
use_displaced_mesh = false
component = 0
[]
[]
[AuxKernels]
[rate]
type = FunctionAux
variable = rate
execute_on = timestep_begin
function = decay_rate
[]
[pgas]
type = PorousFlowPropertyAux
property = pressure
phase = 1
variable = pgas
[]
[swater]
type = PorousFlowPropertyAux
property = saturation
phase = 0
variable = swater
[]
[stress_rr]
type = RankTwoAux
rank_two_tensor = stress
variable = stress_rr
index_i = 0
index_j = 0
[]
[stress_tt]
type = RankTwoAux
rank_two_tensor = stress
variable = stress_tt
index_i = 2
index_j = 2
[]
[stress_zz]
type = RankTwoAux
rank_two_tensor = stress
variable = stress_zz
index_i = 1
index_j = 1
[]
[mineral]
type = PorousFlowPropertyAux
property = mineral_concentration
mineral_species = 0
variable = mineral_conc_m3_per_m3
[]
[eqm_const_auxk]
type = ParsedAux
variable = eqm_const
coupled_variables = temp
expression = '(358 - temp) / (358 - 294)'
[]
[porosity_auxk]
type = PorousFlowPropertyAux
property = porosity
variable = porosity
[]
[]
[Functions]
[decay_rate]
# Eqn(26) of the first paper of LaForce et al.
# Ka * (rho C)_a = 10056886.914
# h = 11
type = ParsedFunction
expression = 'sqrt(10056886.914/t)/11.0'
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'temp pwater sgas disp_r'
number_fluid_phases = 2
number_fluid_components = 2
number_aqueous_kinetic = 1
aqueous_phase_number = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[FluidProperties]
[water]
type = SimpleFluidProperties
bulk_modulus = 2.27e14
density0 = 970.0
viscosity = 0.3394e-3
cv = 4149.0
cp = 4149.0
porepressure_coefficient = 0.0
thermal_expansion = 0
[]
[co2]
type = SimpleFluidProperties
bulk_modulus = 2.27e14
density0 = 516.48
viscosity = 0.0393e-3
cv = 2920.5
cp = 2920.5
porepressure_coefficient = 0.0
thermal_expansion = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = temp
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = pwater
phase1_saturation = sgas
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[water]
type = PorousFlowSingleComponentFluid
fp = water
phase = 0
[]
[gas]
type = PorousFlowSingleComponentFluid
fp = co2
phase = 1
[]
[porosity_reservoir]
type = PorousFlowPorosity
porosity_zero = 0.2
chemical = true
reference_chemistry = 0.1
initial_mineral_concentrations = 0.1
[]
[permeability_reservoir]
type = PorousFlowPermeabilityConst
permeability = '2e-12 0 0 0 0 0 0 0 0'
[]
[relperm_liquid]
type = PorousFlowRelativePermeabilityCorey
n = 4
phase = 0
s_res = 0.200
sum_s_res = 0.405
[]
[relperm_gas]
type = PorousFlowRelativePermeabilityBC
phase = 1
s_res = 0.205
sum_s_res = 0.405
nw_phase = true
lambda = 2
[]
[thermal_conductivity_reservoir]
type = PorousFlowThermalConductivityIdeal
dry_thermal_conductivity = '0 0 0 0 1.320 0 0 0 0'
wet_thermal_conductivity = '0 0 0 0 3.083 0 0 0 0'
[]
[internal_energy_reservoir]
type = PorousFlowMatrixInternalEnergy
specific_heat_capacity = 1100
density = 2350.0
[]
[elasticity_tensor]
type = ComputeIsotropicElasticityTensor
shear_modulus = 6.0E9
poissons_ratio = 0.2
[]
[strain]
type = ComputeAxisymmetricRZSmallStrain
eigenstrain_names = 'thermal_contribution ini_stress'
[]
[ini_strain]
type = ComputeEigenstrainFromInitialStress
initial_stress = '-12.8E6 0 0 0 -51.3E6 0 0 0 -12.8E6'
eigenstrain_name = ini_stress
[]
[thermal_contribution]
type = ComputeThermalExpansionEigenstrain
temperature = temp
stress_free_temperature = 358
thermal_expansion_coeff = 5E-6
eigenstrain_name = thermal_contribution
[]
[stress]
type = ComputeLinearElasticStress
[]
[eff_fluid_pressure]
type = PorousFlowEffectiveFluidPressure
[]
[vol_strain]
type = PorousFlowVolumetricStrain
[]
[predis]
type = PorousFlowAqueousPreDisChemistry
num_reactions = 1
primary_concentrations = 1.0 # fixed activity
equilibrium_constants_as_log10 = true
equilibrium_constants = eqm_const
primary_activity_coefficients = 1.0 # fixed activity
reactions = 1
kinetic_rate_constant = 1E-6
molar_volume = 1.0
specific_reactive_surface_area = 1.0
activation_energy = 0.0 # no Arrhenius
[]
[mineral_conc]
type = PorousFlowAqueousPreDisMineral
initial_concentrations = 0.1
[]
[predis_nodes]
type = PorousFlowAqueousPreDisChemistry
at_nodes = true
num_reactions = 1
primary_concentrations = 1.0 # fixed activity
equilibrium_constants_as_log10 = true
equilibrium_constants = eqm_const
primary_activity_coefficients = 1.0 # fixed activity
reactions = 1
kinetic_rate_constant = 1E-6
molar_volume = 1.0
specific_reactive_surface_area = 1.0
activation_energy = 0.0 # no Arrhenius
[]
[mineral_conc_nodes]
type = PorousFlowAqueousPreDisMineral
at_nodes = true
initial_concentrations = 0.1
[]
[]
[BCs]
[outer_pressure_fixed]
type = DirichletBC
boundary = right
value = 18.3e6
variable = pwater
[]
[outer_saturation_fixed]
type = DirichletBC
boundary = right
value = 0.0
variable = sgas
[]
[outer_temp_fixed]
type = DirichletBC
boundary = right
value = 358
variable = temp
[]
[fixed_outer_r]
type = DirichletBC
variable = disp_r
value = 0
boundary = right
[]
[co2_injection]
type = PorousFlowSink
boundary = left
variable = sgas
use_mobility = false
use_relperm = false
fluid_phase = 1
flux_function = 'min(t/100.0,1)*(-2.294001475)' # 5.0E5 T/year = 15.855 kg/s, over area of 2Pi*0.1*11
[]
[cold_co2]
type = DirichletBC
boundary = left
variable = temp
value = 294
[]
[cavity_pressure_x]
type = Pressure
boundary = left
variable = disp_r
component = 0
postprocessor = p_bh # note, this lags
use_displaced_mesh = false
[]
[]
[Postprocessors]
[p_bh]
type = PointValue
variable = pwater
point = '0.1 0 0'
execute_on = timestep_begin
use_displaced_mesh = false
[]
[mineral_bh] # mineral concentration (m^3(mineral)/m^3(rock)) at the borehole
type = PointValue
variable = mineral_conc_m3_per_m3
point = '0.1 0 0'
use_displaced_mesh = false
[]
[]
[VectorPostprocessors]
[ptsuss]
type = LineValueSampler
use_displaced_mesh = false
start_point = '0.1 0 0'
end_point = '5000 0 0'
sort_by = x
num_points = 50000
outputs = csv
variable = 'pwater temp sgas disp_r stress_rr stress_tt mineral_conc_m3_per_m3 porosity'
[]
[]
[Preconditioning]
active = 'smp'
[smp]
type = SMP
full = true
#petsc_options = '-snes_converged_reason -ksp_diagonal_scale -ksp_diagonal_scale_fix -ksp_gmres_modifiedgramschmidt -snes_linesearch_monitor'
petsc_options_iname = '-ksp_type -pc_type -sub_pc_type -sub_pc_factor_shift_type -pc_asm_overlap -snes_atol -snes_rtol -snes_max_it'
petsc_options_value = 'gmres asm lu NONZERO 2 1E2 1E-5 50'
[]
[mumps]
type = SMP
full = true
petsc_options = '-snes_converged_reason -ksp_diagonal_scale -ksp_diagonal_scale_fix -ksp_gmres_modifiedgramschmidt -snes_linesearch_monitor'
petsc_options_iname = '-ksp_type -pc_type -pc_factor_mat_solver_package -pc_factor_shift_type -snes_rtol -snes_atol -snes_max_it'
petsc_options_value = 'gmres lu mumps NONZERO 1E-5 1E2 50'
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
end_time = 1.5768e8
#dtmax = 1e6
[TimeStepper]
type = IterationAdaptiveDT
dt = 1
growth_factor = 1.1
[]
[]
[Outputs]
print_linear_residuals = false
sync_times = '3600 86400 2.592E6 1.5768E8'
perf_graph = true
exodus = true
[csv]
type = CSV
sync_only = true
[]
[]
(modules/porous_flow/test/tests/hysteresis/except16.i)
# Exception test: S_gr_max is too large
[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 = PorousFlowCapillaryPressureConst
[]
[]
[Variables]
[pp]
[]
[]
[Kernels]
[mass_conservation]
type = PorousFlowMassTimeDerivative
variable = pp
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[temperature]
type = PorousFlowTemperature
[]
[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 = 0.9
m = 0.9
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 1
[]
[AuxVariables]
[hys_order]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[hys_order]
type = PorousFlowPropertyAux
variable = hys_order
property = hysteresis_order
[]
[]
(modules/porous_flow/test/tests/flux_limited_TVD_pflow/pffltvd_2D.i)
# Using flux-limited TVD advection ala Kuzmin and Turek, employing PorousFlow Kernels and UserObjects, with superbee flux-limiter
# 3D version
[Mesh]
type = GeneratedMesh
dim = 2
nx = 10
xmin = 0
xmax = 1
ny = 4
ymin = 0
ymax = 0.5
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[porepressure]
[]
[tracer]
[]
[]
[ICs]
[porepressure]
type = FunctionIC
variable = porepressure
function = '1 - x'
[]
[tracer]
type = FunctionIC
variable = tracer
function = 'if(x<0.1,0,if(x>0.3,0,1))'
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = tracer
[]
[flux0]
type = PorousFlowFluxLimitedTVDAdvection
variable = tracer
advective_flux_calculator = advective_flux_calculator_0
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = porepressure
[]
[flux1]
type = PorousFlowFluxLimitedTVDAdvection
variable = porepressure
advective_flux_calculator = advective_flux_calculator_1
[]
[]
[BCs]
[constant_injection_porepressure]
type = DirichletBC
variable = porepressure
value = 1
boundary = left
[]
[no_tracer_on_left]
type = DirichletBC
variable = tracer
value = 0
boundary = left
[]
[remove_component_1]
type = PorousFlowPiecewiseLinearSink
variable = porepressure
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 1
use_mobility = true
flux_function = 1E3
[]
[remove_component_0]
type = PorousFlowPiecewiseLinearSink
variable = tracer
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 0
use_mobility = true
flux_function = 1E3
[]
[]
[FluidProperties]
[the_simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2E9
thermal_expansion = 0
viscosity = 1.0
density0 = 1000.0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure tracer'
number_fluid_phases = 1
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[advective_flux_calculator_0]
type = PorousFlowAdvectiveFluxCalculatorSaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 0
[]
[advective_flux_calculator_1]
type = PorousFlowAdvectiveFluxCalculatorSaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 1
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = tracer
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = the_simple_fluid
phase = 0
[]
[relperm]
type = PorousFlowRelativePermeabilityConst
phase = 0
[]
[porosity]
type = PorousFlowPorosity
porosity_zero = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1E-2 0 0 0 1E-2 0 0 0 1E-2'
[]
[]
[Preconditioning]
active = basic
[basic]
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 lu NONZERO 2'
[]
[preferred_but_might_not_be_installed]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_mat_solver_package'
petsc_options_value = ' lu mumps'
[]
[]
[VectorPostprocessors]
[tracer]
type = LineValueSampler
start_point = '0 0 0'
end_point = '1 0.5 0'
num_points = 11
sort_by = x
variable = tracer
[]
[]
[Executioner]
type = Transient
solve_type = Newton
end_time = 6
dt = 6E-2
nl_abs_tol = 1E-8
timestep_tolerance = 1E-3
[]
[Outputs]
[out]
type = CSV
execute_on = final
[]
[]
(modules/porous_flow/test/tests/heat_conduction/two_phase_fv.i)
# 2 phase heat conduction, with saturation fixed at 0.5
# Apply a boundary condition of T=300 to a bar that
# is initially at T=200, and observe the expected
# error-function response
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
nx = 10
xmin = 0
xmax = 100
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[phase0_porepressure]
type = MooseVariableFVReal
initial_condition = 0
[]
[phase1_saturation]
type = MooseVariableFVReal
initial_condition = 0.5
[]
[temp]
type = MooseVariableFVReal
initial_condition = 200
[]
[]
[FVKernels]
[dummy_p0]
type = FVTimeKernel
variable = phase0_porepressure
[]
[dummy_s1]
type = FVTimeKernel
variable = phase1_saturation
[]
[energy_dot]
type = FVPorousFlowEnergyTimeDerivative
variable = temp
[]
[heat_conduction]
type = FVPorousFlowHeatConduction
variable = temp
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'temp phase0_porepressure phase1_saturation'
number_fluid_phases = 2
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[FluidProperties]
[simple_fluid0]
type = SimpleFluidProperties
bulk_modulus = 1.5
density0 = 0.4
thermal_expansion = 0
cv = 1
[]
[simple_fluid1]
type = SimpleFluidProperties
bulk_modulus = 0.5
density0 = 0.3
thermal_expansion = 0
cv = 2
[]
[]
[Materials]
[temperature]
type = ADPorousFlowTemperature
temperature = temp
[]
[thermal_conductivity]
type = ADPorousFlowThermalConductivityIdeal
dry_thermal_conductivity = '0.3 0 0 0 0 0 0 0 0'
wet_thermal_conductivity = '1.7 0 0 0 0 0 0 0 0'
exponent = 1.0
aqueous_phase_number = 1
[]
[ppss]
type = ADPorousFlow2PhasePS
phase0_porepressure = phase0_porepressure
phase1_saturation = phase1_saturation
capillary_pressure = pc
[]
[porosity]
type = ADPorousFlowPorosityConst
porosity = 0.8
[]
[rock_heat]
type = ADPorousFlowMatrixInternalEnergy
specific_heat_capacity = 1.0
density = 0.25
[]
[simple_fluid0]
type = ADPorousFlowSingleComponentFluid
fp = simple_fluid0
phase = 0
[]
[simple_fluid1]
type = ADPorousFlowSingleComponentFluid
fp = simple_fluid1
phase = 1
[]
[]
[FVBCs]
[left]
type = FVDirichletBC
boundary = left
value = 300
variable = temp
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1E1
end_time = 1E2
[]
[Postprocessors]
[t005]
type = PointValue
variable = temp
point = '5 0 0'
execute_on = 'initial timestep_end'
[]
[t015]
type = PointValue
variable = temp
point = '15 0 0'
execute_on = 'initial timestep_end'
[]
[t025]
type = PointValue
variable = temp
point = '25 0 0'
execute_on = 'initial timestep_end'
[]
[t035]
type = PointValue
variable = temp
point = '35 0 0'
execute_on = 'initial timestep_end'
[]
[t045]
type = PointValue
variable = temp
point = '45 0 0'
execute_on = 'initial timestep_end'
[]
[t055]
type = PointValue
variable = temp
point = '55 0 0'
execute_on = 'initial timestep_end'
[]
[t065]
type = PointValue
variable = temp
point = '65 0 0'
execute_on = 'initial timestep_end'
[]
[t075]
type = PointValue
variable = temp
point = '75 0 0'
execute_on = 'initial timestep_end'
[]
[t085]
type = PointValue
variable = temp
point = '85 0 0'
execute_on = 'initial timestep_end'
[]
[t095]
type = PointValue
variable = temp
point = '95 0 0'
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
file_base = two_phase_fv
csv = true
[]
(modules/porous_flow/test/tests/recover/theis.i)
# Tests that PorousFlow can successfully recover using a checkpoint file.
# This test contains stateful material properties, adaptivity and integrated
# boundary conditions with nodal-sized materials.
#
# This test file is run three times:
# 1) The full input file is run to completion
# 2) The input file is run for half the time and checkpointing is included
# 3) The input file is run in recovery using the checkpoint data
#
# The final output of test 3 is compared to the final output of test 1 to verify
# that recovery was successful.
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
nx = 20
xmax = 100
bias_x = 1.05
[]
coord_type = RZ
rz_coord_axis = Y
# To get consistent ordering of results with distributed meshes
allow_renumbering = false
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Adaptivity]
marker = marker
max_h_level = 4
[Indicators]
[front]
type = GradientJumpIndicator
variable = zi
[]
[]
[Markers]
[marker]
type = ErrorFractionMarker
indicator = front
refine = 0.8
coarsen = 0.2
[]
[]
[]
[AuxVariables]
[saturation_gas]
order = CONSTANT
family = MONOMIAL
[]
[x1]
order = CONSTANT
family = MONOMIAL
[]
[y0]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = timestep_end
[]
[x1]
type = PorousFlowPropertyAux
variable = x1
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = timestep_end
[]
[y0]
type = PorousFlowPropertyAux
variable = y0
property = mass_fraction
phase = 1
fluid_component = 0
execute_on = timestep_end
[]
[]
[Variables]
[pgas]
initial_condition = 20e6
[]
[zi]
initial_condition = 0
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pgas
[]
[flux0]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = pgas
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = zi
[]
[flux1]
type = PorousFlowAdvectiveFlux
fluid_component = 1
variable = zi
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas zi'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowWaterNCG
water_fp = water
gas_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2]
type = CO2FluidProperties
[]
[water]
type = Water97FluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = 20
[]
[waterncg]
type = PorousFlowFluidState
gas_porepressure = pgas
z = zi
temperature_unit = Celsius
capillary_pressure = pc
fluid_state = fs
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.2
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm_water]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
s_res = 0.1
sum_s_res = 0.1
[]
[relperm_gas]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 1
[]
[]
[BCs]
[aquifer]
type = PorousFlowPiecewiseLinearSink
variable = pgas
boundary = right
pt_vals = '0 1e8'
multipliers = '0 1e8'
flux_function = 1e-6
PT_shift = 20e6
[]
[]
[DiracKernels]
[source]
type = PorousFlowSquarePulsePointSource
point = '0 0 0'
mass_flux = 2
variable = zi
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
end_time = 2e2
dt = 50
[]
[VectorPostprocessors]
[line]
type = NodalValueSampler
sort_by = x
variable = 'pgas zi'
[]
[]
[Outputs]
print_linear_residuals = false
perf_graph = true
csv = true
[]
(modules/porous_flow/test/tests/sinks/s11_act.i)
# Test that using PorousFlowSinkBC we get the same answer as in s11.i
[Mesh]
type = GeneratedMesh
dim = 3
nx = 2
ny = 2
nz = 2
xmin = 0
xmax = 10
ymin = 0
ymax = 10
zmin = 0
zmax = 10
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp temp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0.1
[]
[]
[Variables]
[pp]
initial_condition = 1
[]
[temp]
initial_condition = 2
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[heat_conduction]
type = TimeDerivative
variable = temp
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 1
density0 = 10
thermal_expansion = 0
viscosity = 11
[]
[]
[Materials]
[ppss]
type = PorousFlow1PhaseFullySaturated
porepressure = pp
[]
[massfrac]
type = PorousFlowMassFraction
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.125
[]
[temperature]
type = PorousFlowTemperature
temperature = temp
[]
[]
[Modules]
[PorousFlow]
[BCs]
[left]
type = PorousFlowSinkBC
boundary = left
fluid_phase = 0
T_in = 300
fp = simple_fluid
flux_function = -1
[]
[]
[]
[]
[Preconditioning]
[andy]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 0.25
end_time = 1
nl_rel_tol = 1E-12
nl_abs_tol = 1E-12
[]
[Outputs]
file_base = s11
[exodus]
type = Exodus
execute_on = 'initial final'
[]
[]
(modules/porous_flow/test/tests/actions/block_restricted_and_not.i)
# This input file illustrates that the PorousFlow Joiners can correctly join block-restricted Materials, even when one PorousFlow material type (relative permeability and fluid properties in this case) is block-restricted for one phase and not block-restricted for another
[Mesh]
[gmg]
type = GeneratedMeshGenerator
dim = 1
nx = 10
xmin = 0
xmax = 10
[]
[block1]
type = SubdomainBoundingBoxGenerator
input = gmg
block_id = 1
bottom_left = '3 -1 -1'
top_right = '6 1 1'
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'p0 p1'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[Variables]
[p0]
[]
[p1]
[]
[]
[Kernels]
[dot0]
type = PorousFlowMassTimeDerivative
variable = p0
fluid_component = 0
[]
[dot1]
type = PorousFlowAdvectiveFlux
variable = p1
gravity = '0 0 0'
fluid_component = 1
[]
[]
[AuxVariables]
[m0]
[]
[m1]
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePP
capillary_pressure = pc
phase0_porepressure = p0
phase1_porepressure = p1
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'm0 m1'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[simple_fluid10]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 1
block = 0
[]
[simple_fluid11]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 1
block = 1
[]
[porosity0]
type = PorousFlowPorosityConst
porosity = 0.1
block = 0
[]
[porosity1]
type = PorousFlowPorosityConst
porosity = 0.1
block = 1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '0 0 0 0 0 0 0 0 0'
[]
[relperm00]
type = PorousFlowRelativePermeabilityConst
phase = 0
block = 0
[]
[relperm01]
type = PorousFlowRelativePermeabilityConst
phase = 0
block = 1
[]
[relperm1_nonblockrestricted]
type = PorousFlowRelativePermeabilityConst
phase = 1
[]
[]
[Preconditioning]
[andy]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 1
[]
(modules/porous_flow/test/tests/chemistry/precipitation_2phase.i)
# Using a two-phase system (see precipitation.i for the single-phase)
# The saturation and porosity are chosen so that the results are identical to precipitation.i
#
# The precipitation reaction
#
# a <==> mineral
#
# produces "mineral". Using mineral_density = fluid_density, theta = 1 = eta, the DE is
#
# a' = -(mineral / (porosity * saturation))' = rate * surf_area * molar_vol (1 - (1 / eqm_const) * (act_coeff * a)^stoi)
#
# The following parameters are used
#
# T_ref = 0.5 K
# T = 1 K
# activation_energy = 3 J/mol
# gas_constant = 6 J/(mol K)
# kinetic_rate_at_ref_T = 0.60653 mol/(m^2 s)
# These give rate = 0.60653 * exp(1/2) = 1 mol/(m^2 s)
#
# surf_area = 0.5 m^2/L
# molar_volume = 2 L/mol
# These give rate * surf_area * molar_vol = 1 s^-1
#
# equilibrium_constant = 0.5 (dimensionless)
# primary_activity_coefficient = 2 (dimensionless)
# stoichiometry = 1 (dimensionless)
# This means that 1 - (1 / eqm_const) * (act_coeff * a)^stoi = 1 - 4 a, which is negative for a > 0.25, ie precipitation for a(t=0) > 0.25
#
# The solution of the DE is
# a = eqm_const / act_coeff + (a(t=0) - eqm_const / act_coeff) exp(-rate * surf_area * molar_vol * act_coeff * t / eqm_const)
# = 0.25 + (a(t=0) - 0.25) exp(-4 * t)
# c = c(t=0) - (a - a(t=0)) * (porosity * saturation)
#
# This test checks that (a + c / (porosity * saturation)) is time-independent, and that a follows the above solution
#
# Aside:
# The exponential curve is not followed exactly because moose actually solves
# (a - a_old)/dt = rate * surf_area * molar_vol (1 - (1 / eqm_const) * (act_coeff * a)^stoi)
# which does not give an exponential exactly, except in the limit dt->0
[Mesh]
type = GeneratedMesh
dim = 1
[]
[Variables]
[a]
initial_condition = 0.9
[]
[]
[AuxVariables]
[eqm_k]
initial_condition = 0.5
[]
[pressure0]
[]
[saturation1]
initial_condition = 0.25
[]
[b]
initial_condition = 0.123
[]
[ini_mineral_conc]
initial_condition = 0.2
[]
[mineral]
family = MONOMIAL
order = CONSTANT
[]
[should_be_static]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[mineral]
type = PorousFlowPropertyAux
property = mineral_concentration
mineral_species = 0
variable = mineral
[]
[should_be_static]
type = ParsedAux
coupled_variables = 'mineral a'
expression = 'a + mineral / 0.1'
variable = should_be_static
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Kernels]
[mass_a]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = a
[]
[pre_dis]
type = PorousFlowPreDis
variable = a
mineral_density = 1000
stoichiometry = 1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = a
number_fluid_phases = 2
number_fluid_components = 2
number_aqueous_kinetic = 1
aqueous_phase_number = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2e9 # huge, so mimic chemical_reactions
density0 = 1000
thermal_expansion = 0
viscosity = 1e-3
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = 1
[]
[ppss]
type = PorousFlow2PhasePS
capillary_pressure = pc
phase0_porepressure = pressure0
phase1_saturation = saturation1
[]
[mass_frac]
type = PorousFlowMassFraction
mass_fraction_vars = 'b a'
[]
[predis]
type = PorousFlowAqueousPreDisChemistry
primary_concentrations = a
num_reactions = 1
equilibrium_constants = eqm_k
primary_activity_coefficients = 2
reactions = 1
specific_reactive_surface_area = 0.5
kinetic_rate_constant = 0.6065306597126334
activation_energy = 3
molar_volume = 2
gas_constant = 6
reference_temperature = 0.5
[]
[mineral_conc]
type = PorousFlowAqueousPreDisMineral
initial_concentrations = ini_mineral_conc
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.4
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
nl_abs_tol = 1E-10
dt = 0.01
end_time = 1
[]
[Postprocessors]
[a]
type = PointValue
point = '0 0 0'
variable = a
[]
[should_be_static]
type = PointValue
point = '0 0 0'
variable = should_be_static
[]
[]
[Outputs]
time_step_interval = 10
csv = true
perf_graph = true
[]
(modules/porous_flow/test/tests/pressure_pulse/pressure_pulse_1d_2phasePS.i)
# Pressure pulse in 1D with 2 phases, 2components - transient
[Mesh]
type = GeneratedMesh
dim = 1
nx = 10
xmin = 0
xmax = 100
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[ppwater]
initial_condition = 2e6
[]
[sgas]
initial_condition = 0.3
[]
[]
[AuxVariables]
[massfrac_ph0_sp0]
family = MONOMIAL
order = FIRST
initial_condition = 1
[]
[massfrac_ph1_sp0]
family = MONOMIAL
order = FIRST
initial_condition = 0
[]
[ppgas]
family = MONOMIAL
order = FIRST
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = ppwater
[]
[flux0]
type = PorousFlowAdvectiveFlux
variable = ppwater
fluid_component = 0
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = sgas
[]
[flux1]
type = PorousFlowAdvectiveFlux
variable = sgas
fluid_component = 1
[]
[]
[AuxKernels]
[ppgas]
type = PorousFlowPropertyAux
property = pressure
phase = 1
variable = ppgas
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'ppwater sgas'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 1e5
[]
[]
[FluidProperties]
[simple_fluid0]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 1000
thermal_expansion = 0
viscosity = 1e-3
[]
[simple_fluid1]
type = SimpleFluidProperties
bulk_modulus = 2e7
density0 = 1
thermal_expansion = 0
viscosity = 1e-5
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = ppwater
phase1_saturation = sgas
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid0
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid1
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-15 0 0 0 1e-15 0 0 0 1e-15'
[]
[relperm_water]
type = PorousFlowRelativePermeabilityCorey
n = 1
phase = 0
[]
[relperm_gas]
type = PorousFlowRelativePermeabilityCorey
n = 1
phase = 1
[]
[]
[BCs]
[leftwater]
type = DirichletBC
boundary = left
value = 3e6
variable = ppwater
[]
[rightwater]
type = DirichletBC
boundary = right
value = 2e6
variable = ppwater
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-ksp_type -pc_type -snes_atol -snes_rtol -snes_max_it'
petsc_options_value = 'bcgs bjacobi 1E-15 1E-20 10000'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1e3
end_time = 1e4
[]
[VectorPostprocessors]
[pp]
type = LineValueSampler
warn_discontinuous_face_values = false
sort_by = x
variable = 'ppwater ppgas'
start_point = '0 0 0'
end_point = '100 0 0'
num_points = 11
[]
[]
[Outputs]
file_base = pressure_pulse_1d_2phasePS
print_linear_residuals = false
[csv]
type = CSV
execute_on = final
[]
[]
(modules/porous_flow/test/tests/mass_conservation/mass05.i)
# Checking that the mass postprocessor correctly calculates the mass
# of each component in each phase, as well as the total mass of each
# component in all phases.
# 2phase, 2component, constant porosity
[Mesh]
type = GeneratedMesh
dim = 1
nx = 2
xmin = 0
xmax = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pp]
[]
[sat]
[]
[]
[AuxVariables]
[massfrac_ph0_sp0]
initial_condition = 0.3
[]
[massfrac_ph1_sp0]
initial_condition = 0.55
[]
[]
[ICs]
[pinit]
type = ConstantIC
value = 1
variable = pp
[]
[satinit]
type = FunctionIC
function = 1-x
variable = sat
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = sat
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp sat'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[FluidProperties]
[simple_fluid0]
type = SimpleFluidProperties
bulk_modulus = 1
density0 = 1
thermal_expansion = 0
[]
[simple_fluid1]
type = SimpleFluidProperties
bulk_modulus = 1
density0 = 0.1
thermal_expansion = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = pp
phase1_saturation = sat
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid0
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid1
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[]
[Postprocessors]
[comp0_phase0_mass]
type = PorousFlowFluidMass
fluid_component = 0
phase = 0
[]
[comp0_phase1_mass]
type = PorousFlowFluidMass
fluid_component = 0
phase = 1
[]
[comp0_total_mass]
type = PorousFlowFluidMass
fluid_component = 0
[]
[comp0_total_mass2]
type = PorousFlowFluidMass
fluid_component = 0
phase = '0 1'
[]
[comp1_phase0_mass]
type = PorousFlowFluidMass
fluid_component = 1
phase = 0
[]
[comp1_phase1_mass]
type = PorousFlowFluidMass
fluid_component = 1
phase = 1
[]
[comp1_total_mass]
type = PorousFlowFluidMass
fluid_component = 1
[]
[comp1_total_mass2]
type = PorousFlowFluidMass
fluid_component = 1
phase = '0 1'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
nl_abs_tol = 1e-16
dt = 1
end_time = 1
[]
[Outputs]
execute_on = 'timestep_end'
file_base = mass05
csv = true
[]
(modules/porous_flow/test/tests/numerical_diffusion/no_action.i)
# Using upwinded and mass-lumped PorousFlow Kernels: this is equivalent of fully_saturated_action.i with stabilization = Full
[Mesh]
type = GeneratedMesh
dim = 1
nx = 100
xmin = 0
xmax = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[porepressure]
[]
[tracer]
[]
[]
[ICs]
[porepressure]
type = FunctionIC
variable = porepressure
function = '1 - x'
[]
[tracer]
type = FunctionIC
variable = tracer
function = 'if(x<0.1,0,if(x>0.3,0,1))'
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = tracer
[]
[flux0]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = tracer
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = porepressure
[]
[flux1]
type = PorousFlowAdvectiveFlux
fluid_component = 1
variable = porepressure
[]
[]
[BCs]
[constant_injection_porepressure]
type = DirichletBC
variable = porepressure
value = 1
boundary = left
[]
[no_tracer_on_left]
type = DirichletBC
variable = tracer
value = 0
boundary = left
[]
[remove_component_1]
type = PorousFlowPiecewiseLinearSink
variable = porepressure
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 1
use_mobility = true
flux_function = 1E3
[]
[remove_component_0]
type = PorousFlowPiecewiseLinearSink
variable = tracer
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 0
use_mobility = true
flux_function = 1E3
[]
[]
[FluidProperties]
[the_simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2E9
thermal_expansion = 0
viscosity = 1.0
density0 = 1000.0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure tracer'
number_fluid_phases = 1
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = tracer
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = the_simple_fluid
phase = 0
[]
[relperm]
type = PorousFlowRelativePermeabilityConst
phase = 0
[]
[porosity]
type = PorousFlowPorosity
porosity_zero = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1E-2 0 0 0 1E-2 0 0 0 1E-2'
[]
[]
[Preconditioning]
active = basic
[basic]
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 lu NONZERO 2'
[]
[preferred_but_might_not_be_installed]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_mat_solver_package'
petsc_options_value = ' lu mumps'
[]
[]
[VectorPostprocessors]
[tracer]
type = LineValueSampler
start_point = '0 0 0'
end_point = '1 0 0'
num_points = 101
sort_by = x
variable = tracer
[]
[]
[Executioner]
type = Transient
solve_type = Newton
end_time = 6
dt = 6E-1
nl_abs_tol = 1E-8
timestep_tolerance = 1E-3
[]
[Outputs]
[out]
type = CSV
execute_on = final
[]
[]
(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/fluidstate/brineco2_ic.i)
# Tests correct calculation of z (total mass fraction of NCG summed over all
# phases) using the PorousFlowFluidStateIC initial condition. Once z is
# calculated by the initial condition, the thermophysical properties are calculated
# and the resulting gas saturation should be equal to that given in the intial condition
[Mesh]
type = GeneratedMesh
dim = 2
[]
[GlobalParams]
PorousFlowDictator = dictator
temperature_unit = Celsius
[]
[Variables]
[pgas]
initial_condition = 1e6
[]
[z]
[]
[]
[ICs]
[z]
type = PorousFlowFluidStateIC
saturation = 0.5
gas_porepressure = pgas
temperature = 50
variable = z
xnacl = 0.1
fluid_state = fs
[]
[]
[AuxVariables]
[saturation_gas]
order = CONSTANT
family = MONOMIAL
[]
[saturation_water]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[saturation_water]
type = PorousFlowPropertyAux
variable = saturation_water
property = saturation
phase = 0
execute_on = timestep_end
[]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = timestep_end
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
variable = pgas
fluid_component = 0
[]
[mass1]
type = PorousFlowMassTimeDerivative
variable = z
fluid_component = 1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas z'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2]
type = CO2FluidProperties
[]
[brine]
type = BrineFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = 50
[]
[waterncg]
type = PorousFlowFluidState
gas_porepressure = pgas
z = z
fluid_state = fs
capillary_pressure = pc
xnacl = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm0]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[relperm1]
type = PorousFlowRelativePermeabilityCorey
n = 3
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
dt = 1
end_time = 1
nl_abs_tol = 1e-12
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Postprocessors]
[sg]
type = ElementIntegralVariablePostprocessor
variable = saturation_gas
execute_on = 'initial timestep_end'
[]
[sw]
type = ElementIntegralVariablePostprocessor
variable = saturation_water
execute_on = 'initial timestep_end'
[]
[z]
type = ElementIntegralVariablePostprocessor
variable = z
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/actions/addjoiner_exception.i)
# Tests that including a PorousFlowJoiner material throws the
# informative deprecation warning rather than a duplicate material property error
[GlobalParams]
PorousFlowDictator = dictator
[]
[Mesh]
type = GeneratedMesh
dim = 1
[]
[Variables]
[p0]
[]
[p1]
[]
[]
[Kernels]
[p0]
type = Diffusion
variable = p0
[]
[p1]
type = Diffusion
variable = p1
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
at_nodes = true
[]
[temperature_qp]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePP
at_nodes = true
phase0_porepressure = p0
phase1_porepressure = p1
capillary_pressure = pc
[]
[relperm0]
type = PorousFlowRelativePermeabilityConst
at_nodes = true
kr = 0.5
phase = 0
[]
[relperm1]
type = PorousFlowRelativePermeabilityConst
at_nodes = true
kr = 0.8
phase = 1
[]
[relperm]
type = PorousFlowJoiner
at_nodes = true
material_property = PorousFlow_relative_permeability_nodal
[]
[]
[Executioner]
type = Steady
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'p0 p1'
number_fluid_phases = 2
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
(modules/porous_flow/test/tests/numerical_diffusion/pffltvd.i)
# Using flux-limited TVD advection ala Kuzmin and Turek, employing PorousFlow Kernels and UserObjects, with superbee flux-limiter
[Mesh]
type = GeneratedMesh
dim = 1
nx = 100
xmin = 0
xmax = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[porepressure]
[]
[tracer]
[]
[]
[ICs]
[porepressure]
type = FunctionIC
variable = porepressure
function = '1 - x'
[]
[tracer]
type = FunctionIC
variable = tracer
function = 'if(x<0.1,0,if(x>0.3,0,1))'
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = tracer
[]
[flux0]
type = PorousFlowFluxLimitedTVDAdvection
variable = tracer
advective_flux_calculator = advective_flux_calculator_0
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = porepressure
[]
[flux1]
type = PorousFlowFluxLimitedTVDAdvection
variable = porepressure
advective_flux_calculator = advective_flux_calculator_1
[]
[]
[BCs]
[constant_injection_porepressure]
type = DirichletBC
variable = porepressure
value = 1
boundary = left
[]
[no_tracer_on_left]
type = DirichletBC
variable = tracer
value = 0
boundary = left
[]
[remove_component_1]
type = PorousFlowPiecewiseLinearSink
variable = porepressure
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 1
use_mobility = true
flux_function = 1E3
[]
[remove_component_0]
type = PorousFlowPiecewiseLinearSink
variable = tracer
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 0
use_mobility = true
flux_function = 1E3
[]
[]
[FluidProperties]
[the_simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2E9
thermal_expansion = 0
viscosity = 1.0
density0 = 1000.0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure tracer'
number_fluid_phases = 1
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[advective_flux_calculator_0]
type = PorousFlowAdvectiveFluxCalculatorSaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 0
[]
[advective_flux_calculator_1]
type = PorousFlowAdvectiveFluxCalculatorSaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 1
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = tracer
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = the_simple_fluid
phase = 0
[]
[relperm]
type = PorousFlowRelativePermeabilityConst
phase = 0
[]
[porosity]
type = PorousFlowPorosity
porosity_zero = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1E-2 0 0 0 1E-2 0 0 0 1E-2'
[]
[]
[Preconditioning]
active = basic
[basic]
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 lu NONZERO 2'
[]
[preferred_but_might_not_be_installed]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_mat_solver_package'
petsc_options_value = ' lu mumps'
[]
[]
[VectorPostprocessors]
[tracer]
type = LineValueSampler
start_point = '0 0 0'
end_point = '1 0 0'
num_points = 101
sort_by = x
variable = tracer
[]
[]
[Executioner]
type = Transient
solve_type = Newton
end_time = 6
dt = 6E-2
nl_abs_tol = 1E-8
timestep_tolerance = 1E-3
[]
[Outputs]
[out]
type = CSV
execute_on = final
[]
[]
(modules/porous_flow/test/tests/basic_advection/2phase.i)
# Basic advection of u in a 2-phase situation
#
# grad(P) = -2
# density * gravity = 4 * 0.25
# grad(P) - density * gravity = -3
# permeability = 10
# relative permeability = 0.5
# viscosity = 150
# so Darcy velocity = 0.1
[Mesh]
type = GeneratedMesh
dim = 1
nx = 10
xmin = 0
xmax = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[u]
[]
[]
[AuxVariables]
[P0]
[]
[P1]
[]
[]
[ICs]
[P0]
type = FunctionIC
variable = P0
function = '0'
[]
[P1]
type = FunctionIC
variable = P1
function = '2*(1-x)'
[]
[u]
type = FunctionIC
variable = u
function = 'if(x<0.1,1,0)'
[]
[]
[Kernels]
[u_dot]
type = TimeDerivative
variable = u
[]
[u_advection]
type = PorousFlowBasicAdvection
variable = u
phase = 1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = ''
number_fluid_phases = 2
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[FluidProperties]
[simple_fluid0]
type = SimpleFluidProperties
density0 = 32
viscosity = 123
[]
[simple_fluid1]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 4
thermal_expansion = 0
viscosity = 150.0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePP
phase0_porepressure = P0
phase1_porepressure = P1
capillary_pressure = pc
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid0
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid1
phase = 1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '10 0 0 0 10 0 0 0 10'
[]
[relperm0]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[relperm1]
type = PorousFlowRelativePermeabilityConst
kr = 0.5
phase = 1
[]
[darcy_velocity]
type = PorousFlowDarcyVelocityMaterial
gravity = '0.25 0 0'
[]
[]
[BCs]
[left]
type = DirichletBC
boundary = left
value = 1
variable = u
[]
[right]
type = DirichletBC
boundary = right
value = 0
variable = u
[]
[]
[Preconditioning]
[basic]
type = SMP
full = true
petsc_options_iname = '-pc_type -snes_rtol'
petsc_options_value = ' lu 1E-10'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 5
[]
[Outputs]
exodus = true
print_linear_residuals = false
[]
(modules/porous_flow/test/tests/sinks/s11.i)
# Test PorousFlowEnthalpySink boundary condition
[Mesh]
type = GeneratedMesh
dim = 3
nx = 2
ny = 2
nz = 2
xmin = 0
xmax = 10
ymin = 0
ymax = 10
zmin = 0
zmax = 10
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp temp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0.1
[]
[]
[Variables]
[pp]
initial_condition = 1
[]
[temp]
initial_condition = 2
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[heat_conduction]
type = TimeDerivative
variable = temp
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 1
density0 = 10
thermal_expansion = 0
viscosity = 11
[]
[]
[Materials]
[ppss]
type = PorousFlow1PhaseFullySaturated
porepressure = pp
[]
[massfrac]
type = PorousFlowMassFraction
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.125
[]
[temperature]
type = PorousFlowTemperature
temperature = temp
[]
[]
[BCs]
[left_p]
type = PorousFlowSink
variable = pp
boundary = left
flux_function = -1
[]
[left_T]
# Note, there is no `fluid_phase` or `porepressure_var` prescribed, since they are passed in from the `tests` file
type = PorousFlowEnthalpySink
variable = temp
boundary = left
T_in = 300
fp = simple_fluid
flux_function = -1
[]
[]
[Preconditioning]
[andy]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 0.25
end_time = 1
nl_rel_tol = 1E-12
nl_abs_tol = 1E-12
[]
[Outputs]
file_base = s11
[exodus]
type = Exodus
execute_on = 'initial final'
[]
[]
(modules/porous_flow/test/tests/poroperm/except2.i)
# Exception test: fluid=true but no solid_bulk is provided
[Mesh]
type = GeneratedMesh
dim = 3
[]
[GlobalParams]
PorousFlowDictator = dictator
displacements = 'disp_x disp_y disp_z'
biot_coefficient = 0.7
[]
[Variables]
[porepressure]
initial_condition = 2
[]
[temperature]
initial_condition = 4
[]
[disp_x]
[]
[disp_y]
[]
[disp_z]
[]
[]
[ICs]
[disp_x]
type = FunctionIC
function = '0.5 * x'
variable = disp_x
[]
[]
[Kernels]
[dummy_p]
type = TimeDerivative
variable = porepressure
[]
[dummy_t]
type = TimeDerivative
variable = temperature
[]
[dummy_x]
type = TimeDerivative
variable = disp_x
[]
[dummy_y]
type = TimeDerivative
variable = disp_y
[]
[dummy_z]
type = TimeDerivative
variable = disp_z
[]
[]
[AuxVariables]
[porosity]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[porosity]
type = PorousFlowPropertyAux
property = porosity
variable = porosity
[]
[]
[Postprocessors]
[porosity]
type = PointValue
variable = porosity
point = '0 0 0'
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure temperature'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = temperature
[]
[eff_fluid_pressure]
type = PorousFlowEffectiveFluidPressure
[]
[vol_strain]
type = PorousFlowVolumetricStrain
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[porosity]
type = PorousFlowPorosity
mechanical = true
fluid = true
thermal = true
ensure_positive = false
porosity_zero = 0.5
thermal_expansion_coeff = 0.5
reference_porepressure = 3
reference_temperature = 3.5
[]
[]
[Executioner]
solve_type = Newton
type = Transient
num_steps = 1
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/basic_advection/except2.i)
# PorousFlowDarcyVelocityMaterial attempts to have at_nodes = true
[Mesh]
type = GeneratedMesh
dim = 1
nx = 100
xmin = 0
xmax = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[u]
[]
[]
[AuxVariables]
[P]
[]
[]
[ICs]
[P]
type = FunctionIC
variable = P
function = '2*(1-x)'
[]
[u]
type = FunctionIC
variable = u
function = 'if(x<0.1,1,0)'
[]
[]
[Kernels]
[u_dot]
type = TimeDerivative
variable = u
[]
[u_advection]
type = PorousFlowBasicAdvection
variable = u
phase = 1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = ''
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 4
thermal_expansion = 0
viscosity = 150.0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = P
capillary_pressure = pc
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '5 0 0 0 5 0 0 0 5'
[]
[relperm]
type = PorousFlowRelativePermeabilityCorey
n = 0
phase = 0
[]
[darcy_velocity]
type = PorousFlowDarcyVelocityMaterial
gravity = '0.25 0 0'
at_nodes = true
[]
[]
[BCs]
[left]
type = DirichletBC
boundary = left
value = 1
variable = u
[]
[right]
type = DirichletBC
boundary = right
value = 0
variable = u
[]
[]
[Preconditioning]
[basic]
type = SMP
full = true
petsc_options_iname = '-pc_type -snes_rtol'
petsc_options_value = ' lu 1E-10'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 5
[]
[Outputs]
exodus = true
print_linear_residuals = false
[]
(modules/porous_flow/test/tests/jacobian/diff02.i)
# Test the Jacobian of the diffusive component of the PorousFlowDisperiveFlux kernel for two phases.
# By setting disp_long and disp_trans to zero, the purely diffusive component of the flux
# can be isolated. Uses constant tortuosity and diffusion coefficients
[Mesh]
type = GeneratedMesh
dim = 2
nx = 3
xmin = 0
xmax = 1
ny = 1
ymin = 0
ymax = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[sgas]
[]
[massfrac0]
[]
[]
[AuxVariables]
[massfrac1]
[]
[]
[ICs]
[sgas]
type = RandomIC
variable = sgas
max = 1
min = 0
[]
[massfrac0]
type = RandomIC
variable = massfrac0
min = 0
max = 1
[]
[massfrac1]
type = RandomIC
variable = massfrac1
min = 0
max = 1
[]
[]
[Kernels]
[diff0]
type = PorousFlowDispersiveFlux
fluid_component = 0
variable = sgas
gravity = '1 0 0'
disp_long = '0 0'
disp_trans = '0 0'
[]
[diff1]
type = PorousFlowDispersiveFlux
fluid_component = 1
variable = massfrac0
gravity = '1 0 0'
disp_long = '0 0'
disp_trans = '0 0'
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'sgas massfrac0'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[FluidProperties]
[simple_fluid0]
type = SimpleFluidProperties
bulk_modulus = 1e7
density0 = 10
thermal_expansion = 0
viscosity = 1
[]
[simple_fluid1]
type = SimpleFluidProperties
bulk_modulus = 1e7
density0 = 1
thermal_expansion = 0
viscosity = 0.1
[]
[]
[Materials]
[temp]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = 1
phase1_saturation = sgas
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac0 massfrac1'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid0
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid1
phase = 1
[]
[poro]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[diff]
type = PorousFlowDiffusivityConst
diffusion_coeff = '1e-2 1e-1 1e-2 1e-1'
tortuosity = '0.1 0.2'
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1 0 0 0 2 0 0 0 3'
[]
[relperm0]
type = PorousFlowRelativePermeabilityConst
phase = 0
[]
[relperm1]
type = PorousFlowRelativePermeabilityConst
phase = 1
[]
[]
[Preconditioning]
active = smp
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 1
[]
[Outputs]
exodus = false
[]
(modules/porous_flow/test/tests/jacobian/esbc01.i)
# Tests the Jacobian of PorousFlowEnthalpySink when pore pressure is specified
[Mesh]
type = GeneratedMesh
dim = 2
[]
[GlobalParams]
PorousFlowDictator = dictator
at_nodes = true
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp temp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0.1
[]
[]
[Variables]
[pp]
initial_condition = 1
[]
[temp]
initial_condition = 2
[]
[]
[Kernels]
[mass0]
type = TimeDerivative
variable = pp
[]
[heat_conduction]
type = TimeDerivative
variable = temp
[]
[]
[FluidProperties]
[simple_fluid]
type = IdealGasFluidProperties
[]
[]
[Materials]
[ppss]
type = PorousFlow1PhaseFullySaturated
porepressure = pp
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[temperature]
type = PorousFlowTemperature
temperature = temp
[]
[]
[BCs]
[left]
type = PorousFlowEnthalpySink
variable = temp
boundary = left
fluid_phase = 0
T_in = 300
fp = simple_fluid
flux_function = -23
[]
[]
[Preconditioning]
[andy]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 0.1
num_steps = 1
nl_rel_tol = 1E-12
nl_abs_tol = 1E-12
petsc_options_iname = '-snes_test_err'
petsc_options_value = '1e-2'
[]
(modules/porous_flow/test/tests/poroperm/poro_hm.i)
# Test that porosity is correctly calculated.
# Porosity = biot + (phi0 - biot) * exp(-vol_strain + (biot_prime - 1) / solid_bulk * (porepressure - ref_pressure))
# The parameters used are:
# biot = 0.7
# biot_prime = 0.75
# phi0 = 0.5
# vol_strain = 0.5
# solid_bulk = 0.3
# porepressure = 2
# ref_pressure = 3
# which yield porosity = 0.420877515
[Mesh]
type = GeneratedMesh
dim = 3
[]
[GlobalParams]
PorousFlowDictator = dictator
displacements = 'disp_x disp_y disp_z'
biot_coefficient = 0.7
[]
[Variables]
[porepressure]
initial_condition = 2
[]
[disp_x]
[]
[disp_y]
[]
[disp_z]
[]
[]
[ICs]
[disp_x]
type = FunctionIC
function = '0.5 * x'
variable = disp_x
[]
[]
[Kernels]
[dummy_p]
type = TimeDerivative
variable = porepressure
[]
[dummy_x]
type = TimeDerivative
variable = disp_x
[]
[dummy_y]
type = TimeDerivative
variable = disp_y
[]
[dummy_z]
type = TimeDerivative
variable = disp_z
[]
[]
[AuxVariables]
[porosity]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[porosity]
type = PorousFlowPropertyAux
property = porosity
variable = porosity
[]
[]
[Postprocessors]
[porosity]
type = PointValue
variable = porosity
point = '0 0 0'
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = 3
[]
[eff_fluid_pressure]
type = PorousFlowEffectiveFluidPressure
[]
[total_strain]
type = ComputeSmallStrain
[]
[vol_strain]
type = PorousFlowVolumetricStrain
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[porosity]
type = PorousFlowPorosity
fluid = true
mechanical = true
ensure_positive = false
porosity_zero = 0.5
solid_bulk = 0.3
reference_porepressure = 3
biot_coefficient_prime = 0.75
[]
[]
[Executioner]
solve_type = Newton
type = Transient
num_steps = 1
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/relperm/corey4.i)
# Test Corey relative permeability curve by varying saturation over the mesh
# Residual saturation of phase 0: s0r = 0.2
# Residual saturation of phase 1: s1r = 0.3
[Mesh]
type = GeneratedMesh
dim = 1
nx = 20
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[p0]
initial_condition = 1e6
[]
[s1]
family = LAGRANGE
order = FIRST
[]
[]
[AuxVariables]
[s0aux]
family = MONOMIAL
order = CONSTANT
[]
[s1aux]
family = MONOMIAL
order = CONSTANT
[]
[kr0aux]
family = MONOMIAL
order = CONSTANT
[]
[kr1aux]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[s0]
type = PorousFlowPropertyAux
property = saturation
phase = 0
variable = s0aux
[]
[s1]
type = PorousFlowPropertyAux
property = saturation
phase = 1
variable = s1aux
[]
[kr0]
type = PorousFlowPropertyAux
property = relperm
phase = 0
variable = kr0aux
[]
[kr1]
type = PorousFlowPropertyAux
property = relperm
phase = 1
variable = kr1aux
[]
[]
[Functions]
[s1]
type = ParsedFunction
expression = x
[]
[]
[ICs]
[s1]
type = FunctionIC
variable = s1
function = s1
[]
[]
[Kernels]
[p0]
type = Diffusion
variable = p0
[]
[s1]
type = Diffusion
variable = s1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'p0 s1'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = p0
phase1_saturation = s1
capillary_pressure = pc
[]
[kr0]
type = PorousFlowRelativePermeabilityCorey
scaling = 0.1
phase = 0
n = 2
s_res = 0.2
sum_s_res = 0.5
[]
[kr1]
type = PorousFlowRelativePermeabilityCorey
scaling = 10.0
phase = 1
n = 2
s_res = 0.3
sum_s_res = 0.5
[]
[]
[VectorPostprocessors]
[vpp]
type = LineValueSampler
warn_discontinuous_face_values = false
variable = 's0aux s1aux kr0aux kr1aux'
start_point = '0 0 0'
end_point = '1 0 0'
num_points = 20
sort_by = id
[]
[]
[Executioner]
type = Steady
solve_type = NEWTON
nl_abs_tol = 1e-8
[]
[BCs]
[sleft]
type = DirichletBC
variable = s1
value = 0
boundary = left
[]
[sright]
type = DirichletBC
variable = s1
value = 1
boundary = right
[]
[]
[Outputs]
csv = true
execute_on = timestep_end
[]
(modules/porous_flow/test/tests/relperm/corey1.i)
# Test Corey relative permeability curve by varying saturation over the mesh
# Corey exponent n = 1 for both phases (linear residual saturation)
# No residual saturation in either phase
[Mesh]
type = GeneratedMesh
dim = 1
nx = 20
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[p0]
initial_condition = 1e6
[]
[s1]
[]
[]
[AuxVariables]
[s0aux]
family = MONOMIAL
order = CONSTANT
[]
[s1aux]
family = MONOMIAL
order = CONSTANT
[]
[kr0aux]
family = MONOMIAL
order = CONSTANT
[]
[kr1aux]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[s0]
type = PorousFlowPropertyAux
property = saturation
phase = 0
variable = s0aux
[]
[s1]
type = PorousFlowPropertyAux
property = saturation
phase = 1
variable = s1aux
[]
[kr0]
type = PorousFlowPropertyAux
property = relperm
phase = 0
variable = kr0aux
[]
[kr1]
type = PorousFlowPropertyAux
property = relperm
phase = 1
variable = kr1aux
[]
[]
[Functions]
[s1]
type = ParsedFunction
expression = x
[]
[]
[ICs]
[s1]
type = FunctionIC
variable = s1
function = s1
[]
[]
[Kernels]
[p0]
type = Diffusion
variable = p0
[]
[s1]
type = Diffusion
variable = s1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'p0 s1'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = p0
phase1_saturation = s1
capillary_pressure = pc
[]
[kr0]
type = PorousFlowRelativePermeabilityCorey
phase = 0
n = 1
[]
[kr1]
type = PorousFlowRelativePermeabilityCorey
phase = 1
n = 1
[]
[]
[VectorPostprocessors]
[vpp]
type = LineValueSampler
warn_discontinuous_face_values = false
variable = 's0aux s1aux kr0aux kr1aux'
start_point = '0 0 0'
end_point = '1 0 0'
num_points = 20
sort_by = id
[]
[]
[Executioner]
type = Steady
solve_type = NEWTON
nl_abs_tol = 1e-8
[]
[BCs]
[sleft]
type = DirichletBC
variable = s1
value = 0
boundary = left
[]
[sright]
type = DirichletBC
variable = s1
value = 1
boundary = right
[]
[]
[Outputs]
csv = true
execute_on = timestep_end
[]
(modules/porous_flow/test/tests/heat_advection/except1.i)
# Exception testing: cannot use PorousFlowFullySaturatedUpwindHeatAdvection with != 1 phase
[Mesh]
type = GeneratedMesh
dim = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[ppwater]
[]
[ppgas]
[]
[temp]
[]
[]
[Kernels]
[dummy1]
type = Diffusion
variable = ppwater
[]
[dummy2]
type = Diffusion
variable = ppgas
[]
[advection]
type = PorousFlowFullySaturatedUpwindHeatAdvection
variable = temp
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'ppwater ppgas temp'
number_fluid_phases = 2
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = temp
[]
[ppss]
type = PorousFlow2PhasePP
phase0_porepressure = ppwater
phase1_porepressure = ppgas
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1.1 0 0 0 2 0 0 0 3'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
num_steps = 1
[]
(modules/porous_flow/test/tests/fluidstate/brineco2.i)
# Tests correct calculation of properties in PorousFlowBrineCO2
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 2
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
temperature = 30
[]
[Variables]
[pgas]
initial_condition = 20e6
[]
[z]
initial_condition = 0.2
[]
[]
[AuxVariables]
[xnacl]
initial_condition = 0.1
[]
[pressure_gas]
order = CONSTANT
family = MONOMIAL
[]
[pressure_water]
order = CONSTANT
family = MONOMIAL
[]
[saturation_gas]
order = CONSTANT
family = MONOMIAL
[]
[saturation_water]
order = CONSTANT
family = MONOMIAL
[]
[density_water]
order = CONSTANT
family = MONOMIAL
[]
[density_gas]
order = CONSTANT
family = MONOMIAL
[]
[viscosity_water]
order = CONSTANT
family = MONOMIAL
[]
[viscosity_gas]
order = CONSTANT
family = MONOMIAL
[]
[enthalpy_water]
order = CONSTANT
family = MONOMIAL
[]
[enthalpy_gas]
order = CONSTANT
family = MONOMIAL
[]
[internal_energy_water]
order = CONSTANT
family = MONOMIAL
[]
[internal_energy_gas]
order = CONSTANT
family = MONOMIAL
[]
[x0_water]
order = CONSTANT
family = MONOMIAL
[]
[x0_gas]
order = CONSTANT
family = MONOMIAL
[]
[x1_water]
order = CONSTANT
family = MONOMIAL
[]
[x1_gas]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[pressure_water]
type = PorousFlowPropertyAux
variable = pressure_water
property = pressure
phase = 0
execute_on = timestep_end
[]
[pressure_gas]
type = PorousFlowPropertyAux
variable = pressure_gas
property = pressure
phase = 1
execute_on = timestep_end
[]
[saturation_water]
type = PorousFlowPropertyAux
variable = saturation_water
property = saturation
phase = 0
execute_on = timestep_end
[]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = timestep_end
[]
[density_water]
type = PorousFlowPropertyAux
variable = density_water
property = density
phase = 0
execute_on = timestep_end
[]
[density_gas]
type = PorousFlowPropertyAux
variable = density_gas
property = density
phase = 1
execute_on = timestep_end
[]
[viscosity_water]
type = PorousFlowPropertyAux
variable = viscosity_water
property = viscosity
phase = 0
execute_on = timestep_end
[]
[viscosity_gas]
type = PorousFlowPropertyAux
variable = viscosity_gas
property = viscosity
phase = 1
execute_on = timestep_end
[]
[enthalpy_water]
type = PorousFlowPropertyAux
variable = enthalpy_water
property = enthalpy
phase = 0
execute_on = timestep_end
[]
[enthalpy_gas]
type = PorousFlowPropertyAux
variable = enthalpy_gas
property = enthalpy
phase = 1
execute_on = timestep_end
[]
[internal_energy_water]
type = PorousFlowPropertyAux
variable = internal_energy_water
property = internal_energy
phase = 0
execute_on = timestep_end
[]
[internal_energy_gas]
type = PorousFlowPropertyAux
variable = internal_energy_gas
property = internal_energy
phase = 1
execute_on = timestep_end
[]
[x1_water]
type = PorousFlowPropertyAux
variable = x1_water
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = timestep_end
[]
[x1_gas]
type = PorousFlowPropertyAux
variable = x1_gas
property = mass_fraction
phase = 1
fluid_component = 1
execute_on = timestep_end
[]
[x0_water]
type = PorousFlowPropertyAux
variable = x0_water
property = mass_fraction
phase = 0
fluid_component = 0
execute_on = timestep_end
[]
[x0_gas]
type = PorousFlowPropertyAux
variable = x0_gas
property = mass_fraction
phase = 1
fluid_component = 0
execute_on = timestep_end
[]
[]
[Kernels]
[mass0]
type = NullKernel
variable = pgas
[]
[mass1]
type = NullKernel
variable = z
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas z'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2]
type = CO2FluidProperties
[]
[brine]
type = BrineFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[brineco2]
type = PorousFlowFluidState
gas_porepressure = pgas
z = z
temperature_unit = Celsius
xnacl = xnacl
capillary_pressure = pc
fluid_state = fs
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
dt = 1
end_time = 1
nl_abs_tol = 1e-12
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Postprocessors]
[density_water]
type = ElementIntegralVariablePostprocessor
variable = density_water
[]
[density_gas]
type = ElementIntegralVariablePostprocessor
variable = density_gas
[]
[viscosity_water]
type = ElementIntegralVariablePostprocessor
variable = viscosity_water
[]
[viscosity_gas]
type = ElementIntegralVariablePostprocessor
variable = viscosity_gas
[]
[enthalpy_water]
type = ElementIntegralVariablePostprocessor
variable = enthalpy_water
[]
[enthalpy_gas]
type = ElementIntegralVariablePostprocessor
variable = enthalpy_gas
[]
[internal_energy_water]
type = ElementIntegralVariablePostprocessor
variable = internal_energy_water
[]
[internal_energy_gas]
type = ElementIntegralVariablePostprocessor
variable = internal_energy_gas
[]
[x1_water]
type = ElementIntegralVariablePostprocessor
variable = x1_water
[]
[x0_water]
type = ElementIntegralVariablePostprocessor
variable = x0_water
[]
[x1_gas]
type = ElementIntegralVariablePostprocessor
variable = x1_gas
[]
[x0_gas]
type = ElementIntegralVariablePostprocessor
variable = x0_gas
[]
[sg]
type = ElementIntegralVariablePostprocessor
variable = saturation_gas
[]
[sw]
type = ElementIntegralVariablePostprocessor
variable = saturation_water
[]
[pwater]
type = ElementIntegralVariablePostprocessor
variable = pressure_water
[]
[pgas]
type = ElementIntegralVariablePostprocessor
variable = pressure_gas
[]
[x0mass]
type = PorousFlowFluidMass
fluid_component = 0
phase = '0 1'
[]
[x1mass]
type = PorousFlowFluidMass
fluid_component = 1
phase = '0 1'
[]
[]
[Outputs]
csv = true
file_base = brineco2
execute_on = 'TIMESTEP_END'
perf_graph = false
[]
(modules/porous_flow/examples/fluidflower/fluidflower.i)
# FluidFlower International Benchmark study model
# CSIRO 2023
#
# This example can be used to reproduce the results presented by the
# CSIRO team as part of this benchmark study. See
# Green, C., Jackson, S.J., Gunning, J., Wilkins, A. and Ennis-King, J.,
# 2023. Modelling the FluidFlower: Insights from Characterisation and
# Numerical Predictions. Transport in Porous Media.
#
# This example takes a long time to run! The large density contrast
# between the gas phase CO2 and the water makes convergence very hard,
# so small timesteps must be taken during injection.
#
# This example uses a simplified mesh in order to be run during the
# automated testing. To reproduce the results of the benchmark study,
# replace the simple layered input mesh with the one located in the
# large_media submodule.
#
# The mesh file contains:
# - porosity as given by FluidFlower description
# - permeability as given by FluidFlower description
# - subdomain ids for each sand type
#
# The nominal thickness of the FluidFlower tank is 19mm. To keep masses consistent
# with the experiment, porosity and permeability are multiplied by the thickness
thickness = 0.019
#
# Properties associated with each sand type associated with mesh block ids
#
# block 0 - ESF (very fine sand)
sandESF = '0 10 20'
sandESF_pe = 1471.5
sandESF_krg = 0.09
sandESF_swi = 0.32
sandESF_krw = 0.71
sandESF_sgi = 0.14
# block 1 - C - Coarse lower
sandC = '1 21'
sandC_pe = 294.3
sandC_krg = 0.05
sandC_swi = 0.14
sandC_krw = 0.93
sandC_sgi = 0.1
# block 2 - D - Coarse upper
sandD = '2 22'
sandD_pe = 98.1
sandD_krg = 0.02
sandD_swi = 0.12
sandD_krw = 0.95
sandD_sgi = 0.08
# block 3 - E - Very Coarse lower
sandE = '3 13 23'
sandE_pe = 10
sandE_krg = 0.1
sandE_swi = 0.12
sandE_krw = 0.93
sandE_sgi = 0.06
# block 4 - F - Very Coarse upper
sandF = '4 14 24 34'
sandF_pe = 10
sandF_krg = 0.11
sandF_swi = 0.12
sandF_krw = 0.72
sandF_sgi = 0.13
# block 5 - G - Flush Zone
sandG = '5 15 35'
sandG_pe = 10
sandG_krg = 0.16
sandG_swi = 0.1
sandG_krw = 0.75
sandG_sgi = 0.06
# block 6 - Fault 1 - Heterogeneous
fault1 = '6 26'
fault1_pe = 10
fault1_krg = 0.16
fault1_swi = 0.1
fault1_krw = 0.75
fault1_sgi = 0.06
# block 7 - Fault 2 - Impermeable
# Note: this fault has been removed from the mesh (no elements in this region)
# block 8 - Fault 3 - Homogeneous
fault3 = '8'
fault3_pe = 10
fault3_krg = 0.16
fault3_swi = 0.1
fault3_krw = 0.75
fault3_sgi = 0.06
# Top layer
top_layer = '9'
# Boxes A, B an C used to report values (sg, sgr, xco2, etc)
boxA = '10 13 14 15 34 35'
boxB = '20 21 22 23 24 26'
boxC = '34 35'
# Furthermore, the seal sand unit in boxes A and B
seal_boxA = '10'
seal_boxB = '20'
# CO2 injection details:
# CO2 density ~1.8389 kg/m3 at 293.15 K, 1.01325e5 Pa
# Injection in Port (9, 3) for 5 hours.
# Injection in Port (17, 7) for 2:45 hours.
# Injection of 10 ml/min = 0.1666 ml/s = 1.666e-7 m3/s = ~3.06e-7 kg/s.
# Total mass of CO2 injected ~ 8.5g.
inj_rate = 3.06e-7
[Mesh]
[mesh]
type = FileMeshGenerator
file = 'fluidflower_test.e'
# file = '../../../../large_media/porous_flow/examples/fluidflower/fluidflower.e'
use_for_exodus_restart = true
[]
[]
[Debug]
show_var_residual_norms = true
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 -9.81 0'
temperature = temperature
log_extension = false
[]
[Variables]
[pgas]
family = MONOMIAL
order = CONSTANT
fv = true
[]
[z]
family = MONOMIAL
order = CONSTANT
fv = true
scaling = 1e4
[]
[]
[AuxVariables]
[xnacl]
family = MONOMIAL
order = CONSTANT
fv = true
initial_condition = 0.0055
[]
[temperature]
family = MONOMIAL
order = CONSTANT
fv = true
initial_condition = 20
[]
[porosity]
family = MONOMIAL
order = CONSTANT
fv = true
initial_from_file_var = porosity
[]
[porosity_times_thickness]
family = MONOMIAL
order = CONSTANT
fv = true
[]
[permeability]
family = MONOMIAL
order = CONSTANT
fv = true
initial_from_file_var = permeability
[]
[permeability_times_thickness]
family = MONOMIAL
order = CONSTANT
fv = true
[]
[saturation_water]
family = MONOMIAL
order = CONSTANT
[]
[saturation_gas]
family = MONOMIAL
order = CONSTANT
[]
[pressure_water]
family = MONOMIAL
order = CONSTANT
[]
[pc]
family = MONOMIAL
order = CONSTANT
[]
[x0_water]
order = CONSTANT
family = MONOMIAL
[]
[x0_gas]
order = CONSTANT
family = MONOMIAL
[]
[x1_water]
order = CONSTANT
family = MONOMIAL
[]
[x1_gas]
order = CONSTANT
family = MONOMIAL
[]
[density_water]
order = CONSTANT
family = MONOMIAL
[]
[density_gas]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[porosity_times_thickness]
type = ParsedAux
variable = porosity_times_thickness
coupled_variables = porosity
expression = 'porosity * ${thickness}'
execute_on = 'initial'
[]
[permeability_times_thickness]
type = ParsedAux
variable = permeability_times_thickness
coupled_variables = permeability
expression = 'permeability * ${thickness}'
execute_on = 'initial'
[]
[pressure_water]
type = ADPorousFlowPropertyAux
variable = pressure_water
property = pressure
phase = 0
execute_on = 'initial timestep_end'
[]
[saturation_water]
type = ADPorousFlowPropertyAux
variable = saturation_water
property = saturation
phase = 0
execute_on = 'initial timestep_end'
[]
[saturation_gas]
type = ADPorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = 'initial timestep_end'
[]
[density_water]
type = ADPorousFlowPropertyAux
variable = density_water
property = density
phase = 0
execute_on = 'initial timestep_end'
[]
[density_gas]
type = ADPorousFlowPropertyAux
variable = density_gas
property = density
phase = 1
execute_on = 'initial timestep_end'
[]
[x1_water]
type = ADPorousFlowPropertyAux
variable = x1_water
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = 'initial timestep_end'
[]
[x1_gas]
type = ADPorousFlowPropertyAux
variable = x1_gas
property = mass_fraction
phase = 1
fluid_component = 1
execute_on = 'initial timestep_end'
[]
[x0_water]
type = ADPorousFlowPropertyAux
variable = x0_water
property = mass_fraction
phase = 0
fluid_component = 0
execute_on = 'initial timestep_end'
[]
[x0_gas]
type = ADPorousFlowPropertyAux
variable = x0_gas
property = mass_fraction
phase = 1
fluid_component = 0
execute_on = 'initial timestep_end'
[]
[pc]
type = ADPorousFlowPropertyAux
variable = pc
property = capillary_pressure
execute_on = 'initial timestep_end'
[]
[]
[FVKernels]
[mass0]
type = FVPorousFlowMassTimeDerivative
variable = pgas
fluid_component = 0
[]
[flux0]
type = FVPorousFlowAdvectiveFlux
variable = pgas
fluid_component = 0
[]
[diff0]
type = FVPorousFlowDispersiveFlux
variable = pgas
fluid_component = 0
disp_long = '0 0'
disp_trans = '0 0'
[]
[mass1]
type = FVPorousFlowMassTimeDerivative
variable = z
fluid_component = 1
[]
[flux1]
type = FVPorousFlowAdvectiveFlux
variable = z
fluid_component = 1
[]
[diff1]
type = FVPorousFlowDispersiveFlux
variable = z
fluid_component = 1
disp_long = '0 0'
disp_trans = '0 0'
[]
[]
[DiracKernels]
[injector1]
type = ConstantPointSource
point = '0.9 0.3 0'
value = ${inj_rate}
variable = z
[]
[injector2]
type = ConstantPointSource
point = '1.7 0.7 0'
value = ${inj_rate}
variable = z
[]
[]
[Controls]
[injection1]
type = ConditionalFunctionEnableControl
enable_objects = 'DiracKernels::injector1'
conditional_function = injection_schedule1
[]
[injection2]
type = ConditionalFunctionEnableControl
enable_objects = 'DiracKernels::injector2'
conditional_function = injection_schedule2
[]
[]
[Functions]
[initial_p]
type = ParsedFunction
symbol_names = 'p0 g H rho0'
symbol_values = '101.325e3 9.81 1.5 1002'
expression = 'p0 + rho0 * g * (H - y)'
[]
[injection_schedule1]
type = ParsedFunction
expression = 'if(t >= 0 & t <= 1.8e4, 1, 0)'
[]
[injection_schedule2]
type = ParsedFunction
expression = 'if(t >= 8.1e3 & t <= 1.8e4, 1, 0)'
[]
[]
[ICs]
[p]
type = FunctionIC
variable = pgas
function = initial_p
[]
[]
[FVBCs]
[pressure_top]
type = FVPorousFlowAdvectiveFluxBC
boundary = top
porepressure_value = 1.01325e5
variable = pgas
[]
[]
[FluidProperties]
[water]
type = Water97FluidProperties
[]
[watertab]
type = TabulatedBicubicFluidProperties
fp = water
save_file = false
pressure_min = 1e5
pressure_max = 1e6
temperature_min = 290
temperature_max = 300
num_p = 20
num_T = 10
[]
[co2]
type = CO2FluidProperties
[]
[co2tab]
type = TabulatedBicubicFluidProperties
fp = co2
save_file = false
pressure_min = 1e5
pressure_max = 1e6
temperature_min = 290
temperature_max = 300
num_p = 20
num_T = 10
[]
[brine]
type = BrineFluidProperties
water_fp = watertab
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas z'
number_fluid_phases = 2
number_fluid_components = 2
[]
[sandESF_pc]
type = PorousFlowCapillaryPressureBC
pe = ${sandESF_pe}
lambda = 2
block = ${sandESF}
pc_max = 1e4
sat_lr = ${sandESF_swi}
[]
[sandC_pc]
type = PorousFlowCapillaryPressureBC
pe = ${sandC_pe}
lambda = 2
block = ${sandC}
pc_max = 1e4
sat_lr = ${sandC_swi}
[]
[sandD_pc]
type = PorousFlowCapillaryPressureBC
pe = ${sandD_pe}
lambda = 2
block = ${sandD}
pc_max = 1e4
sat_lr = ${sandD_swi}
[]
[sandE_pc]
type = PorousFlowCapillaryPressureBC
pe = ${sandE_pe}
lambda = 2
block = ${sandE}
pc_max = 1e4
sat_lr = ${sandE_swi}
[]
[sandF_pc]
type = PorousFlowCapillaryPressureBC
pe = ${sandF_pe}
lambda = 2
block = ${sandF}
pc_max = 1e4
sat_lr = ${sandF_swi}
[]
[sandG_pc]
type = PorousFlowCapillaryPressureBC
pe = ${sandG_pe}
lambda = 2
block = ${sandG}
pc_max = 1e4
sat_lr = ${sandG_swi}
[]
[fault1_pc]
type = PorousFlowCapillaryPressureBC
pe = ${fault1_pe}
lambda = 2
block = ${fault1}
pc_max = 1e4
sat_lr = ${fault1_swi}
[]
[fault3_pc]
type = PorousFlowCapillaryPressureBC
pe = ${fault3_pe}
lambda = 2
block = ${fault3}
pc_max = 1e4
sat_lr = ${fault3_swi}
[]
[top_layer_pc]
type = PorousFlowCapillaryPressureConst
pc = 0
block = ${top_layer}
[]
[sandESF_fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2tab
capillary_pressure = sandESF_pc
[]
[sandC_fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2tab
capillary_pressure = sandC_pc
[]
[sandD_fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2tab
capillary_pressure = sandD_pc
[]
[sandE_fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2tab
capillary_pressure = sandE_pc
[]
[sandF_fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2tab
capillary_pressure = sandF_pc
[]
[sandG_fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2tab
capillary_pressure = sandG_pc
[]
[fault1_fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2tab
capillary_pressure = fault1_pc
[]
[fault3_fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2tab
capillary_pressure = fault3_pc
[]
[top_layer_fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2tab
capillary_pressure = top_layer_pc
[]
[]
[Materials]
[temperature]
type = ADPorousFlowTemperature
temperature = temperature
[]
[sandESF_brineco2]
type = ADPorousFlowFluidState
gas_porepressure = pgas
z = z
temperature_unit = Celsius
xnacl = xnacl
fluid_state = sandESF_fs
capillary_pressure = sandESF_pc
block = ${sandESF}
[]
[sandC_brineco2]
type = ADPorousFlowFluidState
gas_porepressure = pgas
z = z
temperature_unit = Celsius
xnacl = xnacl
fluid_state = sandC_fs
capillary_pressure = sandC_pc
block = ${sandC}
[]
[sandD_brineco2]
type = ADPorousFlowFluidState
gas_porepressure = pgas
z = z
temperature_unit = Celsius
xnacl = xnacl
fluid_state = sandD_fs
capillary_pressure = sandD_pc
block = ${sandD}
[]
[sandE_brineco2]
type = ADPorousFlowFluidState
gas_porepressure = pgas
z = z
temperature_unit = Celsius
xnacl = xnacl
fluid_state = sandE_fs
capillary_pressure = sandE_pc
block = ${sandE}
[]
[sandF_brineco2]
type = ADPorousFlowFluidState
gas_porepressure = pgas
z = z
temperature_unit = Celsius
xnacl = xnacl
fluid_state = sandF_fs
capillary_pressure = sandF_pc
block = ${sandF}
[]
[sandG_brineco2]
type = ADPorousFlowFluidState
gas_porepressure = pgas
z = z
temperature_unit = Celsius
xnacl = xnacl
fluid_state = sandG_fs
capillary_pressure = sandG_pc
block = ${sandG}
[]
[fault1_brineco2]
type = ADPorousFlowFluidState
gas_porepressure = pgas
z = z
temperature_unit = Celsius
xnacl = xnacl
fluid_state = fault1_fs
capillary_pressure = fault1_pc
block = ${fault1}
[]
[fault3_brineco2]
type = ADPorousFlowFluidState
gas_porepressure = pgas
z = z
temperature_unit = Celsius
xnacl = xnacl
fluid_state = fault3_fs
capillary_pressure = fault3_pc
block = ${fault3}
[]
[top_layer_brineco2]
type = ADPorousFlowFluidState
gas_porepressure = pgas
z = z
temperature_unit = Celsius
xnacl = xnacl
fluid_state = top_layer_fs
capillary_pressure = top_layer_pc
block = ${top_layer}
[]
[porosity]
type = ADPorousFlowPorosityConst
porosity = porosity_times_thickness
[]
[permeability]
type = ADPorousFlowPermeabilityConstFromVar
perm_xx = permeability_times_thickness
perm_yy = permeability_times_thickness
perm_zz = permeability_times_thickness
[]
[diffcoeff]
type = ADPorousFlowDiffusivityConst
tortuosity = '1 1'
diffusion_coeff = '2e-9 2e-9 0 0'
[]
[sandESF_relperm0]
type = ADPorousFlowRelativePermeabilityBC
phase = 0
lambda = 2
s_res = ${sandESF_swi}
sum_s_res = ${fparse sandESF_sgi + sandESF_swi}
scaling = ${sandESF_krw}
block = ${sandESF}
[]
[sandESF_relperm1]
type = ADPorousFlowRelativePermeabilityBC
phase = 1
nw_phase = true
lambda = 2
s_res = ${sandESF_sgi}
sum_s_res = ${fparse sandESF_sgi + sandESF_swi}
scaling = ${sandESF_krg}
block = ${sandESF}
[]
[sandC_relperm0]
type = ADPorousFlowRelativePermeabilityBC
phase = 0
lambda = 2
s_res = ${sandC_swi}
sum_s_res = ${fparse sandC_sgi + sandC_swi}
scaling = ${sandC_krw}
block = ${sandC}
[]
[sandC_relperm1]
type = ADPorousFlowRelativePermeabilityBC
phase = 1
nw_phase = true
lambda = 2
s_res = ${sandC_sgi}
sum_s_res = ${fparse sandC_sgi + sandC_swi}
scaling = ${sandC_krg}
block = ${sandC}
[]
[sandD_relperm0]
type = ADPorousFlowRelativePermeabilityBC
phase = 0
lambda = 2
s_res = ${sandD_swi}
sum_s_res = ${fparse sandD_sgi + sandD_swi}
scaling = ${sandD_krw}
block = ${sandD}
[]
[sandD_relperm1]
type = ADPorousFlowRelativePermeabilityBC
phase = 1
nw_phase = true
lambda = 2
s_res = ${sandD_sgi}
sum_s_res = ${fparse sandD_sgi + sandD_swi}
scaling = ${sandD_krg}
block = ${sandD}
[]
[sandE_relperm0]
type = ADPorousFlowRelativePermeabilityBC
phase = 0
lambda = 2
s_res = ${sandE_swi}
sum_s_res = ${fparse sandE_sgi + sandE_swi}
scaling = ${sandE_krw}
block = ${sandE}
[]
[sandE_relperm1]
type = ADPorousFlowRelativePermeabilityBC
phase = 1
nw_phase = true
lambda = 2
s_res = ${sandE_sgi}
sum_s_res = ${fparse sandE_sgi + sandE_swi}
scaling = ${sandE_krg}
block = ${sandE}
[]
[sandF_relperm0]
type = ADPorousFlowRelativePermeabilityBC
phase = 0
lambda = 2
s_res = ${sandF_swi}
sum_s_res = ${fparse sandF_sgi + sandF_swi}
scaling = ${sandF_krw}
block = ${sandF}
[]
[sandF_relperm1]
type = ADPorousFlowRelativePermeabilityBC
phase = 1
nw_phase = true
lambda = 2
s_res = ${sandF_sgi}
sum_s_res = ${fparse sandF_sgi + sandF_swi}
scaling = ${sandF_krg}
block = ${sandF}
[]
[sandG_relperm0]
type = ADPorousFlowRelativePermeabilityBC
phase = 0
lambda = 2
s_res = ${sandG_swi}
sum_s_res = ${fparse sandG_sgi + sandG_swi}
scaling = ${sandG_krw}
block = ${sandG}
[]
[sandG_relperm1]
type = ADPorousFlowRelativePermeabilityBC
phase = 1
nw_phase = true
lambda = 2
s_res = ${sandG_sgi}
sum_s_res = ${fparse sandG_sgi + sandG_swi}
scaling = ${sandG_krg}
block = ${sandG}
[]
[fault1_relperm0]
type = ADPorousFlowRelativePermeabilityBC
phase = 0
lambda = 2
s_res = ${fault1_swi}
sum_s_res = ${fparse fault1_sgi + fault1_swi}
scaling = ${fault1_krw}
block = ${fault1}
[]
[fault1_relperm1]
type = ADPorousFlowRelativePermeabilityBC
phase = 1
nw_phase = true
lambda = 2
s_res = ${fault1_sgi}
sum_s_res = ${fparse fault1_sgi + fault1_swi}
scaling = ${fault1_krg}
block = ${fault1}
[]
[fault3_relperm0]
type = ADPorousFlowRelativePermeabilityBC
phase = 0
lambda = 2
s_res = ${fault3_swi}
sum_s_res = ${fparse fault3_sgi + fault3_swi}
scaling = ${fault3_krw}
block = ${fault3}
[]
[fault3_relperm1]
type = ADPorousFlowRelativePermeabilityBC
phase = 1
nw_phase = true
lambda = 2
s_res = ${fault3_sgi}
sum_s_res = ${fparse fault3_sgi + fault3_swi}
scaling = ${fault3_krg}
block = ${fault3}
[]
[top_layer_relperm0]
type = ADPorousFlowRelativePermeabilityBC
phase = 0
lambda = 2
block = ${top_layer}
[]
[top_layer_relperm1]
type = ADPorousFlowRelativePermeabilityBC
phase = 1
nw_phase = true
lambda = 2
block = ${top_layer}
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options = '-ksp_snes_ew'
petsc_options_iname = '-ksp_type -pc_type -pc_factor_mat_solver_package -sub_pc_factor_shift_type'
petsc_options_value = 'gmres lu mumps NONZERO'
# petsc_options_iname = '-ksp_type -pc_type -pc_hypre_type -sub_pc_type -sub_pc_factor_shift_type -sub_pc_factor_levels -ksp_gmres_restart'
# petsc_options_value = 'gmres hypre boomeramg lu NONZERO 4 301'
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
dtmax = 60
start_time = 0
end_time = 4.32e5
nl_rel_tol = 1e-6
nl_abs_tol = 1e-8
nl_max_its = 15
l_tol = 1e-5
l_abs_tol = 1e-8
# line_search = none # Can be a useful option for this problem
[TimeSteppers]
[time]
type = FunctionDT
growth_factor = 2
cutback_factor_at_failure = 0.5
function = 'if(t<1.8e4, 2, if(t<3.6e4, 20, 60))'
[]
[]
[]
[Postprocessors]
[p_5_3]
type = PointValue
variable = pgas
point = '0.5 0.3 0'
execute_on = 'initial timestep_end'
[]
[p_5_3_w]
type = PointValue
variable = pressure_water
point = '0.5 0.3 0'
execute_on = 'initial timestep_end'
[]
[p_5_7]
type = PointValue
variable = pgas
point = '0.5 0.7 0'
execute_on = 'initial timestep_end'
[]
[p_5_7_w]
type = PointValue
variable = pressure_water
point = '0.5 0.7 0'
execute_on = 'initial timestep_end'
[]
[p_9_3]
type = PointValue
variable = pgas
point = '0.9 0.3 0'
execute_on = 'initial timestep_end'
[]
[p_9_3_w]
type = PointValue
variable = pressure_water
point = '0.9 0.3 0'
execute_on = 'initial timestep_end'
[]
[p_15_5]
type = PointValue
variable = pgas
point = '1.5 0.5 0'
execute_on = 'initial timestep_end'
[]
[p_15_5_w]
type = PointValue
variable = pressure_water
point = '1.5 0.5 0'
execute_on = 'initial timestep_end'
[]
[p_17_7]
type = PointValue
variable = pgas
point = '1.7 0.7 0'
execute_on = 'initial timestep_end'
[]
[p_17_7_w]
type = PointValue
variable = pressure_water
point = '1.7 0.7 0'
execute_on = 'initial timestep_end'
[]
[p_17_11]
type = PointValue
variable = pgas
point = '1.7 1.1 0'
execute_on = 'initial timestep_end'
[]
[p_17_11_w]
type = PointValue
variable = pressure_water
point = '1.7 1.1 0'
execute_on = 'initial timestep_end'
[]
[x0mass]
type = FVPorousFlowFluidMass
fluid_component = 0
phase = '0 1'
execute_on = 'initial timestep_end'
[]
[x1mass]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = '0 1'
execute_on = 'initial timestep_end'
[]
[x1gas]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = '1'
execute_on = 'initial timestep_end'
[]
[boxA]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = '0 1'
block = ${boxA}
execute_on = 'initial timestep_end'
[]
[imm_A_sandESF]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = 1
saturation_threshold = ${sandESF_sgi}
block = 10
execute_on = 'initial timestep_end'
[]
[imm_A_sandE]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = 1
saturation_threshold = ${sandE_sgi}
block = 13
execute_on = 'initial timestep_end'
[]
[imm_A_sandF]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = 1
saturation_threshold = ${sandF_sgi}
block = '14 34'
execute_on = 'initial timestep_end'
[]
[imm_A_sandG]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = 1
saturation_threshold = ${sandG_sgi}
block = '15 35'
execute_on = 'initial timestep_end'
[]
[imm_A]
type = LinearCombinationPostprocessor
pp_names = 'imm_A_sandESF imm_A_sandE imm_A_sandF imm_A_sandG'
pp_coefs = '1 1 1 1'
execute_on = 'initial timestep_end'
[]
[diss_A]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = 0
block = ${boxA}
execute_on = 'initial timestep_end'
[]
[seal_A]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = '0 1'
block = ${seal_boxA}
execute_on = 'initial timestep_end'
[]
[boxB]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = '0 1'
block = ${boxB}
execute_on = 'initial timestep_end'
[]
[imm_B_sandESF]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = 1
saturation_threshold = ${sandESF_sgi}
block = 20
execute_on = 'initial timestep_end'
[]
[imm_B_sandC]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = 1
saturation_threshold = ${sandC_sgi}
block = 21
execute_on = 'initial timestep_end'
[]
[imm_B_sandD]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = 1
saturation_threshold = ${sandD_sgi}
block = 22
execute_on = 'initial timestep_end'
[]
[imm_B_sandE]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = 1
saturation_threshold = ${sandE_sgi}
block = 23
execute_on = 'initial timestep_end'
[]
[imm_B_sandF]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = 1
saturation_threshold = ${sandF_sgi}
block = 24
execute_on = 'initial timestep_end'
[]
[imm_B_fault1]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = 1
saturation_threshold = ${fault1_sgi}
block = 26
execute_on = 'initial timestep_end'
[]
[imm_B]
type = LinearCombinationPostprocessor
pp_names = 'imm_B_sandESF imm_B_sandC imm_B_sandD imm_B_sandE imm_B_sandF imm_B_fault1'
pp_coefs = '1 1 1 1 1 1'
execute_on = 'initial timestep_end'
[]
[diss_B]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = 0
block = ${boxB}
execute_on = 'initial timestep_end'
[]
[seal_B]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = '0 1'
block = ${seal_boxB}
execute_on = 'initial timestep_end'
[]
[boxC]
type = FVPorousFlowFluidMass
fluid_component = 1
phase = '0'
block = ${boxC}
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
print_linear_residuals = false
perf_graph = true
# exodus = true
[csv]
type = CSV
[]
[]
(modules/porous_flow/test/tests/relperm/vangenuchten2.i)
# Test van Genuchten relative permeability curve by varying saturation over the mesh
# van Genuchten exponent m = 0.4 for both phases
# Phase 0 residual saturation s0r = 0.1
# Phase 1 residual saturation s1r = 0.2
[Mesh]
type = GeneratedMesh
dim = 1
nx = 100
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[p0]
initial_condition = 1e6
[]
[s1]
[]
[]
[AuxVariables]
[s0aux]
family = MONOMIAL
order = CONSTANT
[]
[s1aux]
family = MONOMIAL
order = CONSTANT
[]
[kr0aux]
family = MONOMIAL
order = CONSTANT
[]
[kr1aux]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[s0]
type = PorousFlowPropertyAux
property = saturation
phase = 0
variable = s0aux
[]
[s1]
type = PorousFlowPropertyAux
property = saturation
phase = 1
variable = s1aux
[]
[kr0]
type = PorousFlowPropertyAux
property = relperm
phase = 0
variable = kr0aux
[]
[kr1]
type = PorousFlowPropertyAux
property = relperm
phase = 1
variable = kr1aux
[]
[]
[Functions]
[s1]
type = ParsedFunction
expression = x
[]
[]
[ICs]
[s1]
type = FunctionIC
variable = s1
function = s1
[]
[]
[Kernels]
[p0]
type = Diffusion
variable = p0
[]
[s1]
type = Diffusion
variable = s1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'p0 s1'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = p0
phase1_saturation = s1
capillary_pressure = pc
[]
[kr0]
type = PorousFlowRelativePermeabilityVG
phase = 0
m = 0.4
s_res = 0.1
sum_s_res = 0.3
[]
[kr1]
type = PorousFlowRelativePermeabilityVG
phase = 1
m = 0.4
s_res = 0.2
sum_s_res = 0.3
wetting = false
[]
[]
[VectorPostprocessors]
[vpp]
type = LineValueSampler
warn_discontinuous_face_values = false
variable = 's0aux s1aux kr0aux kr1aux'
start_point = '0 0 0'
end_point = '1 0 0'
num_points = 20
sort_by = id
[]
[]
[Executioner]
type = Steady
solve_type = NEWTON
nl_abs_tol = 1e-7
[]
[BCs]
[sleft]
type = DirichletBC
variable = s1
value = 0
boundary = left
[]
[sright]
type = DirichletBC
variable = s1
value = 1
boundary = right
[]
[]
[Outputs]
csv = true
execute_on = timestep_end
[]
(modules/porous_flow/test/tests/relperm/vangenuchten1.i)
# Test van Genuchten relative permeability curve by varying saturation over the mesh
# van Genuchten exponent m = 0.5 for both phases
# No residual saturation in either phase
[Mesh]
type = GeneratedMesh
dim = 1
nx = 100
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[p0]
initial_condition = 1e6
[]
[s1]
[]
[]
[AuxVariables]
[s0aux]
family = MONOMIAL
order = CONSTANT
[]
[s1aux]
family = MONOMIAL
order = CONSTANT
[]
[kr0aux]
family = MONOMIAL
order = CONSTANT
[]
[kr1aux]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[s0]
type = PorousFlowPropertyAux
property = saturation
phase = 0
variable = s0aux
[]
[s1]
type = PorousFlowPropertyAux
property = saturation
phase = 1
variable = s1aux
[]
[kr0]
type = PorousFlowPropertyAux
property = relperm
phase = 0
variable = kr0aux
[]
[kr1]
type = PorousFlowPropertyAux
property = relperm
phase = 1
variable = kr1aux
[]
[]
[Functions]
[s1]
type = ParsedFunction
expression = x
[]
[]
[ICs]
[s1]
type = FunctionIC
variable = s1
function = s1
[]
[]
[Kernels]
[p0]
type = Diffusion
variable = p0
[]
[s1]
type = Diffusion
variable = s1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'p0 s1'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = p0
phase1_saturation = s1
capillary_pressure = pc
[]
[kr0]
type = PorousFlowRelativePermeabilityVG
phase = 0
m = 0.5
[]
[kr1]
type = PorousFlowRelativePermeabilityVG
phase = 1
m = 0.5
wetting = false
[]
[]
[VectorPostprocessors]
[vpp]
type = LineValueSampler
warn_discontinuous_face_values = false
variable = 's0aux s1aux kr0aux kr1aux'
start_point = '0 0 0'
end_point = '1 0 0'
num_points = 20
sort_by = id
[]
[]
[Executioner]
type = Steady
solve_type = NEWTON
nl_abs_tol = 1e-7
[]
[BCs]
[sleft]
type = DirichletBC
variable = s1
value = 0
boundary = left
[]
[sright]
type = DirichletBC
variable = s1
value = 1
boundary = right
[]
[]
[Outputs]
csv = true
execute_on = timestep_end
[]
(modules/porous_flow/test/tests/aux_kernels/darcy_velocity_lower_except.i)
# Exception testing for PorousFlowDarcyVelocityComponentLowerDimensional
# Checking that an error is produced if the AuxVariable is not defined only on
# lower-dimensional elements
[Mesh]
type = FileMesh
file = fractured_block.e
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '1 0.5 0.2'
[]
[Variables]
[pp]
[]
[]
[Kernels]
[dummy]
type = TimeDerivative
variable = pp
[]
[]
[AuxVariables]
[fracture_vel_x]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[fracture_vel_x]
type = PorousFlowDarcyVelocityComponentLowerDimensional
variable = fracture_vel_x
component = x
fluid_phase = 0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 1E16
viscosity = 10
density0 = 2
thermal_expansion = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = pp
capillary_pressure = pc
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '5 0 0 0 5 0 0 0 5'
[]
[relperm]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[]
[Executioner]
type = Transient
dt = 1
end_time = 1
[]
(modules/porous_flow/test/tests/fluidstate/theis_tabulated.i)
# Two phase Theis problem: Flow from single source using WaterNCG fluidstate.
# Constant rate injection 2 kg/s
# 1D cylindrical mesh
# Initially, system has only a liquid phase, until enough gas is injected
# to form a gas phase, in which case the system becomes two phase.
# Note: this test is the same as theis.i, but uses the tabulated version of the CO2FluidProperties
[Mesh]
type = GeneratedMesh
dim = 1
nx = 80
xmax = 200
bias_x = 1.05
coord_type = RZ
rz_coord_axis = Y
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[AuxVariables]
[saturation_gas]
order = CONSTANT
family = MONOMIAL
[]
[x1]
order = CONSTANT
family = MONOMIAL
[]
[y0]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = timestep_end
[]
[x1]
type = PorousFlowPropertyAux
variable = x1
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = timestep_end
[]
[y0]
type = PorousFlowPropertyAux
variable = y0
property = mass_fraction
phase = 1
fluid_component = 0
execute_on = timestep_end
[]
[]
[Variables]
[pgas]
initial_condition = 20e6
[]
[zi]
initial_condition = 0
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pgas
[]
[flux0]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = pgas
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = zi
[]
[flux1]
type = PorousFlowAdvectiveFlux
fluid_component = 1
variable = zi
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas zi'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowWaterNCG
water_fp = water
gas_fp = tabulated
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2]
type = CO2FluidProperties
[]
[tabulated]
type = TabulatedBicubicFluidProperties
fp = co2
fluid_property_file = fluid_properties.csv
# We try to avoid using both, but some properties are not implemented in the tabulation
allow_fp_and_tabulation = true
# Test was design prior to bounds check
error_on_out_of_bounds = false
# Comment out the fp parameter and uncomment below to use the newly generated tabulation
# fluid_property_file = fluid_properties.csv
[]
[water]
type = Water97FluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = 20
[]
[waterncg]
type = PorousFlowFluidState
gas_porepressure = pgas
z = zi
temperature_unit = Celsius
capillary_pressure = pc
fluid_state = fs
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.2
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm_water]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
s_res = 0.1
sum_s_res = 0.1
[]
[relperm_gas]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 1
[]
[]
[BCs]
[rightwater]
type = DirichletBC
boundary = right
value = 20e6
variable = pgas
[]
[]
[DiracKernels]
[source]
type = PorousFlowSquarePulsePointSource
point = '0 0 0'
mass_flux = 2
variable = zi
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options = '-snes_converged_reason -ksp_diagonal_scale -ksp_diagonal_scale_fix -ksp_gmres_modifiedgramschmidt -snes_linesearch_monitor'
petsc_options_iname = '-ksp_type -pc_type -sub_pc_type -sub_pc_factor_shift_type -pc_asm_overlap -snes_atol -snes_rtol -snes_max_it'
petsc_options_value = 'gmres asm lu NONZERO 2 1E-8 1E-10 20'
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
end_time = 8e2
[TimeStepper]
type = IterationAdaptiveDT
dt = 2
growth_factor = 2
[]
[]
[VectorPostprocessors]
[line]
type = LineValueSampler
warn_discontinuous_face_values = false
sort_by = x
start_point = '0 0 0'
end_point = '200 0 0'
num_points = 1000
variable = 'pgas zi x1 saturation_gas'
execute_on = 'timestep_end'
[]
[]
[Postprocessors]
[pgas]
type = PointValue
point = '1 0 0'
variable = pgas
[]
[sgas]
type = PointValue
point = '1 0 0'
variable = saturation_gas
[]
[zi]
type = PointValue
point = '1 0 0'
variable = zi
[]
[massgas]
type = PorousFlowFluidMass
fluid_component = 1
[]
[x1]
type = PointValue
point = '1 0 0'
variable = x1
[]
[y0]
type = PointValue
point = '1 0 0'
variable = y0
[]
[]
[Outputs]
print_linear_residuals = false
perf_graph = true
[csvout]
type = CSV
file_base = theis_tabulated_csvout
execute_on = timestep_end
execute_vector_postprocessors_on = final
[]
[]
(modules/porous_flow/test/tests/actions/block_restricted_materials.i)
# Tests that the actions to automatically add PorousFlowJoiner's and the correct
# qp or nodal version of each material work as expected when a material is block
# restricted. Tests both phase dependent properties (like relative permeability)
# as well as phase-independent materials (like porosity)
[GlobalParams]
PorousFlowDictator = dictator
[]
[Mesh]
[gen]
type = GeneratedMeshGenerator
dim = 2
ny = 2
[]
[subdomain0]
input = gen
type = SubdomainBoundingBoxGenerator
bottom_left = '0 0 0'
top_right = '1 0.5 0'
block_id = 0
[]
[subdomain1]
input = subdomain0
type = SubdomainBoundingBoxGenerator
bottom_left = '0 0.5 0'
top_right = '1 1 0'
block_id = 1
[]
[]
[Variables]
[p0]
initial_condition = 1
[]
[p1]
initial_condition = 1.1
[]
[]
[AuxVariables]
[porosity]
family = MONOMIAL
order = CONSTANT
[]
[kl]
family = MONOMIAL
order = CONSTANT
[]
[kg]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[porosity]
type = PorousFlowPropertyAux
property = porosity
variable = porosity
[]
[kl]
type = PorousFlowPropertyAux
property = relperm
variable = kl
phase = 0
[]
[kg]
type = PorousFlowPropertyAux
property = relperm
variable = kg
phase = 1
[]
[]
[Kernels]
[p0]
type = PorousFlowMassTimeDerivative
variable = p0
[]
[p1]
type = PorousFlowAdvectiveFlux
gravity = '0 0 0'
variable = p1
[]
[]
[FluidProperties]
[fluid0]
type = SimpleFluidProperties
[]
[fluid1]
type = SimpleFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePP
phase0_porepressure = p0
phase1_porepressure = p1
capillary_pressure = pc
[]
[krl0]
type = PorousFlowRelativePermeabilityConst
kr = 0.7
phase = 0
block = 0
[]
[krg0]
type = PorousFlowRelativePermeabilityConst
kr = 0.8
phase = 1
block = 0
[]
[krl1]
type = PorousFlowRelativePermeabilityConst
kr = 0.5
phase = 0
block = 1
[]
[krg1]
type = PorousFlowRelativePermeabilityConst
kr = 0.4
phase = 1
block = 1
[]
[perm]
type = PorousFlowPermeabilityConst
permeability = '1 0 0 0 1 0 0 0 1'
[]
[fluid0]
type = PorousFlowSingleComponentFluid
fp = fluid0
phase = 0
[]
[fluid1]
type = PorousFlowSingleComponentFluid
fp = fluid1
phase = 1
[]
[massfrac]
type = PorousFlowMassFraction
[]
[porosity0]
type = PorousFlowPorosityConst
porosity = 0.1
block = 0
[]
[porosity1]
type = PorousFlowPorosityConst
porosity = 0.2
block = 1
[]
[]
[Executioner]
type = Transient
end_time = 1
nl_abs_tol = 1e-10
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'p0 p1'
number_fluid_phases = 2
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[Outputs]
exodus = true
[]
(modules/porous_flow/test/tests/fluidstate/brineco2_hightemp.i)
# Tests correct calculation of properties in PorousFlowBrineCO2 in the elevated
# temperature regime (T > 110C)
[Mesh]
type = GeneratedMesh
dim = 2
[]
[GlobalParams]
PorousFlowDictator = dictator
temperature = 250
[]
[Variables]
[pgas]
initial_condition = 20e6
[]
[z]
initial_condition = 0.2
[]
[]
[AuxVariables]
[xnacl]
initial_condition = 0.1
[]
[pressure_gas]
order = CONSTANT
family = MONOMIAL
[]
[pressure_water]
order = CONSTANT
family = MONOMIAL
[]
[saturation_gas]
order = CONSTANT
family = MONOMIAL
[]
[saturation_water]
order = CONSTANT
family = MONOMIAL
[]
[density_water]
order = CONSTANT
family = MONOMIAL
[]
[density_gas]
order = CONSTANT
family = MONOMIAL
[]
[viscosity_water]
order = CONSTANT
family = MONOMIAL
[]
[viscosity_gas]
order = CONSTANT
family = MONOMIAL
[]
[x0_water]
order = CONSTANT
family = MONOMIAL
[]
[x0_gas]
order = CONSTANT
family = MONOMIAL
[]
[x1_water]
order = CONSTANT
family = MONOMIAL
[]
[x1_gas]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[pressure_water]
type = PorousFlowPropertyAux
variable = pressure_water
property = pressure
phase = 0
execute_on = timestep_end
[]
[pressure_gas]
type = PorousFlowPropertyAux
variable = pressure_gas
property = pressure
phase = 1
execute_on = timestep_end
[]
[saturation_water]
type = PorousFlowPropertyAux
variable = saturation_water
property = saturation
phase = 0
execute_on = timestep_end
[]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = timestep_end
[]
[density_water]
type = PorousFlowPropertyAux
variable = density_water
property = density
phase = 0
execute_on = timestep_end
[]
[density_gas]
type = PorousFlowPropertyAux
variable = density_gas
property = density
phase = 1
execute_on = timestep_end
[]
[viscosity_water]
type = PorousFlowPropertyAux
variable = viscosity_water
property = viscosity
phase = 0
execute_on = timestep_end
[]
[viscosity_gas]
type = PorousFlowPropertyAux
variable = viscosity_gas
property = viscosity
phase = 1
execute_on = timestep_end
[]
[x1_water]
type = PorousFlowPropertyAux
variable = x1_water
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = timestep_end
[]
[x1_gas]
type = PorousFlowPropertyAux
variable = x1_gas
property = mass_fraction
phase = 1
fluid_component = 1
execute_on = timestep_end
[]
[x0_water]
type = PorousFlowPropertyAux
variable = x0_water
property = mass_fraction
phase = 0
fluid_component = 0
execute_on = timestep_end
[]
[x0_gas]
type = PorousFlowPropertyAux
variable = x0_gas
property = mass_fraction
phase = 1
fluid_component = 0
execute_on = timestep_end
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
variable = pgas
fluid_component = 0
[]
[mass1]
type = PorousFlowMassTimeDerivative
variable = z
fluid_component = 1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas z'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2]
type = CO2FluidProperties
[]
[brine]
type = BrineFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[brineco2]
type = PorousFlowFluidState
gas_porepressure = pgas
z = z
temperature_unit = Celsius
xnacl = xnacl
capillary_pressure = pc
fluid_state = fs
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm0]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[relperm1]
type = PorousFlowRelativePermeabilityCorey
n = 3
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
dt = 1
end_time = 1
nl_abs_tol = 1e-12
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Postprocessors]
[density_water]
type = ElementIntegralVariablePostprocessor
variable = density_water
[]
[density_gas]
type = ElementIntegralVariablePostprocessor
variable = density_gas
[]
[viscosity_water]
type = ElementIntegralVariablePostprocessor
variable = viscosity_water
[]
[viscosity_gas]
type = ElementIntegralVariablePostprocessor
variable = viscosity_gas
[]
[x1_water]
type = ElementIntegralVariablePostprocessor
variable = x1_water
[]
[x0_water]
type = ElementIntegralVariablePostprocessor
variable = x0_water
[]
[x1_gas]
type = ElementIntegralVariablePostprocessor
variable = x1_gas
[]
[x0_gas]
type = ElementIntegralVariablePostprocessor
variable = x0_gas
[]
[sg]
type = ElementIntegralVariablePostprocessor
variable = saturation_gas
[]
[sw]
type = ElementIntegralVariablePostprocessor
variable = saturation_water
[]
[pwater]
type = ElementIntegralVariablePostprocessor
variable = pressure_water
[]
[pgas]
type = ElementIntegralVariablePostprocessor
variable = pressure_gas
[]
[x0mass]
type = PorousFlowFluidMass
fluid_component = 0
phase = '0 1'
[]
[x1mass]
type = PorousFlowFluidMass
fluid_component = 1
phase = '0 1'
[]
[]
[Outputs]
csv = true
execute_on = 'TIMESTEP_END'
perf_graph = false
[]
(modules/porous_flow/test/tests/jacobian/fflux15.i)
# 1phase, 2components (water and tracer using BrineFluidProperties with constant salinity),
# constant insitu permeability and relative perm, nonzero gravity
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 2
nx = 1
xmin = 0
xmax = 10
ny = 1
ymin = 0
ymax = 10
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 -10 0'
[]
[Variables]
[pp]
[]
[tracer]
[]
[]
[ICs]
[pp]
type = RandomIC
variable = pp
min = 1e6
max = 2e6
[]
[tracer]
type = RandomIC
variable = tracer
min = 0.1
max = 0.2
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
variable = pp
fluid_component = 0
[]
[mass1]
type = PorousFlowMassTimeDerivative
variable = tracer
fluid_component = 1
[]
[flux0]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = pp
[]
[flux1]
type = PorousFlowAdvectiveFlux
fluid_component = 1
variable = tracer
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp tracer'
number_fluid_phases = 1
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[FluidProperties]
[brine]
type = BrineFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = pp
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'tracer'
[]
[brine]
type = PorousFlowBrine
phase = 0
xnacl = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-14 0 0 0 2e-14 0 0 0 3e-14'
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[relperm]
type = PorousFlowRelativePermeabilityConst
kr = 1
phase = 0
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 1
[]
[Outputs]
exodus = false
[]
(modules/porous_flow/test/tests/fluidstate/theis_brineco2_nonisothermal.i)
# Two phase nonisothermal Theis problem: Flow from single source.
# Constant rate injection 2 kg/s of cold CO2 into warm reservoir
# 1D cylindrical mesh
# Initially, system has only a liquid phase, until enough gas is injected
# to form a gas phase, in which case the system becomes two phase.
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
nx = 40
xmin = 0.1
xmax = 200
bias_x = 1.05
[]
coord_type = RZ
rz_coord_axis = Y
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[AuxVariables]
[saturation_gas]
order = CONSTANT
family = MONOMIAL
[]
[x1]
order = CONSTANT
family = MONOMIAL
[]
[y0]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = timestep_end
[]
[x1]
type = PorousFlowPropertyAux
variable = x1
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = timestep_end
[]
[y0]
type = PorousFlowPropertyAux
variable = y0
property = mass_fraction
phase = 1
fluid_component = 0
execute_on = timestep_end
[]
[]
[Variables]
[pgas]
initial_condition = 20e6
[]
[zi]
initial_condition = 0
[]
[xnacl]
initial_condition = 0.1
[]
[temperature]
initial_condition = 70
scaling = 1e-4
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pgas
[]
[flux0]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = pgas
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = zi
[]
[flux1]
type = PorousFlowAdvectiveFlux
fluid_component = 1
variable = zi
[]
[mass2]
type = PorousFlowMassTimeDerivative
fluid_component = 2
variable = xnacl
[]
[flux2]
type = PorousFlowAdvectiveFlux
fluid_component = 2
variable = xnacl
[]
[energy]
type = PorousFlowEnergyTimeDerivative
variable = temperature
[]
[heatadv]
type = PorousFlowHeatAdvection
variable = temperature
[]
[conduction]
type = PorousFlowHeatConduction
variable = temperature
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas zi xnacl temperature'
number_fluid_phases = 2
number_fluid_components = 3
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2]
type = CO2FluidProperties
[]
[brine]
type = BrineFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = temperature
[]
[brineco2]
type = PorousFlowFluidState
gas_porepressure = pgas
z = zi
temperature = temperature
temperature_unit = Celsius
xnacl = xnacl
capillary_pressure = pc
fluid_state = fs
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.2
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm_water]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
s_res = 0.1
sum_s_res = 0.1
[]
[relperm_gas]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 1
[]
[rockheat]
type = PorousFlowMatrixInternalEnergy
specific_heat_capacity = 1000
density = 2500
[]
[rock_thermal_conductivity]
type = PorousFlowThermalConductivityIdeal
dry_thermal_conductivity = '50 0 0 0 50 0 0 0 50'
[]
[]
[BCs]
[cold_gas]
type = DirichletBC
boundary = left
variable = temperature
value = 20
[]
[gas_injecton]
type = PorousFlowSink
boundary = left
variable = zi
flux_function = -0.159155
[]
[rightwater]
type = DirichletBC
boundary = right
value = 20e6
variable = pgas
[]
[righttemp]
type = DirichletBC
boundary = right
value = 70
variable = temperature
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-ksp_type -pc_type -sub_pc_type -sub_pc_factor_shift_type -pc_asm_overlap'
petsc_options_value = 'gmres asm lu NONZERO 2'
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
end_time = 1e4
nl_abs_tol = 1e-7
nl_rel_tol = 1e-5
# Avoids failing first time step in parallel
line_search = 'none'
[TimeStepper]
type = IterationAdaptiveDT
dt = 1
growth_factor = 1.5
[]
[]
[Postprocessors]
[pgas]
type = PointValue
point = '2 0 0'
variable = pgas
[]
[sgas]
type = PointValue
point = '2 0 0'
variable = saturation_gas
[]
[zi]
type = PointValue
point = '2 0 0'
variable = zi
[]
[temperature]
type = PointValue
point = '2 0 0'
variable = temperature
[]
[massgas]
type = PorousFlowFluidMass
fluid_component = 1
[]
[x1]
type = PointValue
point = '2 0 0'
variable = x1
[]
[y0]
type = PointValue
point = '2 0 0'
variable = y0
[]
[]
[Outputs]
print_linear_residuals = false
perf_graph = true
csv = true
[]
(modules/porous_flow/test/tests/jacobian/fflux14.i)
# 1phase, 2components (water and salt using BrineFluidProperties), constant insitu permeability
# Constant relative perm, nonzero gravity
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 2
nx = 1
xmin = 0
xmax = 10
ny = 1
ymin = 0
ymax = 10
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 -10 0'
[]
[Variables]
[pp]
[]
[xnacl]
[]
[]
[ICs]
[pp]
type = RandomIC
variable = pp
min = 1e6
max = 2e6
[]
[massfrac0]
type = RandomIC
variable = xnacl
min = 0.1
max = 0.2
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
variable = pp
fluid_component = 0
[]
[mass1]
type = PorousFlowMassTimeDerivative
variable = xnacl
fluid_component = 1
[]
[flux0]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = pp
[]
[flux1]
type = PorousFlowAdvectiveFlux
fluid_component = 1
variable = xnacl
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp xnacl'
number_fluid_phases = 1
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[FluidProperties]
[brine]
type = BrineFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = pp
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'xnacl'
[]
[brine]
type = PorousFlowBrine
phase = 0
xnacl = xnacl
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-14 0 0 0 2e-14 0 0 0 3e-14'
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[relperm]
type = PorousFlowRelativePermeabilityConst
kr = 1
phase = 0
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 1
[]
[Outputs]
exodus = false
[]
(modules/porous_flow/test/tests/relperm/corey2.i)
# Test Corey relative permeability curve by varying saturation over the mesh
# Corey exponent n = 2 for both phases
# No residual saturation in either phase
[Mesh]
type = GeneratedMesh
dim = 1
nx = 20
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[p0]
initial_condition = 1e6
[]
[s1]
family = LAGRANGE
order = FIRST
[]
[]
[AuxVariables]
[s0aux]
family = MONOMIAL
order = CONSTANT
[]
[s1aux]
family = MONOMIAL
order = CONSTANT
[]
[kr0aux]
family = MONOMIAL
order = CONSTANT
[]
[kr1aux]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[s0]
type = PorousFlowPropertyAux
property = saturation
phase = 0
variable = s0aux
[]
[s1]
type = PorousFlowPropertyAux
property = saturation
phase = 1
variable = s1aux
[]
[kr0]
type = PorousFlowPropertyAux
property = relperm
phase = 0
variable = kr0aux
[]
[kr1]
type = PorousFlowPropertyAux
property = relperm
phase = 1
variable = kr1aux
[]
[]
[Functions]
[s1]
type = ParsedFunction
expression = x
[]
[]
[ICs]
[s1]
type = FunctionIC
variable = s1
function = s1
[]
[]
[Kernels]
[p0]
type = Diffusion
variable = p0
[]
[s1]
type = Diffusion
variable = s1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'p0 s1'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = p0
phase1_saturation = s1
capillary_pressure = pc
[]
[kr0]
type = PorousFlowRelativePermeabilityCorey
phase = 0
n = 2
[]
[kr1]
type = PorousFlowRelativePermeabilityCorey
phase = 1
n = 2
[]
[]
[VectorPostprocessors]
[vpp]
type = LineValueSampler
warn_discontinuous_face_values = false
variable = 's0aux s1aux kr0aux kr1aux'
start_point = '0 0 0'
end_point = '1 0 0'
num_points = 20
sort_by = id
[]
[]
[Executioner]
type = Steady
solve_type = NEWTON
nl_abs_tol = 1e-8
[]
[BCs]
[sleft]
type = DirichletBC
variable = s1
value = 0
boundary = left
[]
[sright]
type = DirichletBC
variable = s1
value = 1
boundary = right
[]
[]
[Outputs]
csv = true
execute_on = timestep_end
[]
(modules/porous_flow/test/tests/fluidstate/theis_nonisothermal.i)
# Two-phase nonisothermal Theis problem: Flow from single source using WaterNCG fluidstate.
# Constant rate injection 2 kg/s of cold gas into warm reservoir
# 1D cylindrical mesh
# Initially, system has only a liquid phase, until enough gas is injected
# to form a gas phase, in which case the system becomes two phase.
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
nx = 40
xmin = 0.1
xmax = 200
bias_x = 1.05
[]
coord_type = RZ
rz_coord_axis = Y
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[AuxVariables]
[saturation_gas]
order = CONSTANT
family = MONOMIAL
[]
[x1]
order = CONSTANT
family = MONOMIAL
[]
[y0]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = timestep_end
[]
[x1]
type = PorousFlowPropertyAux
variable = x1
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = timestep_end
[]
[y0]
type = PorousFlowPropertyAux
variable = y0
property = mass_fraction
phase = 1
fluid_component = 0
execute_on = timestep_end
[]
[]
[Variables]
[pgas]
initial_condition = 20e6
[]
[zi]
initial_condition = 0
[]
[temperature]
initial_condition = 70
scaling = 1e-4
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pgas
[]
[flux0]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = pgas
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = zi
[]
[flux1]
type = PorousFlowAdvectiveFlux
fluid_component = 1
variable = zi
[]
[energy]
type = PorousFlowEnergyTimeDerivative
variable = temperature
[]
[heatadv]
type = PorousFlowHeatAdvection
variable = temperature
[]
[conduction]
type = PorousFlowHeatConduction
variable = temperature
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas zi temperature'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowWaterNCG
water_fp = water
gas_fp = methane
capillary_pressure = pc
[]
[]
[FluidProperties]
[methane]
type = MethaneFluidProperties
[]
[water]
type = Water97FluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = temperature
[]
[waterncg]
type = PorousFlowFluidState
gas_porepressure = pgas
z = zi
temperature = temperature
temperature_unit = Celsius
capillary_pressure = pc
fluid_state = fs
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.2
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm_water]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
s_res = 0.1
sum_s_res = 0.1
[]
[relperm_gas]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 1
[]
[rockheat]
type = PorousFlowMatrixInternalEnergy
specific_heat_capacity = 1000
density = 2500
[]
[rock_thermal_conductivity]
type = PorousFlowThermalConductivityIdeal
dry_thermal_conductivity = '50 0 0 0 50 0 0 0 50'
[]
[]
[BCs]
[cold_gas]
type = DirichletBC
boundary = left
variable = temperature
value = 20
[]
[gas_injecton]
type = PorousFlowSink
boundary = left
variable = zi
flux_function = -0.159155
[]
[rightwater]
type = DirichletBC
boundary = right
value = 20e6
variable = pgas
[]
[righttemp]
type = DirichletBC
boundary = right
value = 70
variable = temperature
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-ksp_type -pc_type -sub_pc_type -sub_pc_factor_shift_type -pc_asm_overlap'
petsc_options_value = 'gmres asm lu NONZERO 2'
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
end_time = 1e4
nl_abs_tol = 1e-7
nl_rel_tol = 1e-5
# Avoids failing first time step in parallel
line_search = 'none'
[TimeStepper]
type = IterationAdaptiveDT
dt = 1
growth_factor = 1.5
[]
[]
[Postprocessors]
[pgas]
type = PointValue
point = '2 0 0'
variable = pgas
[]
[sgas]
type = PointValue
point = '2 0 0'
variable = saturation_gas
[]
[zi]
type = PointValue
point = '2 0 0'
variable = zi
[]
[temperature]
type = PointValue
point = '2 0 0'
variable = temperature
[]
[massgas]
type = PorousFlowFluidMass
fluid_component = 1
[]
[x1]
type = PointValue
point = '2 0 0'
variable = x1
[]
[y0]
type = PointValue
point = '2 0 0'
variable = y0
[]
[]
[Outputs]
print_linear_residuals = false
perf_graph = true
csv = true
[]
(modules/porous_flow/test/tests/flux_limited_TVD_pflow/pffltvd_2D_angle.i)
# Using flux-limited TVD advection ala Kuzmin and Turek, mploying PorousFlow Kernels and UserObjects, with superbee flux-limiter
# 2D version with velocity = (0.1, 0.2, 0)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 10
xmin = 0
xmax = 1
ny = 10
ymin = 0
ymax = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[porepressure]
[]
[tracer]
[]
[]
[ICs]
[porepressure]
type = FunctionIC
variable = porepressure
function = '1 - x - 2 * y'
[]
[tracer]
type = FunctionIC
variable = tracer
function = 'if(x<0.1 | x > 0.3 | y < 0.1 | y > 0.3, 0, 1)'
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = tracer
[]
[flux0]
type = PorousFlowFluxLimitedTVDAdvection
variable = tracer
advective_flux_calculator = advective_flux_calculator_0
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = porepressure
[]
[flux1]
type = PorousFlowFluxLimitedTVDAdvection
variable = porepressure
advective_flux_calculator = advective_flux_calculator_1
[]
[]
[BCs]
[constant_boundary_porepressure]
type = FunctionDirichletBC
variable = porepressure
function = '1 - x - 2 * y'
boundary = 'left right top bottom'
[]
[no_tracer_at_boundary]
type = DirichletBC
variable = tracer
value = 0
boundary = 'left right top bottom'
[]
[]
[FluidProperties]
[the_simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2E9
thermal_expansion = 0
viscosity = 1.0
density0 = 1000.0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure tracer'
number_fluid_phases = 1
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[advective_flux_calculator_0]
type = PorousFlowAdvectiveFluxCalculatorUnsaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 0
[]
[advective_flux_calculator_1]
type = PorousFlowAdvectiveFluxCalculatorUnsaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 1
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = tracer
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = the_simple_fluid
phase = 0
[]
[relperm]
type = PorousFlowRelativePermeabilityConst
phase = 0
[]
[porosity]
type = PorousFlowPorosity
porosity_zero = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1E-2 0 0 0 1E-2 0 0 0 1E-2'
[]
[]
[Preconditioning]
active = basic
[basic]
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 lu NONZERO 2'
[]
[preferred_but_might_not_be_installed]
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 = 0.3
dt = 0.1
[]
[Outputs]
[out]
type = Exodus
execute_on = 'initial final'
[]
[]
(modules/porous_flow/test/tests/relperm/brooks_corey1.i)
# Test Brooks-Corey relative permeability curve by varying saturation over the mesh
# Exponent lambda = 2 for both phases
[Mesh]
type = GeneratedMesh
dim = 1
nx = 20
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[p0]
initial_condition = 1e6
[]
[s1]
[]
[]
[AuxVariables]
[s0aux]
family = MONOMIAL
order = CONSTANT
[]
[s1aux]
family = MONOMIAL
order = CONSTANT
[]
[kr0aux]
family = MONOMIAL
order = CONSTANT
[]
[kr1aux]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[s0]
type = PorousFlowPropertyAux
property = saturation
phase = 0
variable = s0aux
[]
[s1]
type = PorousFlowPropertyAux
property = saturation
phase = 1
variable = s1aux
[]
[kr0]
type = PorousFlowPropertyAux
property = relperm
phase = 0
variable = kr0aux
[]
[kr1]
type = PorousFlowPropertyAux
property = relperm
phase = 1
variable = kr1aux
[]
[]
[Functions]
[s1]
type = ParsedFunction
expression = x
[]
[]
[ICs]
[s1]
type = FunctionIC
variable = s1
function = s1
[]
[]
[Kernels]
[p0]
type = Diffusion
variable = p0
[]
[s1]
type = Diffusion
variable = s1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'p0 s1'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = p0
phase1_saturation = s1
capillary_pressure = pc
[]
[kr0]
type = PorousFlowRelativePermeabilityBC
phase = 0
lambda = 2
[]
[kr1]
type = PorousFlowRelativePermeabilityBC
phase = 1
lambda = 2
nw_phase = true
[]
[]
[VectorPostprocessors]
[vpp]
type = LineValueSampler
warn_discontinuous_face_values = false
variable = 's0aux s1aux kr0aux kr1aux'
start_point = '0 0 0'
end_point = '1 0 0'
num_points = 20
sort_by = id
[]
[]
[Executioner]
type = Steady
solve_type = NEWTON
nl_abs_tol = 1e-8
[]
[BCs]
[sleft]
type = DirichletBC
variable = s1
value = 0
boundary = left
[]
[sright]
type = DirichletBC
variable = s1
value = 1
boundary = right
[]
[]
[Outputs]
csv = true
execute_on = timestep_end
[]
(modules/porous_flow/test/tests/actions/addjoiner.i)
# Tests that including PorousFlowJoiner materials doesn't cause the simulation
# to fail due to the PorousFlowAddMaterialJoiner action adding duplicate
# PorousFlowJoiner materials
[GlobalParams]
PorousFlowDictator = dictator
[]
[Mesh]
type = GeneratedMesh
dim = 1
[]
[Variables]
[p0]
[]
[p1]
[]
[]
[Kernels]
[p0]
type = Diffusion
variable = p0
[]
[p1]
type = Diffusion
variable = p1
[]
[]
[FluidProperties]
[fluid0]
type = SimpleFluidProperties
[]
[fluid1]
type = SimpleFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
at_nodes = true
[]
[temperature_qp]
type = PorousFlowTemperature
[]
[ppss_nodal]
type = PorousFlow2PhasePP
at_nodes = true
phase0_porepressure = p0
phase1_porepressure = p1
capillary_pressure = pc
[]
[ppss_qp]
type = PorousFlow2PhasePP
phase0_porepressure = p0
phase1_porepressure = p1
capillary_pressure = pc
[]
[fluid0_nodal]
type = PorousFlowSingleComponentFluid
fp = fluid0
at_nodes = true
phase = 0
[]
[fluid1_nodal]
type = PorousFlowSingleComponentFluid
fp = fluid1
at_nodes = true
phase = 1
[]
[fluid0_qp]
type = PorousFlowSingleComponentFluid
fp = fluid0
phase = 0
[]
[fluid1_qp]
type = PorousFlowSingleComponentFluid
fp = fluid1
phase = 1
[]
[density_nodal]
type = PorousFlowJoiner
at_nodes = true
material_property = PorousFlow_fluid_phase_density_nodal
[]
[density_qp]
type = PorousFlowJoiner
material_property = PorousFlow_fluid_phase_density_qp
[]
[viscosity_nodal]
type = PorousFlowJoiner
material_property = PorousFlow_viscosity_nodal
at_nodes = true
[]
[viscosity_qp]
type = PorousFlowJoiner
material_property = PorousFlow_viscosity_qp
[]
[energy_ndoal]
type = PorousFlowJoiner
at_nodes = true
material_property = PorousFlow_fluid_phase_internal_energy_nodal
[]
[energy_qp]
type = PorousFlowJoiner
material_property = PorousFlow_fluid_phase_internal_energy_qp
[]
[enthalpy_nodal]
type = PorousFlowJoiner
material_property = PorousFlow_fluid_phase_enthalpy_nodal
at_nodes = true
[]
[enthalpy_qp]
type = PorousFlowJoiner
material_property = PorousFlow_fluid_phase_enthalpy_qp
[]
[relperm0_nodal]
type = PorousFlowRelativePermeabilityConst
at_nodes = true
kr = 0.5
phase = 0
[]
[relperm1_nodal]
type = PorousFlowRelativePermeabilityConst
at_nodes = true
kr = 0.8
phase = 1
[]
[relperm_nodal]
type = PorousFlowJoiner
at_nodes = true
material_property = PorousFlow_relative_permeability_nodal
[]
[]
[Executioner]
type = Steady
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'p0 p1'
number_fluid_phases = 2
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
(modules/porous_flow/test/tests/aux_kernels/darcy_velocity_lower.i)
# checking that the PorousFlowDarcyVelocityComponentLowerDimensional AuxKernel works as expected
# for the fully-saturated case (relative-permeability = 1)
# The fractured_block.e has size = 10x10x10, and a fracture running through its
# centre, with normal = (0, -sin(20deg), cos(20deg))
# Porepressure is initialised to grad(P) = (0, 0, 1)
# Fluid_density = 2
# viscosity = 10
# relative_permeability = 1
# permeability = (5, 5, 5) (in the bulk)
# permeability = (10, 10, 10) (in the fracture)
# aperture = 1
# gravity = (1, 0.5, 0.2)
# So Darcy velocity in the bulk = (1, 0.5, -0.3)
# in the fracture grad(P) = (0, 0.3213938, 0.11697778)
# In the fracture the projected gravity vector is
# tangential_gravity = (1, 0.5057899, 0.18409245)
# So the Darcy velocity in the fracture = (2, 0.690186, 0.251207)
[Mesh]
type = FileMesh
file = fractured_block.e
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '1 0.5 0.2'
[]
[Variables]
[pp]
[]
[]
[ICs]
[pinit]
type = FunctionIC
function = z
variable = pp
[]
[]
[Kernels]
[dummy]
type = TimeDerivative
variable = pp
[]
[]
[AuxVariables]
[bulk_vel_x]
order = CONSTANT
family = MONOMIAL
[]
[bulk_vel_y]
order = CONSTANT
family = MONOMIAL
[]
[bulk_vel_z]
order = CONSTANT
family = MONOMIAL
[]
[fracture_vel_x]
order = CONSTANT
family = MONOMIAL
block = 3
[]
[fracture_vel_y]
order = CONSTANT
family = MONOMIAL
block = 3
[]
[fracture_vel_z]
order = CONSTANT
family = MONOMIAL
block = 3
[]
[]
[AuxKernels]
[bulk_vel_x]
type = PorousFlowDarcyVelocityComponent
variable = bulk_vel_x
component = x
fluid_phase = 0
[]
[bulk_vel_y]
type = PorousFlowDarcyVelocityComponent
variable = bulk_vel_y
component = y
fluid_phase = 0
[]
[bulk_vel_z]
type = PorousFlowDarcyVelocityComponent
variable = bulk_vel_z
component = z
fluid_phase = 0
[]
[fracture_vel_x]
type = PorousFlowDarcyVelocityComponentLowerDimensional
variable = fracture_vel_x
component = x
fluid_phase = 0
[]
[fracture_vel_y]
type = PorousFlowDarcyVelocityComponentLowerDimensional
variable = fracture_vel_y
component = y
fluid_phase = 0
[]
[fracture_vel_z]
type = PorousFlowDarcyVelocityComponentLowerDimensional
variable = fracture_vel_z
component = z
fluid_phase = 0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 1E16
viscosity = 10
density0 = 2
thermal_expansion = 0
[]
[]
[Postprocessors]
[bulk_vel_x]
type = ElementAverageValue
block = 1
variable = bulk_vel_x
[]
[bulk_vel_y]
type = ElementAverageValue
block = 1
variable = bulk_vel_y
[]
[bulk_vel_z]
type = ElementAverageValue
block = 1
variable = bulk_vel_z
[]
[fracture_vel_x]
type = ElementAverageValue
block = 3
variable = fracture_vel_x
[]
[fracture_vel_y]
type = ElementAverageValue
block = 3
variable = fracture_vel_y
[]
[fracture_vel_z]
type = ElementAverageValue
block = 3
variable = fracture_vel_z
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = pp
capillary_pressure = pc
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '5 0 0 0 5 0 0 0 5'
block = '1 2'
[]
[permeability_fracture]
type = PorousFlowPermeabilityConst
permeability = '10 0 0 0 10 0 0 0 10'
block = 3
[]
[relperm]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[]
[Executioner]
type = Transient
dt = 1
end_time = 1
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/gravity/grav02e_fv.i)
# Checking that gravity head is established in the transient situation when 0<=saturation<=1 (note the less-than-or-equal-to).
# 2phase (PS), 2components, constant capillary pressure, constant fluid bulk-moduli for each phase, constant viscosity,
# constant permeability, Corey relative permeabilities with no residual saturation
[Mesh]
type = GeneratedMesh
dim = 1
nx = 10
xmax = 100
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '-10 0 0'
[]
[Variables]
[ppwater]
type = MooseVariableFVReal
initial_condition = 1.5e6
[]
[sgas]
type = MooseVariableFVReal
initial_condition = 0.3
[]
[]
[AuxVariables]
[massfrac_ph0_sp0]
type = MooseVariableFVReal
initial_condition = 1
[]
[massfrac_ph1_sp0]
type = MooseVariableFVReal
initial_condition = 0
[]
[ppgas]
type = MooseVariableFVReal
[]
[swater]
type = MooseVariableFVReal
[]
[relpermwater]
type = MooseVariableFVReal
[]
[relpermgas]
type = MooseVariableFVReal
[]
[]
[FVKernels]
[mass0]
type = FVPorousFlowMassTimeDerivative
fluid_component = 0
variable = ppwater
[]
[flux0]
type = FVPorousFlowAdvectiveFlux
fluid_component = 0
variable = ppwater
[]
[mass1]
type = FVPorousFlowMassTimeDerivative
fluid_component = 1
variable = sgas
[]
[flux1]
type = FVPorousFlowAdvectiveFlux
fluid_component = 1
variable = sgas
[]
[]
[AuxKernels]
[ppgas]
type = ADPorousFlowPropertyAux
property = pressure
phase = 1
variable = ppgas
execute_on = 'initial timestep_end'
[]
[swater]
type = ADPorousFlowPropertyAux
property = saturation
phase = 0
variable = swater
execute_on = 'initial timestep_end'
[]
[relpermwater]
type = ADPorousFlowPropertyAux
property = relperm
phase = 0
variable = relpermwater
execute_on = 'initial timestep_end'
[]
[relpermgas]
type = ADPorousFlowPropertyAux
property = relperm
phase = 1
variable = relpermgas
execute_on = 'initial timestep_end'
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'ppwater sgas'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 1e5
[]
[]
[FluidProperties]
[simple_fluid0]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 1000
viscosity = 1e-3
thermal_expansion = 0
[]
[simple_fluid1]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 10
viscosity = 1e-5
thermal_expansion = 0
[]
[]
[Materials]
[temperature]
type = ADPorousFlowTemperature
[]
[ppss]
type = ADPorousFlow2PhasePS
phase0_porepressure = ppwater
phase1_saturation = sgas
capillary_pressure = pc
[]
[massfrac]
type = ADPorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[simple_fluid0]
type = ADPorousFlowSingleComponentFluid
fp = simple_fluid0
phase = 0
[]
[simple_fluid1]
type = ADPorousFlowSingleComponentFluid
fp = simple_fluid1
phase = 1
[]
[porosity]
type = ADPorousFlowPorosityConst
porosity = 0.1
[]
[permeability]
type = ADPorousFlowPermeabilityConst
permeability = '1e-11 0 0 0 1e-11 0 0 0 1e-11'
[]
[relperm_water]
type = ADPorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[relperm_gas]
type = ADPorousFlowRelativePermeabilityCorey
n = 2
phase = 1
[]
[]
[VectorPostprocessors]
[vars]
type = ElementValueSampler
variable = 'ppgas ppwater sgas swater'
sort_by = x
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
end_time = 5e3
nl_abs_tol = 1e-12
[TimeStepper]
type = IterationAdaptiveDT
dt = 1e3
[]
[]
[Outputs]
execute_on = 'final'
perf_graph = true
csv = true
[]
(modules/porous_flow/test/tests/fluidstate/theis.i)
# Two phase Theis problem: Flow from single source using WaterNCG fluidstate.
# Constant rate injection 2 kg/s
# 1D cylindrical mesh
# Initially, system has only a liquid phase, until enough gas is injected
# to form a gas phase, in which case the system becomes two phase.
[Mesh]
type = GeneratedMesh
dim = 1
nx = 40
xmax = 200
bias_x = 1.05
coord_type = RZ
rz_coord_axis = Y
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[AuxVariables]
[saturation_gas]
order = CONSTANT
family = MONOMIAL
[]
[x1]
order = CONSTANT
family = MONOMIAL
[]
[y0]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = timestep_end
[]
[x1]
type = PorousFlowPropertyAux
variable = x1
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = timestep_end
[]
[y0]
type = PorousFlowPropertyAux
variable = y0
property = mass_fraction
phase = 1
fluid_component = 0
execute_on = timestep_end
[]
[]
[Variables]
[pgas]
initial_condition = 20e6
[]
[zi]
initial_condition = 0
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pgas
[]
[flux0]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = pgas
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = zi
[]
[flux1]
type = PorousFlowAdvectiveFlux
fluid_component = 1
variable = zi
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas zi'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowWaterNCG
water_fp = water
gas_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2]
type = CO2FluidProperties
[]
[water]
type = Water97FluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = 20
[]
[waterncg]
type = PorousFlowFluidState
gas_porepressure = pgas
z = zi
temperature_unit = Celsius
capillary_pressure = pc
fluid_state = fs
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.2
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm_water]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
s_res = 0.1
sum_s_res = 0.1
[]
[relperm_gas]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 1
[]
[]
[BCs]
[rightwater]
type = DirichletBC
boundary = right
value = 20e6
variable = pgas
[]
[]
[DiracKernels]
[source]
type = PorousFlowSquarePulsePointSource
point = '0 0 0'
mass_flux = 2
variable = zi
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options = '-snes_converged_reason -ksp_diagonal_scale -ksp_diagonal_scale_fix -ksp_gmres_modifiedgramschmidt -snes_linesearch_monitor'
petsc_options_iname = '-ksp_type -pc_type -sub_pc_type -sub_pc_factor_shift_type -pc_asm_overlap -snes_atol -snes_rtol -snes_max_it'
petsc_options_value = 'gmres asm lu NONZERO 2 1E-8 1E-10 20'
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
end_time = 2e2
[TimeStepper]
type = IterationAdaptiveDT
dt = 10
growth_factor = 2
[]
[]
[VectorPostprocessors]
[line]
type = NodalValueSampler
sort_by = x
variable = 'pgas zi'
execute_on = 'timestep_end'
[]
[]
[Postprocessors]
[pgas]
type = PointValue
point = '1 0 0'
variable = pgas
[]
[sgas]
type = PointValue
point = '1 0 0'
variable = saturation_gas
[]
[zi]
type = PointValue
point = '1 0 0'
variable = zi
[]
[massgas]
type = PorousFlowFluidMass
fluid_component = 1
[]
[x1]
type = PointValue
point = '1 0 0'
variable = x1
[]
[y0]
type = PointValue
point = '1 0 0'
variable = y0
[]
[]
[Outputs]
print_linear_residuals = false
perf_graph = true
[csvout]
type = CSV
execute_on = timestep_end
execute_vector_postprocessors_on = final
[]
[]
(modules/porous_flow/test/tests/fluidstate/waterncg_nonisothermal.i)
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 2
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pgas]
initial_condition = 1e6
[]
[z]
initial_condition = 0.25
[]
[temperature]
initial_condition = 70
[]
[]
[AuxVariables]
[pressure_gas]
order = CONSTANT
family = MONOMIAL
[]
[pressure_water]
order = CONSTANT
family = MONOMIAL
[]
[saturation_gas]
order = CONSTANT
family = MONOMIAL
[]
[saturation_water]
order = CONSTANT
family = MONOMIAL
[]
[density_water]
order = CONSTANT
family = MONOMIAL
[]
[density_gas]
order = CONSTANT
family = MONOMIAL
[]
[viscosity_water]
order = CONSTANT
family = MONOMIAL
[]
[viscosity_gas]
order = CONSTANT
family = MONOMIAL
[]
[enthalpy_water]
order = CONSTANT
family = MONOMIAL
[]
[enthalpy_gas]
order = CONSTANT
family = MONOMIAL
[]
[internal_energy_water]
order = CONSTANT
family = MONOMIAL
[]
[internal_energy_gas]
order = CONSTANT
family = MONOMIAL
[]
[x0_water]
order = CONSTANT
family = MONOMIAL
[]
[x0_gas]
order = CONSTANT
family = MONOMIAL
[]
[x1_water]
order = CONSTANT
family = MONOMIAL
[]
[x1_gas]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[pressure_water]
type = PorousFlowPropertyAux
variable = pressure_water
property = pressure
phase = 0
execute_on = timestep_end
[]
[pressure_gas]
type = PorousFlowPropertyAux
variable = pressure_gas
property = pressure
phase = 1
execute_on = timestep_end
[]
[saturation_water]
type = PorousFlowPropertyAux
variable = saturation_water
property = saturation
phase = 0
execute_on = timestep_end
[]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = timestep_end
[]
[density_water]
type = PorousFlowPropertyAux
variable = density_water
property = density
phase = 0
execute_on = timestep_end
[]
[density_gas]
type = PorousFlowPropertyAux
variable = density_gas
property = density
phase = 1
execute_on = timestep_end
[]
[viscosity_water]
type = PorousFlowPropertyAux
variable = viscosity_water
property = viscosity
phase = 0
execute_on = timestep_end
[]
[viscosity_gas]
type = PorousFlowPropertyAux
variable = viscosity_gas
property = viscosity
phase = 1
execute_on = timestep_end
[]
[enthalpy_water]
type = PorousFlowPropertyAux
variable = enthalpy_water
property = enthalpy
phase = 0
execute_on = timestep_end
[]
[enthalpy_gas]
type = PorousFlowPropertyAux
variable = enthalpy_gas
property = enthalpy
phase = 1
execute_on = timestep_end
[]
[internal_energy_water]
type = PorousFlowPropertyAux
variable = internal_energy_water
property = internal_energy
phase = 0
execute_on = timestep_end
[]
[internal_energy_gas]
type = PorousFlowPropertyAux
variable = internal_energy_gas
property = internal_energy
phase = 1
execute_on = timestep_end
[]
[x1_water]
type = PorousFlowPropertyAux
variable = x1_water
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = timestep_end
[]
[x1_gas]
type = PorousFlowPropertyAux
variable = x1_gas
property = mass_fraction
phase = 1
fluid_component = 1
execute_on = timestep_end
[]
[x0_water]
type = PorousFlowPropertyAux
variable = x0_water
property = mass_fraction
phase = 0
fluid_component = 0
execute_on = timestep_end
[]
[x0_gas]
type = PorousFlowPropertyAux
variable = x0_gas
property = mass_fraction
phase = 1
fluid_component = 0
execute_on = timestep_end
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
variable = pgas
fluid_component = 0
[]
[mass1]
type = PorousFlowMassTimeDerivative
variable = z
fluid_component = 1
[]
[heat]
type = TimeDerivative
variable = temperature
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas z '
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowWaterNCG
water_fp = water
gas_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2]
type = CO2FluidProperties
[]
[water]
type = Water97FluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = temperature
[]
[waterncg]
type = PorousFlowFluidState
gas_porepressure = pgas
z = z
temperature = temperature
temperature_unit = Celsius
capillary_pressure = pc
fluid_state = fs
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm0]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[relperm1]
type = PorousFlowRelativePermeabilityCorey
n = 3
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
dt = 1
end_time = 1
nl_abs_tol = 1e-12
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Postprocessors]
[density_water]
type = ElementIntegralVariablePostprocessor
variable = density_water
[]
[density_gas]
type = ElementIntegralVariablePostprocessor
variable = density_gas
[]
[viscosity_water]
type = ElementIntegralVariablePostprocessor
variable = viscosity_water
[]
[viscosity_gas]
type = ElementIntegralVariablePostprocessor
variable = viscosity_gas
[]
[enthalpy_water]
type = ElementIntegralVariablePostprocessor
variable = enthalpy_water
[]
[enthalpy_gas]
type = ElementIntegralVariablePostprocessor
variable = enthalpy_gas
[]
[internal_energy_water]
type = ElementIntegralVariablePostprocessor
variable = internal_energy_water
[]
[internal_energy_gas]
type = ElementIntegralVariablePostprocessor
variable = internal_energy_gas
[]
[x0_water]
type = ElementIntegralVariablePostprocessor
variable = x0_water
[]
[x1_gas]
type = ElementIntegralVariablePostprocessor
variable = x1_gas
[]
[x0_gas]
type = ElementIntegralVariablePostprocessor
variable = x0_gas
[]
[sg]
type = ElementIntegralVariablePostprocessor
variable = saturation_gas
[]
[sw]
type = ElementIntegralVariablePostprocessor
variable = saturation_water
[]
[pwater]
type = ElementIntegralVariablePostprocessor
variable = pressure_water
[]
[pgas]
type = ElementIntegralVariablePostprocessor
variable = pressure_gas
[]
[x0mass]
type = PorousFlowFluidMass
fluid_component = 0
phase = '0 1'
[]
[x1mass]
type = PorousFlowFluidMass
fluid_component = 1
phase = '0 1'
[]
[]
[Outputs]
csv = true
execute_on = timestep_end
[]
(modules/porous_flow/test/tests/poroperm/poro_hm_func.i)
# Test that porosity is correctly calculated.
# Porosity = biot + (phi0 - biot) * exp(-vol_strain + (biot_prime - 1) / solid_bulk * (porepressure - ref_pressure))
# The parameters used are:
# biot = 0.7
# biot_prime = 0.75
# phi0 = 0.5
# vol_strain = 0.5
# solid_bulk = 0.3
# porepressure = 2
# ref_pressure = 3
# which yield porosity = 0.420877515
[Mesh]
type = GeneratedMesh
dim = 3
[]
[GlobalParams]
PorousFlowDictator = dictator
displacements = 'disp_x disp_y disp_z'
biot_coefficient = 0.7
[]
[Variables]
[porepressure]
initial_condition = 2
[]
[disp_x]
[]
[disp_y]
[]
[disp_z]
[]
[]
[ICs]
[disp_x]
type = FunctionIC
function = '0.5 * x'
variable = disp_x
[]
[]
[Kernels]
[dummy_p]
type = TimeDerivative
variable = porepressure
[]
[dummy_x]
type = TimeDerivative
variable = disp_x
[]
[dummy_y]
type = TimeDerivative
variable = disp_y
[]
[dummy_z]
type = TimeDerivative
variable = disp_z
[]
[]
[AuxVariables]
[porosity]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[porosity]
type = PorousFlowPropertyAux
property = porosity
variable = porosity
[]
[]
[Postprocessors]
[porosity]
type = PointValue
variable = porosity
point = '0 0 0'
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Functions]
[solid_bulk_func]
type = ParsedFunction
expression = '0.3 + (t-1) * 0.1'
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = 3
[]
[eff_fluid_pressure]
type = PorousFlowEffectiveFluidPressure
[]
[total_strain]
type = ComputeSmallStrain
[]
[vol_strain]
type = PorousFlowVolumetricStrain
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[porosity]
type = PorousFlowPorosity
fluid = true
mechanical = true
ensure_positive = false
porosity_zero = 0.5
solid_bulk = solid_bulk_func
reference_porepressure = 3
biot_coefficient_prime = 0.75
[]
[]
[Executioner]
solve_type = Newton
type = Transient
num_steps = 2
[]
[Outputs]
csv = true
[]
(modules/porous_flow/examples/lava_lamp/1phase_convection.i)
# Two phase density-driven convection of dissolved CO2 in brine
#
# The model starts with CO2 in the liquid phase only. The CO2 diffuses into the brine.
# As the density of the CO2-saturated brine is greater
# than the unsaturated brine, a gravitational instability arises and density-driven
# convection of CO2-rich fingers descend into the unsaturated brine.
#
# The instability is seeded by a random perturbation to the porosity field.
# Mesh adaptivity is used to refine the mesh as the fingers form.
#
# Note: this model is computationally expensive, so should be run with multiple cores.
[GlobalParams]
PorousFlowDictator = 'dictator'
gravity = '0 -9.81 0'
[]
[Adaptivity]
max_h_level = 2
marker = marker
initial_marker = initial
initial_steps = 2
[Indicators]
[indicator]
type = GradientJumpIndicator
variable = zi
[]
[]
[Markers]
[marker]
type = ErrorFractionMarker
indicator = indicator
refine = 0.8
[]
[initial]
type = BoxMarker
bottom_left = '0 1.95 0'
top_right = '2 2 0'
inside = REFINE
outside = DO_NOTHING
[]
[]
[]
[Mesh]
type = GeneratedMesh
dim = 2
ymin = 1.5
ymax = 2
xmax = 2
ny = 20
nx = 40
bias_y = 0.95
[]
[AuxVariables]
[xnacl]
initial_condition = 0.01
[]
[saturation_gas]
order = FIRST
family = MONOMIAL
[]
[xco2l]
order = FIRST
family = MONOMIAL
[]
[density_liquid]
order = FIRST
family = MONOMIAL
[]
[porosity]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = 'timestep_end'
[]
[xco2l]
type = PorousFlowPropertyAux
variable = xco2l
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = 'timestep_end'
[]
[density_liquid]
type = PorousFlowPropertyAux
variable = density_liquid
property = density
phase = 0
execute_on = 'timestep_end'
[]
[]
[Variables]
[pgas]
[]
[zi]
scaling = 1e4
[]
[]
[ICs]
[pressure]
type = FunctionIC
function = 10e6-9.81*1000*y
variable = pgas
[]
[zi]
type = ConstantIC
value = 0
variable = zi
[]
[porosity]
type = RandomIC
variable = porosity
min = 0.25
max = 0.275
seed = 0
[]
[]
[BCs]
[top]
type = DirichletBC
value = 0.04
variable = zi
boundary = top
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pgas
[]
[flux0]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = pgas
[]
[diff0]
type = PorousFlowDispersiveFlux
fluid_component = 0
variable = pgas
disp_long = '0 0'
disp_trans = '0 0'
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = zi
[]
[flux1]
type = PorousFlowAdvectiveFlux
fluid_component = 1
variable = zi
[]
[diff1]
type = PorousFlowDispersiveFlux
fluid_component = 1
variable = zi
disp_long = '0 0'
disp_trans = '0 0'
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas zi'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2sw]
type = CO2FluidProperties
[]
[co2]
type = TabulatedBicubicFluidProperties
fp = co2sw
[]
[brine]
type = BrineFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = '45'
[]
[brineco2]
type = PorousFlowFluidState
gas_porepressure = 'pgas'
z = 'zi'
temperature_unit = Celsius
xnacl = 'xnacl'
capillary_pressure = pc
fluid_state = fs
[]
[porosity]
type = PorousFlowPorosityConst
porosity = porosity
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-11 0 0 0 1e-11 0 0 0 1e-11'
[]
[relperm_water]
type = PorousFlowRelativePermeabilityCorey
phase = 0
n = 2
s_res = 0.1
sum_s_res = 0.2
[]
[relperm_gas]
type = PorousFlowRelativePermeabilityCorey
phase = 1
n = 2
s_res = 0.1
sum_s_res = 0.2
[]
[diffusivity]
type = PorousFlowDiffusivityConst
diffusion_coeff = '2e-9 2e-9 2e-9 2e-9'
tortuosity = '1 1'
[]
[]
[Preconditioning]
active = basic
[mumps_is_best_for_parallel_jobs]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_mat_solver_package'
petsc_options_value = ' lu mumps'
[]
[basic]
type = SMP
full = true
petsc_options_iname = '-ksp_type -pc_type -sub_pc_type -sub_pc_factor_shift_type -pc_asm_overlap'
petsc_options_value = 'gmres asm lu NONZERO 2 '
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
end_time = 1e6
nl_max_its = 25
l_max_its = 100
dtmax = 1e4
nl_abs_tol = 1e-6
[TimeStepper]
type = IterationAdaptiveDT
dt = 100
growth_factor = 2
cutback_factor = 0.5
[]
[]
[Functions]
[flux]
type = ParsedFunction
symbol_values = 'delta_xco2 dt'
symbol_names = 'dx dt'
expression = 'dx/dt'
[]
[]
[Postprocessors]
[total_co2_in_gas]
type = PorousFlowFluidMass
phase = 1
fluid_component = 1
[]
[total_co2_in_liquid]
type = PorousFlowFluidMass
phase = 0
fluid_component = 1
[]
[numdofs]
type = NumDOFs
[]
[delta_xco2]
type = ChangeOverTimePostprocessor
postprocessor = total_co2_in_liquid
[]
[dt]
type = TimestepSize
[]
[flux]
type = FunctionValuePostprocessor
function = flux
[]
[]
[Outputs]
print_linear_residuals = false
perf_graph = true
exodus = true
csv = true
[]
(modules/porous_flow/examples/co2_intercomparison/1Dradial/properties.i)
# Liquid and gas properties for code intercomparison problem 3
#
# From Pruess et al, Code intercomparison builds confidence in
# numerical simulation models for geologic disposal of CO2, Energy 29 (2004)
#
# This test simply calculates density and viscosity of each phase for
# various pressures and salinities, as well as mass fractions of CO2 in the
# liquid phase and H2O in the gas phase.
#
# Four versions of this are run:
# 1) No CO2, 0 salt mass fraction (pure water)
# 2) Enough CO2 to form gas phase, 0 salt mass fraction (pure water)
# 3) No CO2, 0.15 salt mass fraction
# 4) Enough CO2 to form gas phase, 0.15 salt mass fraction
#
# These results compare well with detailed results presented in Pruess et al,
# Intercomparison of numerical simulation codes for geologic disposal of CO2,
# LBNL-51813 (2002)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 4
xmax = 4
# To get consistent ordering of results with distributed meshes
allow_renumbering = false
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[AuxVariables]
[density_liquid]
order = CONSTANT
family = MONOMIAL
[]
[density_gas]
order = CONSTANT
family = MONOMIAL
[]
[viscosity_liquid]
order = CONSTANT
family = MONOMIAL
[]
[viscosity_gas]
order = CONSTANT
family = MONOMIAL
[]
[x1]
order = CONSTANT
family = MONOMIAL
[]
[y0]
order = CONSTANT
family = MONOMIAL
[]
[xnacl]
initial_condition = 0.0
[]
[]
[AuxKernels]
[density_liquid]
type = PorousFlowPropertyAux
variable = density_liquid
property = density
phase = 0
execute_on = timestep_end
[]
[density_gas]
type = PorousFlowPropertyAux
variable = density_gas
property = density
phase = 1
execute_on = timestep_end
[]
[viscosity_liquid]
type = PorousFlowPropertyAux
variable = viscosity_liquid
property = viscosity
phase = 0
execute_on = timestep_end
[]
[viscosity_gas]
type = PorousFlowPropertyAux
variable = viscosity_gas
property = viscosity
phase = 1
execute_on = timestep_end
[]
[x1]
type = PorousFlowPropertyAux
variable = x1
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = timestep_end
[]
[y0]
type = PorousFlowPropertyAux
variable = y0
property = mass_fraction
phase = 1
fluid_component = 0
execute_on = timestep_end
[]
[]
[Variables]
[pgas]
order = CONSTANT
family = MONOMIAL
[]
[zi]
initial_condition = 0.0
[]
[]
[Functions]
[pic]
type = ParsedFunction
expression = 'if(x<1,12e6,if(x<2,16e6,if(x<3,20e6,24e6)))'
[]
[]
[ICs]
[pic]
type = FunctionIC
function = pic
variable = pgas
[]
[]
[Kernels]
[diffusionp]
type = NullKernel
variable = pgas
[]
[diffusionz]
type = NullKernel
variable = zi
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas zi'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2]
type = CO2FluidProperties
[]
[brine]
type = BrineFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = 45
[]
[brineco2]
type = PorousFlowFluidState
gas_porepressure = pgas
z = zi
temperature_unit = Celsius
xnacl = xnacl
capillary_pressure = pc
fluid_state = fs
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-ksp_type -pc_type -sub_pc_type -sub_pc_factor_shift_type -pc_asm_overlap'
petsc_options_value = 'gmres asm lu NONZERO 2 '
[]
[]
[Executioner]
type = Steady
solve_type = NEWTON
[]
[Outputs]
perf_graph = true
csv = true
execute_on = timestep_end
file_base = properties_water
[]
[VectorPostprocessors]
[vpp]
type = ElementValueSampler
variable = 'pgas density_liquid density_gas viscosity_liquid viscosity_gas x1 y0'
sort_by = x
[]
[]
(modules/porous_flow/examples/thm_example/2D.i)
# Two phase, temperature-dependent, with mechanics, radial with fine mesh, constant injection of cold co2 into a overburden-reservoir-underburden containing mostly water
# species=0 is water
# species=1 is co2
# phase=0 is liquid, and since massfrac_ph0_sp0 = 1, this is all water
# phase=1 is gas, and since massfrac_ph1_sp0 = 0, this is all co2
#
# The mesh used below has very high resolution, so the simulation takes a long time to complete.
# Some suggested meshes of different resolution:
# nx=50, bias_x=1.2
# nx=100, bias_x=1.1
# nx=200, bias_x=1.05
# nx=400, bias_x=1.02
# nx=1000, bias_x=1.01
# nx=2000, bias_x=1.003
[Mesh]
type = GeneratedMesh
dim = 2
nx = 2000
bias_x = 1.003
xmin = 0.1
xmax = 5000
ny = 1
ymin = 0
ymax = 11
coord_type = RZ
[]
[GlobalParams]
displacements = 'disp_r disp_z'
PorousFlowDictator = dictator
gravity = '0 0 0'
biot_coefficient = 1.0
[]
[Variables]
[pwater]
initial_condition = 18.3e6
[]
[sgas]
initial_condition = 0.0
[]
[temp]
initial_condition = 358
[]
[disp_r]
[]
[]
[AuxVariables]
[rate]
[]
[disp_z]
[]
[massfrac_ph0_sp0]
initial_condition = 1 # all H20 in phase=0
[]
[massfrac_ph1_sp0]
initial_condition = 0 # no H2O in phase=1
[]
[pgas]
family = MONOMIAL
order = FIRST
[]
[swater]
family = MONOMIAL
order = FIRST
[]
[stress_rr]
order = CONSTANT
family = MONOMIAL
[]
[stress_tt]
order = CONSTANT
family = MONOMIAL
[]
[stress_zz]
order = CONSTANT
family = MONOMIAL
[]
[]
[Kernels]
[mass_water_dot]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pwater
[]
[flux_water]
type = PorousFlowAdvectiveFlux
fluid_component = 0
use_displaced_mesh = false
variable = pwater
[]
[mass_co2_dot]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = sgas
[]
[flux_co2]
type = PorousFlowAdvectiveFlux
fluid_component = 1
use_displaced_mesh = false
variable = sgas
[]
[energy_dot]
type = PorousFlowEnergyTimeDerivative
variable = temp
[]
[advection]
type = PorousFlowHeatAdvection
use_displaced_mesh = false
variable = temp
[]
[conduction]
type = PorousFlowExponentialDecay
use_displaced_mesh = false
variable = temp
reference = 358
rate = rate
[]
[grad_stress_r]
type = StressDivergenceRZTensors
temperature = temp
eigenstrain_names = thermal_contribution
variable = disp_r
use_displaced_mesh = false
component = 0
[]
[poro_r]
type = PorousFlowEffectiveStressCoupling
variable = disp_r
use_displaced_mesh = false
component = 0
[]
[]
[AuxKernels]
[rate]
type = FunctionAux
variable = rate
execute_on = timestep_begin
function = decay_rate
[]
[pgas]
type = PorousFlowPropertyAux
property = pressure
phase = 1
variable = pgas
[]
[swater]
type = PorousFlowPropertyAux
property = saturation
phase = 0
variable = swater
[]
[stress_rr]
type = RankTwoAux
rank_two_tensor = stress
variable = stress_rr
index_i = 0
index_j = 0
[]
[stress_tt]
type = RankTwoAux
rank_two_tensor = stress
variable = stress_tt
index_i = 2
index_j = 2
[]
[stress_zz]
type = RankTwoAux
rank_two_tensor = stress
variable = stress_zz
index_i = 1
index_j = 1
[]
[]
[Functions]
[decay_rate]
# Eqn(26) of the first paper of LaForce et al.
# Ka * (rho C)_a = 10056886.914
# h = 11
type = ParsedFunction
expression = 'sqrt(10056886.914/t)/11.0'
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'temp pwater sgas disp_r'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[FluidProperties]
[water]
type = SimpleFluidProperties
bulk_modulus = 2.27e14
density0 = 970.0
viscosity = 0.3394e-3
cv = 4149.0
cp = 4149.0
porepressure_coefficient = 0.0
thermal_expansion = 0
[]
[co2]
type = SimpleFluidProperties
bulk_modulus = 2.27e14
density0 = 516.48
viscosity = 0.0393e-3
cv = 2920.5
cp = 2920.5
porepressure_coefficient = 0.0
thermal_expansion = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = temp
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = pwater
phase1_saturation = sgas
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[water]
type = PorousFlowSingleComponentFluid
fp = water
phase = 0
[]
[gas]
type = PorousFlowSingleComponentFluid
fp = co2
phase = 1
[]
[porosity_reservoir]
type = PorousFlowPorosityConst
porosity = 0.2
[]
[permeability_reservoir]
type = PorousFlowPermeabilityConst
permeability = '2e-12 0 0 0 0 0 0 0 0'
[]
[relperm_liquid]
type = PorousFlowRelativePermeabilityCorey
n = 4
phase = 0
s_res = 0.200
sum_s_res = 0.405
[]
[relperm_gas]
type = PorousFlowRelativePermeabilityBC
phase = 1
s_res = 0.205
sum_s_res = 0.405
nw_phase = true
lambda = 2
[]
[thermal_conductivity_reservoir]
type = PorousFlowThermalConductivityIdeal
dry_thermal_conductivity = '0 0 0 0 1.320 0 0 0 0'
wet_thermal_conductivity = '0 0 0 0 3.083 0 0 0 0'
[]
[internal_energy_reservoir]
type = PorousFlowMatrixInternalEnergy
specific_heat_capacity = 1100
density = 2350.0
[]
[elasticity_tensor]
type = ComputeIsotropicElasticityTensor
shear_modulus = 6.0E9
poissons_ratio = 0.2
[]
[strain]
type = ComputeAxisymmetricRZSmallStrain
eigenstrain_names = 'thermal_contribution ini_stress'
[]
[ini_strain]
type = ComputeEigenstrainFromInitialStress
initial_stress = '-12.8E6 0 0 0 -51.3E6 0 0 0 -12.8E6'
eigenstrain_name = ini_stress
[]
[thermal_contribution]
type = ComputeThermalExpansionEigenstrain
temperature = temp
stress_free_temperature = 358
thermal_expansion_coeff = 5E-6
eigenstrain_name = thermal_contribution
[]
[stress]
type = ComputeLinearElasticStress
[]
[eff_fluid_pressure]
type = PorousFlowEffectiveFluidPressure
[]
[vol_strain]
type = PorousFlowVolumetricStrain
[]
[]
[BCs]
[outer_pressure_fixed]
type = DirichletBC
boundary = right
value = 18.3e6
variable = pwater
[]
[outer_saturation_fixed]
type = DirichletBC
boundary = right
value = 0.0
variable = sgas
[]
[outer_temp_fixed]
type = DirichletBC
boundary = right
value = 358
variable = temp
[]
[fixed_outer_r]
type = DirichletBC
variable = disp_r
value = 0
boundary = right
[]
[co2_injection]
type = PorousFlowSink
boundary = left
variable = sgas
use_mobility = false
use_relperm = false
fluid_phase = 1
flux_function = 'min(t/100.0,1)*(-2.294001475)' # 5.0E5 T/year = 15.855 kg/s, over area of 2Pi*0.1*11
[]
[cold_co2]
type = DirichletBC
boundary = left
variable = temp
value = 294
[]
[cavity_pressure_x]
type = Pressure
boundary = left
variable = disp_r
component = 0
postprocessor = p_bh # note, this lags
use_displaced_mesh = false
[]
[]
[Postprocessors]
[p_bh]
type = PointValue
variable = pwater
point = '0.1 0 0'
execute_on = timestep_begin
use_displaced_mesh = false
[]
[]
[VectorPostprocessors]
[ptsuss]
type = LineValueSampler
use_displaced_mesh = false
start_point = '0.1 0 0'
end_point = '5000 0 0'
sort_by = x
num_points = 50000
outputs = csv
variable = 'pwater temp sgas disp_r stress_rr stress_tt'
[]
[]
[Preconditioning]
active = 'smp'
[smp]
type = SMP
full = true
#petsc_options = '-snes_converged_reason -ksp_diagonal_scale -ksp_diagonal_scale_fix -ksp_gmres_modifiedgramschmidt -snes_linesearch_monitor'
petsc_options_iname = '-ksp_type -pc_type -sub_pc_type -sub_pc_factor_shift_type -pc_asm_overlap -snes_atol -snes_rtol -snes_max_it'
petsc_options_value = 'gmres asm lu NONZERO 2 1E2 1E-5 500'
[]
[mumps]
type = SMP
full = true
petsc_options = '-snes_converged_reason -ksp_diagonal_scale -ksp_diagonal_scale_fix -ksp_gmres_modifiedgramschmidt -snes_linesearch_monitor'
petsc_options_iname = '-ksp_type -pc_type -pc_factor_mat_solver_package -pc_factor_shift_type -snes_rtol -snes_atol -snes_max_it'
petsc_options_value = 'gmres lu mumps NONZERO 1E-5 1E2 50'
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
end_time = 1.5768e8
#dtmax = 1e6
[TimeStepper]
type = IterationAdaptiveDT
dt = 1
growth_factor = 1.1
[]
[]
[Outputs]
print_linear_residuals = false
sync_times = '3600 86400 2.592E6 1.5768E8'
perf_graph = true
exodus = true
[csv]
type = CSV
sync_only = true
[]
[]
(modules/porous_flow/test/tests/pressure_pulse/pressure_pulse_1d_2comp.i)
# Pressure pulse in 1D with 1 phase but 2 components (where density and viscosity depend on mass fraction)
# This test uses BrineFluidProperties with the PorousFlowMultiComponentFluid material, but could be run using
# the PorousFlowBrine material instead.
[Mesh]
type = GeneratedMesh
dim = 1
nx = 10
xmin = 0
xmax = 100
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp xnacl'
number_fluid_phases = 1
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[Variables]
[pp]
initial_condition = 1e6
[]
[xnacl]
initial_condition = 0
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[flux0]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = pp
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = xnacl
[]
[flux1]
type = PorousFlowAdvectiveFlux
fluid_component = 1
variable = xnacl
[]
[]
[AuxVariables]
[density]
family = MONOMIAL
order = FIRST
[]
[]
[AuxKernels]
[density]
type = PorousFlowPropertyAux
variable = density
property = density
phase = 0
execute_on = 'initial timestep_end'
[]
[]
[FluidProperties]
[brine]
type = BrineFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = 293
[]
[mass_fractions]
type = PorousFlowMassFraction
mass_fraction_vars = xnacl
[]
[ps]
type = PorousFlow1PhaseP
porepressure = pp
capillary_pressure = pc
[]
[brine]
type = PorousFlowMultiComponentFluid
x = xnacl
fp = brine
phase = 0
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-7 0 0 0 1e-7 0 0 0 1e-7'
[]
[relperm]
type = PorousFlowRelativePermeabilityConst
kr = 1
phase = 0
[]
[]
[BCs]
[left_p]
type = DirichletBC
boundary = left
value = 2e6
variable = pp
[]
[right_p]
type = DirichletBC
boundary = right
value = 1e6
variable = pp
[]
[left_xnacl]
type = DirichletBC
boundary = left
value = 0.2
variable = xnacl
[]
[right_xnacl]
type = DirichletBC
boundary = right
value = 0
variable = xnacl
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-ksp_type -pc_type -pc_factor_shift_type'
petsc_options_value = 'bcgs lu NONZERO'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 5
[]
[Postprocessors]
[p000]
type = PointValue
variable = pp
point = '0 0 0'
execute_on = 'initial timestep_end'
[]
[p050]
type = PointValue
variable = pp
point = '50 0 0'
execute_on = 'initial timestep_end'
[]
[p100]
type = PointValue
variable = pp
point = '100 0 0'
execute_on = 'initial timestep_end'
[]
[xnacl_000]
type = PointValue
variable = xnacl
point = '0 0 0'
execute_on = 'initial timestep_end'
[]
[density_000]
type = PointValue
variable = density
point = '0 0 0'
execute_on = 'initial timestep_end'
[]
[xnacl_020]
type = PointValue
variable = xnacl
point = '20 0 0'
execute_on = 'initial timestep_end'
[]
[density_020]
type = PointValue
variable = density
point = '20 0 0'
execute_on = 'initial timestep_end'
[]
[xnacl_040]
type = PointValue
variable = xnacl
point = '40 0 0'
execute_on = 'initial timestep_end'
[]
[density_040]
type = PointValue
variable = density
point = '40 0 0'
execute_on = 'initial timestep_end'
[]
[xnacl_060]
type = PointValue
variable = xnacl
point = '60 0 0'
execute_on = 'initial timestep_end'
[]
[density_060]
type = PointValue
variable = density
point = '60 0 0'
execute_on = 'initial timestep_end'
[]
[xnacl_080]
type = PointValue
variable = xnacl
point = '80 0 0'
execute_on = 'initial timestep_end'
[]
[density_080]
type = PointValue
variable = density
point = '80 0 0'
execute_on = 'initial timestep_end'
[]
[xnacl_100]
type = PointValue
variable = xnacl
point = '100 0 0'
execute_on = 'initial timestep_end'
[]
[density_100]
type = PointValue
variable = density
point = '100 0 0'
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/recover/pffltvd.i)
# Tests that PorousFlow can successfully recover using a checkpoint file.
# This test contains stateful material properties, adaptivity, integrated
# boundary conditions with nodal-sized materials, and TVD flux limiting.
#
# This test file is run three times:
# 1) The full input file is run to completion
# 2) The input file is run for half the time and checkpointing is included
# 3) The input file is run in recovery using the checkpoint data
#
# The final output of test 3 is compared to the final output of test 1 to verify
# that recovery was successful.
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
nx = 10
xmin = 0
xmax = 1
[]
# To get consistent ordering of results with distributed meshes
allow_renumbering = false
[]
[Adaptivity]
initial_steps = 1
initial_marker = tracer_marker
marker = tracer_marker
max_h_level = 1
[Markers]
[tracer_marker]
type = ValueRangeMarker
variable = tracer
lower_bound = 0.02
upper_bound = 0.98
[]
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[porepressure]
[]
[tracer]
[]
[]
[ICs]
[porepressure]
type = FunctionIC
variable = porepressure
function = '2 - x'
[]
[tracer]
type = FunctionIC
variable = tracer
function = 'if(x<0.1,0,if(x>0.3,0,1))'
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = tracer
[]
[flux0]
type = PorousFlowFluxLimitedTVDAdvection
variable = tracer
advective_flux_calculator = advective_flux_calculator_0
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = porepressure
[]
[flux1]
type = PorousFlowFluxLimitedTVDAdvection
variable = porepressure
advective_flux_calculator = advective_flux_calculator_1
[]
[]
[BCs]
[constant_injection_porepressure]
type = DirichletBC
variable = porepressure
value = 2
boundary = left
[]
[no_tracer_on_left]
type = DirichletBC
variable = tracer
value = 0
boundary = left
[]
[remove_component_1]
type = PorousFlowPiecewiseLinearSink
variable = porepressure
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 1
use_mobility = true
flux_function = 1E3
[]
[remove_component_0]
type = PorousFlowPiecewiseLinearSink
variable = tracer
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 0
use_mobility = true
flux_function = 1E3
[]
[]
[FluidProperties]
[the_simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2E9
thermal_expansion = 0
viscosity = 1.0
density0 = 1000.0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure tracer'
number_fluid_phases = 1
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[advective_flux_calculator_0]
type = PorousFlowAdvectiveFluxCalculatorSaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 0
[]
[advective_flux_calculator_1]
type = PorousFlowAdvectiveFluxCalculatorSaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 1
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = tracer
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = the_simple_fluid
phase = 0
[]
[relperm]
type = PorousFlowRelativePermeabilityConst
phase = 0
[]
[porosity]
type = PorousFlowPorosity
porosity_zero = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1E-2 0 0 0 1E-2 0 0 0 1E-2'
[]
[]
[Preconditioning]
[basic]
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 lu NONZERO 2'
[]
[]
[VectorPostprocessors]
[tracer]
type = NodalValueSampler
sort_by = x
variable = tracer
[]
[]
[Executioner]
type = Transient
solve_type = Newton
end_time = 0.2
dt = 0.05
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/flux_limited_TVD_pflow/pffltvd_3D.i)
# Using flux-limited TVD advection ala Kuzmin and Turek, employing PorousFlow Kernels and UserObjects, with superbee flux-limiter
# 3D version
[Mesh]
type = GeneratedMesh
dim = 3
nx = 10
xmin = 0
xmax = 1
ny = 4
ymin = 0
ymax = 0.5
nz = 3
zmin = 0
zmax = 2
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[porepressure]
[]
[tracer]
[]
[]
[ICs]
[porepressure]
type = FunctionIC
variable = porepressure
function = '1 - x'
[]
[tracer]
type = FunctionIC
variable = tracer
function = 'if(x<0.1,0,if(x>0.3,0,1))'
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = tracer
[]
[flux0]
type = PorousFlowFluxLimitedTVDAdvection
variable = tracer
advective_flux_calculator = advective_flux_calculator_0
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = porepressure
[]
[flux1]
type = PorousFlowFluxLimitedTVDAdvection
variable = porepressure
advective_flux_calculator = advective_flux_calculator_1
[]
[]
[BCs]
[constant_injection_porepressure]
type = DirichletBC
variable = porepressure
value = 1
boundary = left
[]
[no_tracer_on_left]
type = DirichletBC
variable = tracer
value = 0
boundary = left
[]
[remove_component_1]
type = PorousFlowPiecewiseLinearSink
variable = porepressure
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 1
use_mobility = true
flux_function = 1E3
[]
[remove_component_0]
type = PorousFlowPiecewiseLinearSink
variable = tracer
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 0
use_mobility = true
flux_function = 1E3
[]
[]
[FluidProperties]
[the_simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2E9
thermal_expansion = 0
viscosity = 1.0
density0 = 1000.0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure tracer'
number_fluid_phases = 1
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[advective_flux_calculator_0]
type = PorousFlowAdvectiveFluxCalculatorSaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 0
[]
[advective_flux_calculator_1]
type = PorousFlowAdvectiveFluxCalculatorSaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 1
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = tracer
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = the_simple_fluid
phase = 0
[]
[relperm]
type = PorousFlowRelativePermeabilityConst
phase = 0
[]
[porosity]
type = PorousFlowPorosity
porosity_zero = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1E-2 0 0 0 1E-2 0 0 0 1E-2'
[]
[]
[Preconditioning]
active = basic
[basic]
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 lu NONZERO 2'
[]
[preferred_but_might_not_be_installed]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_mat_solver_package'
petsc_options_value = ' lu mumps'
[]
[]
[VectorPostprocessors]
[tracer]
type = LineValueSampler
start_point = '0 0 0'
end_point = '1 0.5 2'
num_points = 11
sort_by = x
variable = tracer
[]
[]
[Executioner]
type = Transient
solve_type = Newton
end_time = 0.3
dt = 6E-2
nl_abs_tol = 1E-8
timestep_tolerance = 1E-3
[]
[Outputs]
print_linear_residuals = false
[out]
type = CSV
execute_on = final
[]
[]
(modules/porous_flow/test/tests/pressure_pulse/pressure_pulse_1d_2phasePS_fv.i)
# Pressure pulse in 1D with 2 phases, 2components - transient using FV
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
nx = 10
xmin = 0
xmax = 100
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[ppwater]
type = MooseVariableFVReal
initial_condition = 2e6
[]
[sgas]
type = MooseVariableFVReal
initial_condition = 0.3
[]
[]
[AuxVariables]
[massfrac_ph0_sp0]
type = MooseVariableFVReal
initial_condition = 1
[]
[massfrac_ph1_sp0]
type = MooseVariableFVReal
initial_condition = 0
[]
[ppgas]
type = MooseVariableFVReal
[]
[]
[FVKernels]
[mass0]
type = FVPorousFlowMassTimeDerivative
fluid_component = 0
variable = ppwater
[]
[flux0]
type = FVPorousFlowAdvectiveFlux
variable = ppwater
fluid_component = 0
[]
[mass1]
type = FVPorousFlowMassTimeDerivative
fluid_component = 1
variable = sgas
[]
[flux1]
type = FVPorousFlowAdvectiveFlux
variable = sgas
fluid_component = 1
[]
[]
[AuxKernels]
[ppgas]
type = ADPorousFlowPropertyAux
property = pressure
phase = 1
variable = ppgas
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'ppwater sgas'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 1e5
[]
[]
[FluidProperties]
[simple_fluid0]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 1000
thermal_expansion = 0
viscosity = 1e-3
[]
[simple_fluid1]
type = SimpleFluidProperties
bulk_modulus = 2e7
density0 = 1
thermal_expansion = 0
viscosity = 1e-5
[]
[]
[Materials]
[temperature]
type = ADPorousFlowTemperature
[]
[ppss]
type = ADPorousFlow2PhasePS
phase0_porepressure = ppwater
phase1_saturation = sgas
capillary_pressure = pc
[]
[massfrac]
type = ADPorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[simple_fluid0]
type = ADPorousFlowSingleComponentFluid
fp = simple_fluid0
phase = 0
[]
[simple_fluid1]
type = ADPorousFlowSingleComponentFluid
fp = simple_fluid1
phase = 1
[]
[porosity]
type = ADPorousFlowPorosityConst
porosity = 0.1
[]
[permeability]
type = ADPorousFlowPermeabilityConst
permeability = '1e-15 0 0 0 1e-15 0 0 0 1e-15'
[]
[relperm_water]
type = ADPorousFlowRelativePermeabilityCorey
n = 1
phase = 0
[]
[relperm_gas]
type = ADPorousFlowRelativePermeabilityCorey
n = 1
phase = 1
[]
[]
[FVBCs]
[leftwater]
type = FVDirichletBC
boundary = left
value = 3e6
variable = ppwater
[]
[rightwater]
type = FVDirichletBC
boundary = right
value = 2e6
variable = ppwater
[]
[sgas]
type = FVDirichletBC
boundary = 'left right'
value = 0.3
variable = sgas
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1e3
end_time = 1e4
[]
[VectorPostprocessors]
[pp]
type = ElementValueSampler
sort_by = x
variable = 'ppwater ppgas'
[]
[]
[Outputs]
file_base = pressure_pulse_1d_2phasePS_fv
print_linear_residuals = false
[csv]
type = CSV
execute_on = final
[]
exodus = true
[]
(modules/porous_flow/test/tests/relperm/corey3.i)
# Test Corey relative permeability curve by varying saturation over the mesh
# Residual saturation of phase 0: s0r = 0.2
# Residual saturation of phase 1: s1r = 0.3
[Mesh]
type = GeneratedMesh
dim = 1
nx = 20
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[p0]
initial_condition = 1e6
[]
[s1]
family = LAGRANGE
order = FIRST
[]
[]
[AuxVariables]
[s0aux]
family = MONOMIAL
order = CONSTANT
[]
[s1aux]
family = MONOMIAL
order = CONSTANT
[]
[kr0aux]
family = MONOMIAL
order = CONSTANT
[]
[kr1aux]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[s0]
type = PorousFlowPropertyAux
property = saturation
phase = 0
variable = s0aux
[]
[s1]
type = PorousFlowPropertyAux
property = saturation
phase = 1
variable = s1aux
[]
[kr0]
type = PorousFlowPropertyAux
property = relperm
phase = 0
variable = kr0aux
[]
[kr1]
type = PorousFlowPropertyAux
property = relperm
phase = 1
variable = kr1aux
[]
[]
[Functions]
[s1]
type = ParsedFunction
expression = x
[]
[]
[ICs]
[s1]
type = FunctionIC
variable = s1
function = s1
[]
[]
[Kernels]
[p0]
type = Diffusion
variable = p0
[]
[s1]
type = Diffusion
variable = s1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'p0 s1'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = p0
phase1_saturation = s1
capillary_pressure = pc
[]
[kr0]
type = PorousFlowRelativePermeabilityCorey
phase = 0
n = 2
s_res = 0.2
sum_s_res = 0.5
[]
[kr1]
type = PorousFlowRelativePermeabilityCorey
phase = 1
n = 2
s_res = 0.3
sum_s_res = 0.5
[]
[]
[VectorPostprocessors]
[vpp]
type = LineValueSampler
warn_discontinuous_face_values = false
variable = 's0aux s1aux kr0aux kr1aux'
start_point = '0 0 0'
end_point = '1 0 0'
num_points = 20
sort_by = id
[]
[]
[Executioner]
type = Steady
solve_type = NEWTON
nl_abs_tol = 1e-8
[]
[BCs]
[sleft]
type = DirichletBC
variable = s1
value = 0
boundary = left
[]
[sright]
type = DirichletBC
variable = s1
value = 1
boundary = right
[]
[]
[Outputs]
csv = true
execute_on = timestep_end
[]
(modules/porous_flow/test/tests/flux_limited_TVD_pflow/pffltvd_2D_trimesh.i)
# Using flux-limited TVD advection ala Kuzmin and Turek, mploying PorousFlow Kernels and UserObjects, with superbee flux-limiter
# 2D version
[Mesh]
type = FileMesh
file = trimesh.msh
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
block = '50'
[]
[Variables]
[porepressure]
[]
[tracer]
[]
[]
[ICs]
[porepressure]
type = FunctionIC
variable = porepressure
function = '1 - x'
[]
[tracer]
type = FunctionIC
variable = tracer
function = 'if(x<0.1,0,if(x>0.305,0,1))'
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = tracer
[]
[flux0]
type = PorousFlowFluxLimitedTVDAdvection
variable = tracer
advective_flux_calculator = advective_flux_calculator_0
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = porepressure
[]
[flux1]
type = PorousFlowFluxLimitedTVDAdvection
variable = porepressure
advective_flux_calculator = advective_flux_calculator_1
[]
[]
[BCs]
[constant_injection_porepressure]
type = DirichletBC
variable = porepressure
value = 1
boundary = left
[]
[no_tracer_on_left]
type = DirichletBC
variable = tracer
value = 0
boundary = left
[]
[remove_component_1]
type = PorousFlowPiecewiseLinearSink
variable = porepressure
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 1
use_mobility = true
flux_function = 1E3
[]
[remove_component_0]
type = PorousFlowPiecewiseLinearSink
variable = tracer
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 0
use_mobility = true
flux_function = 1E3
[]
[]
[FluidProperties]
[the_simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2E9
thermal_expansion = 0
viscosity = 1.0
density0 = 1000.0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure tracer'
number_fluid_phases = 1
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[advective_flux_calculator_0]
type = PorousFlowAdvectiveFluxCalculatorUnsaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 0
[]
[advective_flux_calculator_1]
type = PorousFlowAdvectiveFluxCalculatorUnsaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 1
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = tracer
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = the_simple_fluid
phase = 0
[]
[relperm]
type = PorousFlowRelativePermeabilityConst
phase = 0
[]
[porosity]
type = PorousFlowPorosity
porosity_zero = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1E-2 0 0 0 1E-2 0 0 0 1E-2'
[]
[]
[Preconditioning]
active = basic
[basic]
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'
[]
[preferred_but_might_not_be_installed]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_mat_solver_package'
petsc_options_value = ' lu mumps'
[]
[]
[VectorPostprocessors]
[tracer]
type = LineValueSampler
start_point = '0 0 0'
end_point = '1 0.04 0'
num_points = 101
sort_by = x
variable = tracer
[]
[]
[Executioner]
type = Transient
solve_type = Newton
end_time = 6
dt = 6E-2
nl_abs_tol = 1E-8
timestep_tolerance = 1E-3
[]
[Outputs]
print_linear_residuals = false
[out]
type = CSV
execute_on = final
[]
[]
(modules/porous_flow/examples/lava_lamp/2phase_convection.i)
# Two phase density-driven convection of dissolved CO2 in brine
#
# Initially, the model has a gas phase at the top with a saturation of 0.29
# (which corresponds to an initial value of zi = 0.2).
# Diffusion of the dissolved CO2
# component from the saturated liquid to the unsaturated liquid below reduces the
# amount of CO2 in the gas phase. As the density of the CO2-saturated brine is greater
# than the unsaturated brine, a gravitational instability arises and density-driven
# convection of CO2-rich fingers descend into the unsaturated brine.
#
# The instability is seeded by a random perturbation to the porosity field.
# Mesh adaptivity is used to refine the mesh as the fingers form.
#
# Note: this model is computationally expensive, so should be run with multiple cores,
# preferably on a cluster.
[GlobalParams]
PorousFlowDictator = 'dictator'
gravity = '0 -9.81 0'
[]
[Adaptivity]
max_h_level = 2
marker = marker
initial_marker = initial
initial_steps = 2
[Indicators]
[indicator]
type = GradientJumpIndicator
variable = zi
[]
[]
[Markers]
[marker]
type = ErrorFractionMarker
indicator = indicator
refine = 0.8
[]
[initial]
type = BoxMarker
bottom_left = '0 1.95 0'
top_right = '2 2 0'
inside = REFINE
outside = DO_NOTHING
[]
[]
[]
[Mesh]
type = GeneratedMesh
dim = 2
ymax = 2
xmax = 2
ny = 40
nx = 40
bias_y = 0.95
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pgas
[]
[flux0]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = pgas
[]
[diff0]
type = PorousFlowDispersiveFlux
fluid_component = 0
variable = pgas
disp_long = '0 0'
disp_trans = '0 0'
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = zi
[]
[flux1]
type = PorousFlowAdvectiveFlux
fluid_component = 1
variable = zi
[]
[diff1]
type = PorousFlowDispersiveFlux
fluid_component = 1
variable = zi
disp_long = '0 0'
disp_trans = '0 0'
[]
[]
[AuxVariables]
[xnacl]
initial_condition = 0.01
[]
[saturation_gas]
order = FIRST
family = MONOMIAL
[]
[xco2l]
order = FIRST
family = MONOMIAL
[]
[density_liquid]
order = FIRST
family = MONOMIAL
[]
[porosity]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = 'timestep_end'
[]
[xco2l]
type = PorousFlowPropertyAux
variable = xco2l
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = 'timestep_end'
[]
[density_liquid]
type = PorousFlowPropertyAux
variable = density_liquid
property = density
phase = 0
execute_on = 'timestep_end'
[]
[]
[Variables]
[pgas]
[]
[zi]
scaling = 1e4
[]
[]
[ICs]
[pressure]
type = FunctionIC
function = 10e6-9.81*1000*y
variable = pgas
[]
[zi]
type = BoundingBoxIC
variable = zi
x1 = 0
x2 = 2
y1 = 1.95
y2 = 2
inside = 0.2
outside = 0
[]
[porosity]
type = RandomIC
variable = porosity
min = 0.25
max = 0.275
seed = 0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas zi'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2sw]
type = CO2FluidProperties
[]
[co2]
type = TabulatedBicubicFluidProperties
fp = co2sw
[]
[brine]
type = BrineFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = '45'
[]
[brineco2]
type = PorousFlowFluidState
gas_porepressure = 'pgas'
z = 'zi'
temperature_unit = Celsius
xnacl = 'xnacl'
capillary_pressure = pc
fluid_state = fs
[]
[porosity]
type = PorousFlowPorosityConst
porosity = porosity
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-11 0 0 0 1e-11 0 0 0 1e-11'
[]
[relperm_water]
type = PorousFlowRelativePermeabilityCorey
phase = 0
n = 2
s_res = 0.1
sum_s_res = 0.2
[]
[relperm_gas]
type = PorousFlowRelativePermeabilityCorey
phase = 1
n = 2
s_res = 0.1
sum_s_res = 0.2
[]
[diffusivity]
type = PorousFlowDiffusivityConst
diffusion_coeff = '2e-9 2e-9 2e-9 2e-9'
tortuosity = '1 1'
[]
[]
[Preconditioning]
active = basic
[mumps_is_best_for_parallel_jobs]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_mat_solver_package'
petsc_options_value = ' lu mumps'
[]
[basic]
type = SMP
full = true
petsc_options_iname = '-ksp_type -pc_type -sub_pc_type -sub_pc_factor_shift_type -pc_asm_overlap'
petsc_options_value = 'gmres asm lu NONZERO 2 '
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
end_time = 1e6
nl_max_its = 25
l_max_its = 100
dtmax = 1e4
nl_abs_tol = 1e-6
[TimeStepper]
type = IterationAdaptiveDT
dt = 10
growth_factor = 2
cutback_factor = 0.5
[]
[]
[Functions]
[flux]
type = ParsedFunction
symbol_values = 'delta_xco2 dt'
symbol_names = 'dx dt'
expression = 'dx/dt'
[]
[]
[Postprocessors]
[total_co2_in_gas]
type = PorousFlowFluidMass
phase = 1
fluid_component = 1
[]
[total_co2_in_liquid]
type = PorousFlowFluidMass
phase = 0
fluid_component = 1
[]
[numdofs]
type = NumDOFs
[]
[delta_xco2]
type = ChangeOverTimePostprocessor
postprocessor = total_co2_in_liquid
[]
[dt]
type = TimestepSize
[]
[flux]
type = FunctionValuePostprocessor
function = flux
[]
[]
[Outputs]
print_linear_residuals = false
perf_graph = true
exodus = true
csv = true
[]
(modules/porous_flow/test/tests/dirackernels/theis3.i)
# Two phase Theis problem: Flow from single source
# Constant rate injection 0.5 kg/s
# 1D cylindrical mesh
[Mesh]
type = GeneratedMesh
dim = 1
nx = 100
xmax = 2000
bias_x = 1.05
coord_type = RZ
rz_coord_axis = Y
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[ppwater]
initial_condition = 20e6
[]
[sgas]
initial_condition = 0
[]
[]
[AuxVariables]
[massfrac_ph0_sp0]
initial_condition = 1
[]
[massfrac_ph1_sp0]
initial_condition = 0
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = ppwater
[]
[flux0]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = ppwater
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = sgas
[]
[flux1]
type = PorousFlowAdvectiveFlux
fluid_component = 1
variable = sgas
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'ppwater sgas'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 1e5
[]
[]
[FluidProperties]
[simple_fluid0]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 1000
viscosity = 1e-3
thermal_expansion = 0
[]
[simple_fluid1]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 10
viscosity = 1e-4
thermal_expansion = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = ppwater
phase1_saturation = sgas
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid0
phase = 0
compute_enthalpy = false
compute_internal_energy = false
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid1
phase = 1
compute_enthalpy = false
compute_internal_energy = false
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.2
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm_water]
type = PorousFlowRelativePermeabilityCorey
n = 1
phase = 0
[]
[relperm_gas]
type = PorousFlowRelativePermeabilityCorey
n = 1
phase = 1
[]
[]
[BCs]
[rightwater]
type = DirichletBC
boundary = right
value = 20e6
variable = ppwater
[]
[]
[DiracKernels]
[source]
type = PorousFlowSquarePulsePointSource
point = '0 0 0'
mass_flux = 0.5
variable = sgas
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options = '-snes_converged_reason -ksp_diagonal_scale -ksp_diagonal_scale_fix -ksp_gmres_modifiedgramschmidt -snes_linesearch_monitor'
petsc_options_iname = '-ksp_type -pc_type -sub_pc_type -sub_pc_factor_shift_type -pc_asm_overlap -snes_atol -snes_rtol -snes_max_it'
petsc_options_value = 'gmres asm lu NONZERO 2 1E-8 1E-10 20'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
end_time = 1e4
[TimeStepper]
type = IterationAdaptiveDT
dt = 10
growth_factor = 2
[]
[]
[VectorPostprocessors]
[line]
type = NodalValueSampler
sort_by = x
variable = 'ppwater sgas'
execute_on = 'timestep_end'
[]
[]
[Postprocessors]
[ppwater]
type = PointValue
point = '4 0 0'
variable = ppwater
[]
[sgas]
type = PointValue
point = '4 0 0'
variable = sgas
[]
[massgas]
type = PorousFlowFluidMass
fluid_component = 1
[]
[]
[Outputs]
file_base = theis3
print_linear_residuals = false
perf_graph = true
[csv]
type = CSV
execute_on = timestep_end
execute_vector_postprocessors_on = final
[]
[]
(modules/porous_flow/test/tests/fluidstate/theis_brineco2.i)
# Two phase Theis problem: Flow from single source.
# Constant rate injection 2 kg/s
# 1D cylindrical mesh
# Initially, system has only a liquid phase, until enough gas is injected
# to form a gas phase, in which case the system becomes two phase.
#
# This test takes a few minutes to run, so is marked heavy
[Mesh]
type = GeneratedMesh
dim = 1
nx = 2000
xmax = 2000
rz_coord_axis = Y
coord_type = RZ
[]
[Problem]
type = FEProblem
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[AuxVariables]
[saturation_gas]
order = CONSTANT
family = MONOMIAL
[]
[x1]
order = CONSTANT
family = MONOMIAL
[]
[y0]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = timestep_end
[]
[x1]
type = PorousFlowPropertyAux
variable = x1
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = timestep_end
[]
[y0]
type = PorousFlowPropertyAux
variable = y0
property = mass_fraction
phase = 1
fluid_component = 0
execute_on = timestep_end
[]
[]
[Variables]
[pgas]
initial_condition = 20e6
[]
[zi]
initial_condition = 0
[]
[xnacl]
initial_condition = 0.1
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pgas
[]
[flux0]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = pgas
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = zi
[]
[flux1]
type = PorousFlowAdvectiveFlux
fluid_component = 1
variable = zi
[]
[mass2]
type = PorousFlowMassTimeDerivative
fluid_component = 2
variable = xnacl
[]
[flux2]
type = PorousFlowAdvectiveFlux
fluid_component = 2
variable = xnacl
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas zi xnacl'
number_fluid_phases = 2
number_fluid_components = 3
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2sw]
type = CO2FluidProperties
[]
[co2]
type = TabulatedFluidProperties
fp = co2sw
fluid_property_file = 'fluid_properties.csv'
allow_fp_and_tabulation = true
error_on_out_of_bounds = false
[]
[water]
type = Water97FluidProperties
[]
[watertab]
type = TabulatedFluidProperties
fp = water
temperature_min = 273.15
temperature_max = 573.15
fluid_property_output_file = water_fluid_properties.csv
# Comment out the fp parameter and uncomment below to use the newly generated tabulation
# fluid_property_file = water_fluid_properties.csv
[]
[brine]
type = BrineFluidProperties
water_fp = watertab
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = 20
[]
[brineco2]
type = PorousFlowFluidState
gas_porepressure = pgas
z = zi
temperature_unit = Celsius
xnacl = xnacl
capillary_pressure = pc
fluid_state = fs
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.2
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm_water]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
s_res = 0.1
sum_s_res = 0.1
[]
[relperm_gas]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 1
[]
[]
[BCs]
[rightwater]
type = DirichletBC
boundary = right
value = 20e6
variable = pgas
[]
[]
[DiracKernels]
[source]
type = PorousFlowSquarePulsePointSource
point = '0 0 0'
mass_flux = 2
variable = zi
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
end_time = 1e5
[TimeStepper]
type = IterationAdaptiveDT
dt = 1
growth_factor = 1.5
[]
[]
[VectorPostprocessors]
[line]
type = LineValueSampler
warn_discontinuous_face_values = false
sort_by = x
start_point = '0 0 0'
end_point = '2000 0 0'
num_points = 10000
variable = 'pgas zi xnacl x1 saturation_gas'
execute_on = 'timestep_end'
[]
[]
[Postprocessors]
[pgas]
type = PointValue
point = '4 0 0'
variable = pgas
[]
[sgas]
type = PointValue
point = '4 0 0'
variable = saturation_gas
[]
[zi]
type = PointValue
point = '4 0 0'
variable = zi
[]
[massgas]
type = PorousFlowFluidMass
fluid_component = 1
[]
[x1]
type = PointValue
point = '4 0 0'
variable = x1
[]
[y0]
type = PointValue
point = '4 0 0'
variable = y0
[]
[xnacl]
type = PointValue
point = '4 0 0'
variable = xnacl
[]
[]
[Outputs]
print_linear_residuals = false
perf_graph = true
[csvout]
type = CSV
execute_on = timestep_end
execute_vector_postprocessors_on = final
[]
[]
(modules/porous_flow/test/tests/relperm/unity.i)
# Test perfectly mobile relative permeability curve by varying saturation over the mesh
[Mesh]
type = GeneratedMesh
dim = 1
nx = 20
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[p0]
initial_condition = 1e6
[]
[s1]
[]
[]
[AuxVariables]
[s0aux]
family = MONOMIAL
order = CONSTANT
[]
[s1aux]
family = MONOMIAL
order = CONSTANT
[]
[kr0aux]
family = MONOMIAL
order = CONSTANT
[]
[kr1aux]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[s0]
type = PorousFlowPropertyAux
property = saturation
phase = 0
variable = s0aux
[]
[s1]
type = PorousFlowPropertyAux
property = saturation
phase = 1
variable = s1aux
[]
[kr0]
type = PorousFlowPropertyAux
property = relperm
phase = 0
variable = kr0aux
[]
[kr1]
type = PorousFlowPropertyAux
property = relperm
phase = 1
variable = kr1aux
[]
[]
[Functions]
[s1]
type = ParsedFunction
expression = x
[]
[]
[ICs]
[s1]
type = FunctionIC
variable = s1
function = s1
[]
[]
[Kernels]
[p0]
type = Diffusion
variable = p0
[]
[s1]
type = Diffusion
variable = s1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'p0 s1'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = p0
phase1_saturation = s1
capillary_pressure = pc
[]
[kr0]
type = PorousFlowRelativePermeabilityConst
phase = 0
[]
[kr1]
type = PorousFlowRelativePermeabilityConst
phase = 1
[]
[]
[VectorPostprocessors]
[vpp]
type = LineValueSampler
warn_discontinuous_face_values = false
variable = 's0aux s1aux kr0aux kr1aux'
start_point = '0 0 0'
end_point = '1 0 0'
num_points = 20
sort_by = id
[]
[]
[Executioner]
type = Steady
solve_type = NEWTON
nl_abs_tol = 1e-8
[]
[BCs]
[sleft]
type = DirichletBC
variable = s1
value = 0
boundary = left
[]
[sright]
type = DirichletBC
variable = s1
value = 1
boundary = right
[]
[]
[Outputs]
csv = true
execute_on = timestep_end
[]
(modules/porous_flow/test/tests/heat_conduction/two_phase.i)
# 2phase heat conduction, with saturation fixed at 0.5
# apply a boundary condition of T=300 to a bar that
# is initially at T=200, and observe the expected
# error-function response
[Mesh]
type = GeneratedMesh
dim = 1
nx = 10
xmin = 0
xmax = 100
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[phase0_porepressure]
initial_condition = 0
[]
[phase1_saturation]
initial_condition = 0.5
[]
[temp]
initial_condition = 200
[]
[]
[Kernels]
[dummy_p0]
type = TimeDerivative
variable = phase0_porepressure
[]
[dummy_s1]
type = TimeDerivative
variable = phase1_saturation
[]
[energy_dot]
type = PorousFlowEnergyTimeDerivative
variable = temp
[]
[heat_conduction]
type = PorousFlowHeatConduction
variable = temp
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'temp phase0_porepressure phase1_saturation'
number_fluid_phases = 2
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[FluidProperties]
[simple_fluid0]
type = SimpleFluidProperties
bulk_modulus = 1.5
density0 = 0.4
thermal_expansion = 0
cv = 1
[]
[simple_fluid1]
type = SimpleFluidProperties
bulk_modulus = 0.5
density0 = 0.3
thermal_expansion = 0
cv = 2
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = temp
[]
[thermal_conductivity]
type = PorousFlowThermalConductivityIdeal
dry_thermal_conductivity = '0.3 0 0 0 0 0 0 0 0'
wet_thermal_conductivity = '1.7 0 0 0 0 0 0 0 0'
exponent = 1.0
aqueous_phase_number = 1
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = phase0_porepressure
phase1_saturation = phase1_saturation
capillary_pressure = pc
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.8
[]
[rock_heat]
type = PorousFlowMatrixInternalEnergy
specific_heat_capacity = 1.0
density = 0.25
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid0
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid1
phase = 1
[]
[]
[BCs]
[left]
type = DirichletBC
boundary = left
value = 300
variable = temp
[]
[]
[Preconditioning]
[andy]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1E1
end_time = 1E2
[]
[Postprocessors]
[t000]
type = PointValue
variable = temp
point = '0 0 0'
execute_on = 'initial timestep_end'
[]
[t010]
type = PointValue
variable = temp
point = '10 0 0'
execute_on = 'initial timestep_end'
[]
[t020]
type = PointValue
variable = temp
point = '20 0 0'
execute_on = 'initial timestep_end'
[]
[t030]
type = PointValue
variable = temp
point = '30 0 0'
execute_on = 'initial timestep_end'
[]
[t040]
type = PointValue
variable = temp
point = '40 0 0'
execute_on = 'initial timestep_end'
[]
[t050]
type = PointValue
variable = temp
point = '50 0 0'
execute_on = 'initial timestep_end'
[]
[t060]
type = PointValue
variable = temp
point = '60 0 0'
execute_on = 'initial timestep_end'
[]
[t070]
type = PointValue
variable = temp
point = '70 0 0'
execute_on = 'initial timestep_end'
[]
[t080]
type = PointValue
variable = temp
point = '80 0 0'
execute_on = 'initial timestep_end'
[]
[t090]
type = PointValue
variable = temp
point = '90 0 0'
execute_on = 'initial timestep_end'
[]
[t100]
type = PointValue
variable = temp
point = '100 0 0'
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
file_base = two_phase
[csv]
type = CSV
[]
exodus = false
[]
(modules/porous_flow/test/tests/poroperm/poro_thm.i)
# Test that porosity is correctly calculated.
# Porosity = biot + (phi0 - biot) * exp(-vol_strain + (biot - 1) / solid_bulk * (porepressure - ref_pressure) + thermal_exp_coeff * (temperature - ref_temperature))
# The parameters used are:
# biot = 0.7
# phi0 = 0.5
# vol_strain = 0.5
# solid_bulk = 0.3
# porepressure = 2
# ref_pressure = 3
# thermal_exp_coeff = 0.5
# temperature = 4
# ref_temperature = 3.5
# which yield porosity = 0.276599996677
[Mesh]
type = GeneratedMesh
dim = 3
[]
[GlobalParams]
PorousFlowDictator = dictator
displacements = 'disp_x disp_y disp_z'
biot_coefficient = 0.7
[]
[Variables]
[porepressure]
initial_condition = 2
[]
[temperature]
initial_condition = 4
[]
[disp_x]
[]
[disp_y]
[]
[disp_z]
[]
[]
[ICs]
[disp_x]
type = FunctionIC
function = '0.5 * x'
variable = disp_x
[]
[]
[Kernels]
[dummy_p]
type = TimeDerivative
variable = porepressure
[]
[dummy_t]
type = TimeDerivative
variable = temperature
[]
[dummy_x]
type = TimeDerivative
variable = disp_x
[]
[dummy_y]
type = TimeDerivative
variable = disp_y
[]
[dummy_z]
type = TimeDerivative
variable = disp_z
[]
[]
[AuxVariables]
[porosity]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[porosity]
type = PorousFlowPropertyAux
property = porosity
variable = porosity
[]
[]
[Postprocessors]
[porosity]
type = PointValue
variable = porosity
point = '0 0 0'
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure temperature'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = temperature
[]
[eff_fluid_pressure]
type = PorousFlowEffectiveFluidPressure
[]
[total_strain]
type = ComputeSmallStrain
[]
[vol_strain]
type = PorousFlowVolumetricStrain
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[porosity]
type = PorousFlowPorosity
mechanical = true
fluid = true
thermal = true
ensure_positive = false
porosity_zero = 0.5
solid_bulk = 0.3
thermal_expansion_coeff = 0.5
reference_porepressure = 3
reference_temperature = 3.5
[]
[]
[Executioner]
solve_type = Newton
type = Transient
num_steps = 1
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/chemistry/2species_equilibrium_2phase.i)
# Using a two-phase system (see 2species_equilibrium for the single-phase)
# The saturations, porosity, mass fractions, tortuosity and diffusion coefficients are chosen so that the results are identical to 2species_equilibrium
#
# PorousFlow analogy of chemical_reactions/test/tests/aqueous_equilibrium/2species.i
#
# Simple equilibrium reaction example to illustrate the use of PorousFlowMassFractionAqueousEquilibriumChemistry
#
# In this example, two primary species a and b are transported by diffusion and convection
# from the left of the porous medium, reacting to form two equilibrium species pa2 and pab
# according to the equilibrium reaction:
#
# reactions = '2a = pa2 rate = 10^2
# a + b = pab rate = 10^-2'
#
[Mesh]
type = GeneratedMesh
dim = 2
nx = 10
[]
[Variables]
[a]
order = FIRST
family = LAGRANGE
[InitialCondition]
type = BoundingBoxIC
x1 = 0.0
y1 = 0.0
x2 = 1.0e-10
y2 = 1
inside = 1.0e-2
outside = 1.0e-10
[]
[]
[b]
order = FIRST
family = LAGRANGE
[InitialCondition]
type = BoundingBoxIC
x1 = 0.0
y1 = 0.0
x2 = 1.0e-10
y2 = 1
inside = 1.0e-2
outside = 1.0e-10
[]
[]
[]
[AuxVariables]
[eqm_k0]
initial_condition = 1E2
[]
[eqm_k1]
initial_condition = 1E-2
[]
[pressure0]
[]
[saturation1]
initial_condition = 0.25
[]
[a_in_phase0]
initial_condition = 0.0
[]
[b_in_phase0]
initial_condition = 0.0
[]
[pa2]
family = MONOMIAL
order = CONSTANT
[]
[pab]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[pa2]
type = PorousFlowPropertyAux
property = secondary_concentration
secondary_species = 0
variable = pa2
[]
[pab]
type = PorousFlowPropertyAux
property = secondary_concentration
secondary_species = 1
variable = pab
[]
[]
[ICs]
[pressure0]
type = FunctionIC
variable = pressure0
function = 2-x
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Kernels]
[mass_a]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = a
[]
[flux_a]
type = PorousFlowAdvectiveFlux
variable = a
fluid_component = 0
[]
[diff_a]
type = PorousFlowDispersiveFlux
variable = a
fluid_component = 0
disp_trans = '0 0'
disp_long = '0 0'
[]
[mass_b]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = b
[]
[flux_b]
type = PorousFlowAdvectiveFlux
variable = b
fluid_component = 1
[]
[diff_b]
type = PorousFlowDispersiveFlux
variable = b
fluid_component = 1
disp_trans = '0 0'
disp_long = '0 0'
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'a b'
number_fluid_phases = 2
number_fluid_components = 3
number_aqueous_equilibrium = 2
aqueous_phase_number = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2e9 # huge, so mimic chemical_reactions
density0 = 1000
thermal_expansion = 0
viscosity = 1e-3
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
capillary_pressure = pc
phase0_porepressure = pressure0
phase1_saturation = saturation1
[]
[massfrac]
type = PorousFlowMassFractionAqueousEquilibriumChemistry
mass_fraction_vars = 'a_in_phase0 b_in_phase0 a b'
num_reactions = 2
equilibrium_constants = 'eqm_k0 eqm_k1'
primary_activity_coefficients = '1 1'
secondary_activity_coefficients = '1 1'
reactions = '2 0
1 1'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.8
[]
[permeability]
type = PorousFlowPermeabilityConst
# porous_flow permeability / porous_flow viscosity = chemical_reactions conductivity = 1E-4
permeability = '1E-7 0 0 0 1E-7 0 0 0 1E-7'
[]
[relp0]
type = PorousFlowRelativePermeabilityConst
phase = 0
[]
[relp1]
type = PorousFlowRelativePermeabilityConst
phase = 1
[]
[diff]
type = PorousFlowDiffusivityConst
# porous_flow diffusion_coeff * tortuousity * porosity = chemical_reactions diffusivity = 1E-4
diffusion_coeff = '5E-4 5E-4 5E-4
5E-4 5E-4 5E-4'
tortuosity = '0.25 0.25'
[]
[]
[BCs]
[a_left]
type = DirichletBC
variable = a
boundary = left
value = 1.0e-2
[]
[b_left]
type = DirichletBC
variable = b
boundary = left
value = 1.0e-2
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 10
end_time = 100
[]
[Outputs]
print_linear_residuals = true
exodus = true
perf_graph = true
[]
(modules/porous_flow/test/tests/chemistry/dissolution_limited_2phase.i)
# Using a two-phase system (see dissolution_limited.i for the single-phase)
# The saturation and porosity are chosen so that the results are identical to dissolution_limited.i
#
# The dissolution reaction, with limited initial mineral concentration
#
# a <==> mineral
#
# produces "mineral". Using mineral_density = fluid_density, theta = 1 = eta, the DE is
#
# a' = -(mineral / (porosity * saturation))' = rate * surf_area * molar_vol (1 - (1 / eqm_const) * (act_coeff * a)^stoi)
#
# The following parameters are used
#
# T_ref = 0.5 K
# T = 1 K
# activation_energy = 3 J/mol
# gas_constant = 6 J/(mol K)
# kinetic_rate_at_ref_T = 0.60653 mol/(m^2 s)
# These give rate = 0.60653 * exp(1/2) = 1 mol/(m^2 s)
#
# surf_area = 0.5 m^2/L
# molar_volume = 2 L/mol
# These give rate * surf_area * molar_vol = 1 s^-1
#
# equilibrium_constant = 0.5 (dimensionless)
# primary_activity_coefficient = 2 (dimensionless)
# stoichiometry = 1 (dimensionless)
# This means that 1 - (1 / eqm_const) * (act_coeff * a)^stoi = 1 - 4 a, which is positive for a < 0.25, ie dissolution for a(t=0) < 0.25
#
# The solution of the DE is
# a = eqm_const / act_coeff + (a(t=0) - eqm_const / act_coeff) exp(-rate * surf_area * molar_vol * act_coeff * t / eqm_const)
# = 0.25 + (a(t=0) - 0.25) exp(-4 * t)
# c = c(t=0) - (a - a(t=0)) * porosity * saturation
#
# However, c(t=0) is small, so that the reaction only works until c=0, then a and c both remain fixed
#
# This test checks that (a + c / (porosity * saturation)) is time-independent, and that a follows the above solution, until c=0 and thereafter remains fixed.
#
# Aside:
# The exponential curve is not followed exactly because moose actually solves
# (a - a_old)/dt = rate * surf_area * molar_vol (1 - (1 / eqm_const) * (act_coeff * a)^stoi)
# which does not give an exponential exactly, except in the limit dt->0
[Mesh]
type = GeneratedMesh
dim = 1
[]
[Variables]
[a]
initial_condition = 0.05
[]
[]
[AuxVariables]
[eqm_k]
initial_condition = 0.5
[]
[pressure0]
[]
[saturation1]
initial_condition = 0.25
[]
[b]
initial_condition = 0.123
[]
[ini_mineral_conc]
initial_condition = 0.015
[]
[mineral]
family = MONOMIAL
order = CONSTANT
[]
[should_be_static]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[mineral]
type = PorousFlowPropertyAux
property = mineral_concentration
mineral_species = 0
variable = mineral
[]
[should_be_static]
type = ParsedAux
coupled_variables = 'mineral a'
expression = 'a + mineral / 0.1'
variable = should_be_static
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Kernels]
[mass_a]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = a
[]
[pre_dis]
type = PorousFlowPreDis
variable = a
mineral_density = 1000
stoichiometry = 1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = a
number_fluid_phases = 2
number_fluid_components = 2
number_aqueous_kinetic = 1
aqueous_phase_number = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2e9 # huge, so mimic chemical_reactions
density0 = 1000
thermal_expansion = 0
viscosity = 1e-3
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = 1
[]
[ppss]
type = PorousFlow2PhasePS
capillary_pressure = pc
phase0_porepressure = pressure0
phase1_saturation = saturation1
[]
[mass_frac]
type = PorousFlowMassFraction
mass_fraction_vars = 'b a'
[]
[predis]
type = PorousFlowAqueousPreDisChemistry
primary_concentrations = a
num_reactions = 1
equilibrium_constants = eqm_k
primary_activity_coefficients = 2
reactions = 1
specific_reactive_surface_area = 0.5
kinetic_rate_constant = 0.6065306597126334
activation_energy = 3
molar_volume = 2
gas_constant = 6
reference_temperature = 0.5
[]
[mineral_conc]
type = PorousFlowAqueousPreDisMineral
initial_concentrations = ini_mineral_conc
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.4
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
nl_abs_tol = 1E-10
dt = 0.01
end_time = 1
[]
[Postprocessors]
[a]
type = PointValue
point = '0 0 0'
variable = a
[]
[should_be_static]
type = PointValue
point = '0 0 0'
variable = should_be_static
[]
[]
[Outputs]
time_step_interval = 10
csv = true
perf_graph = true
[]
(modules/porous_flow/test/tests/poroperm/poro_tm.i)
# Test that porosity is correctly calculated.
# Porosity = 1 + (phi0 - 1) * exp(-vol_strain + thermal_exp_coeff * (temperature - ref_temperature))
# The parameters used are:
# phi0 = 0.5
# vol_strain = 0.5
# thermal_exp_coeff = 0.5
# temperature = 4
# ref_temperature = 3.5
# which yield porosity = 0.610599608464
[Mesh]
type = GeneratedMesh
dim = 3
[]
[GlobalParams]
PorousFlowDictator = dictator
displacements = 'disp_x disp_y disp_z'
[]
[Variables]
[porepressure]
initial_condition = 2
[]
[temperature]
initial_condition = 4
[]
[disp_x]
[]
[disp_y]
[]
[disp_z]
[]
[]
[ICs]
[disp_x]
type = FunctionIC
function = '0.5 * x'
variable = disp_x
[]
[]
[Kernels]
[dummy_p]
type = TimeDerivative
variable = porepressure
[]
[dummy_t]
type = TimeDerivative
variable = temperature
[]
[dummy_x]
type = TimeDerivative
variable = disp_x
[]
[dummy_y]
type = TimeDerivative
variable = disp_y
[]
[dummy_z]
type = TimeDerivative
variable = disp_z
[]
[]
[AuxVariables]
[porosity]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[porosity]
type = PorousFlowPropertyAux
property = porosity
variable = porosity
[]
[]
[Postprocessors]
[porosity]
type = PointValue
variable = porosity
point = '0 0 0'
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure temperature'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = temperature
[]
[eff_fluid_pressure]
type = PorousFlowEffectiveFluidPressure
[]
[total_strain]
type = ComputeSmallStrain
[]
[vol_strain]
type = PorousFlowVolumetricStrain
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[porosity]
type = PorousFlowPorosity
mechanical = true
thermal = true
ensure_positive = false
porosity_zero = 0.5
thermal_expansion_coeff = 0.5
reference_temperature = 3.5
[]
[]
[Executioner]
solve_type = Newton
type = Transient
num_steps = 1
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/fluidstate/brineco2_nonisothermal.i)
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 2
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pgas]
initial_condition = 20e6
[]
[z]
initial_condition = 0.2
[]
[temperature]
initial_condition = 70
[]
[]
[AuxVariables]
[xnacl]
initial_condition = 0.1
[]
[pressure_gas]
order = CONSTANT
family = MONOMIAL
[]
[pressure_water]
order = CONSTANT
family = MONOMIAL
[]
[saturation_gas]
order = CONSTANT
family = MONOMIAL
[]
[saturation_water]
order = CONSTANT
family = MONOMIAL
[]
[density_water]
order = CONSTANT
family = MONOMIAL
[]
[density_gas]
order = CONSTANT
family = MONOMIAL
[]
[viscosity_water]
order = CONSTANT
family = MONOMIAL
[]
[viscosity_gas]
order = CONSTANT
family = MONOMIAL
[]
[enthalpy_water]
order = CONSTANT
family = MONOMIAL
[]
[enthalpy_gas]
order = CONSTANT
family = MONOMIAL
[]
[internal_energy_water]
order = CONSTANT
family = MONOMIAL
[]
[internal_energy_gas]
order = CONSTANT
family = MONOMIAL
[]
[x0_water]
order = CONSTANT
family = MONOMIAL
[]
[x0_gas]
order = CONSTANT
family = MONOMIAL
[]
[x1_water]
order = CONSTANT
family = MONOMIAL
[]
[x1_gas]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[pressure_water]
type = PorousFlowPropertyAux
variable = pressure_water
property = pressure
phase = 0
execute_on = timestep_end
[]
[pressure_gas]
type = PorousFlowPropertyAux
variable = pressure_gas
property = pressure
phase = 1
execute_on = timestep_end
[]
[saturation_water]
type = PorousFlowPropertyAux
variable = saturation_water
property = saturation
phase = 0
execute_on = timestep_end
[]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = timestep_end
[]
[density_water]
type = PorousFlowPropertyAux
variable = density_water
property = density
phase = 0
execute_on = timestep_end
[]
[density_gas]
type = PorousFlowPropertyAux
variable = density_gas
property = density
phase = 1
execute_on = timestep_end
[]
[viscosity_water]
type = PorousFlowPropertyAux
variable = viscosity_water
property = viscosity
phase = 0
execute_on = timestep_end
[]
[viscosity_gas]
type = PorousFlowPropertyAux
variable = viscosity_gas
property = viscosity
phase = 1
execute_on = timestep_end
[]
[enthalpy_water]
type = PorousFlowPropertyAux
variable = enthalpy_water
property = enthalpy
phase = 0
execute_on = timestep_end
[]
[enthalpy_gas]
type = PorousFlowPropertyAux
variable = enthalpy_gas
property = enthalpy
phase = 1
execute_on = timestep_end
[]
[internal_energy_water]
type = PorousFlowPropertyAux
variable = internal_energy_water
property = internal_energy
phase = 0
execute_on = timestep_end
[]
[internal_energy_gas]
type = PorousFlowPropertyAux
variable = internal_energy_gas
property = internal_energy
phase = 1
execute_on = timestep_end
[]
[x1_water]
type = PorousFlowPropertyAux
variable = x1_water
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = timestep_end
[]
[x1_gas]
type = PorousFlowPropertyAux
variable = x1_gas
property = mass_fraction
phase = 1
fluid_component = 1
execute_on = timestep_end
[]
[x0_water]
type = PorousFlowPropertyAux
variable = x0_water
property = mass_fraction
phase = 0
fluid_component = 0
execute_on = timestep_end
[]
[x0_gas]
type = PorousFlowPropertyAux
variable = x0_gas
property = mass_fraction
phase = 1
fluid_component = 0
execute_on = timestep_end
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
variable = pgas
fluid_component = 0
[]
[mass1]
type = PorousFlowMassTimeDerivative
variable = z
fluid_component = 1
[]
[heat]
type = TimeDerivative
variable = temperature
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas z temperature'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2]
type = CO2FluidProperties
[]
[brine]
type = BrineFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[brineco2]
type = PorousFlowFluidState
gas_porepressure = pgas
z = z
temperature = temperature
temperature_unit = Celsius
xnacl = xnacl
capillary_pressure = pc
fluid_state = fs
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm0]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[relperm1]
type = PorousFlowRelativePermeabilityCorey
n = 3
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
dt = 1
end_time = 1
nl_abs_tol = 1e-12
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Postprocessors]
[density_water]
type = ElementIntegralVariablePostprocessor
variable = density_water
[]
[density_gas]
type = ElementIntegralVariablePostprocessor
variable = density_gas
[]
[viscosity_water]
type = ElementIntegralVariablePostprocessor
variable = viscosity_water
[]
[viscosity_gas]
type = ElementIntegralVariablePostprocessor
variable = viscosity_gas
[]
[enthalpy_water]
type = ElementIntegralVariablePostprocessor
variable = enthalpy_water
[]
[enthalpy_gas]
type = ElementIntegralVariablePostprocessor
variable = enthalpy_gas
[]
[internal_energy_water]
type = ElementIntegralVariablePostprocessor
variable = internal_energy_water
[]
[internal_energy_gas]
type = ElementIntegralVariablePostprocessor
variable = internal_energy_gas
[]
[x1_water]
type = ElementIntegralVariablePostprocessor
variable = x1_water
[]
[x0_water]
type = ElementIntegralVariablePostprocessor
variable = x0_water
[]
[x1_gas]
type = ElementIntegralVariablePostprocessor
variable = x1_gas
[]
[x0_gas]
type = ElementIntegralVariablePostprocessor
variable = x0_gas
[]
[sg]
type = ElementIntegralVariablePostprocessor
variable = saturation_gas
[]
[sw]
type = ElementIntegralVariablePostprocessor
variable = saturation_water
[]
[pwater]
type = ElementIntegralVariablePostprocessor
variable = pressure_water
[]
[pgas]
type = ElementIntegralVariablePostprocessor
variable = pressure_gas
[]
[x0mass]
type = PorousFlowFluidMass
fluid_component = 0
phase = '0 1'
[]
[x1mass]
type = PorousFlowFluidMass
fluid_component = 1
phase = '0 1'
[]
[]
[Outputs]
csv = true
execute_on = timestep_end
[]
(modules/porous_flow/test/tests/mass_conservation/mass06.i)
# Checking that the mass postprocessor correctly calculates the mass
# of each component in each phase, as well as the total mass of each
# component in all phases. Also tests that optional saturation threshold
# gives the correct mass
# 2phase, 2component, constant porosity
# saturation_threshold set to 0.6 for phase 1
[Mesh]
type = GeneratedMesh
dim = 1
nx = 10
xmin = 0
xmax = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pp]
[]
[sat]
[]
[]
[AuxVariables]
[massfrac_ph0_sp0]
initial_condition = 1
[]
[massfrac_ph1_sp0]
initial_condition = 0
[]
[]
[ICs]
[pinit]
type = ConstantIC
value = 1
variable = pp
[]
[satinit]
type = FunctionIC
function = 1-x
variable = sat
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = sat
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp sat'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[FluidProperties]
[simple_fluid0]
type = SimpleFluidProperties
bulk_modulus = 1
density0 = 1
thermal_expansion = 0
[]
[simple_fluid1]
type = SimpleFluidProperties
bulk_modulus = 1
density0 = 0.1
thermal_expansion = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = pp
phase1_saturation = sat
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid0
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid1
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[]
[Postprocessors]
[comp0_phase0_mass]
type = PorousFlowFluidMass
fluid_component = 0
phase = 0
[]
[comp0_phase1_mass]
type = PorousFlowFluidMass
fluid_component = 0
phase = 1
[]
[comp0_total_mass]
type = PorousFlowFluidMass
fluid_component = 0
[]
[comp1_phase0_mass]
type = PorousFlowFluidMass
fluid_component = 1
phase = 0
[]
[comp1_phase1_mass]
type = PorousFlowFluidMass
fluid_component = 1
phase = 1
[]
[comp1_total_mass]
type = PorousFlowFluidMass
fluid_component = 1
[]
[comp1_phase1_threshold_mass]
type = PorousFlowFluidMass
fluid_component = 1
phase = 1
saturation_threshold = 0.6
[]
[]
[Executioner]
type = Transient
solve_type = Newton
nl_abs_tol = 1e-16
dt = 1
end_time = 1
[]
[Outputs]
execute_on = 'timestep_end'
file_base = mass06
csv = true
[]
(modules/porous_flow/test/tests/jacobian/basic_advection1.i)
# Basic advection with no PorousFlow variables
[Mesh]
type = GeneratedMesh
dim = 1
nx = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[u]
[]
[]
[AuxVariables]
[P]
[]
[]
[ICs]
[P]
type = FunctionIC
variable = P
function = '2*(1-x)'
[]
[u]
type = RandomIC
variable = u
[]
[]
[Kernels]
[u_advection]
type = PorousFlowBasicAdvection
variable = u
phase = 0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = ''
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 4
thermal_expansion = 0
viscosity = 150.0
[]
[]
[Materials]
[temperature_qp]
type = PorousFlowTemperature
[]
[ppss_qp]
type = PorousFlow1PhaseP
porepressure = P
capillary_pressure = pc
[]
[simple_fluid_qp]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '5 0 0 0 5 0 0 0 5'
[]
[relperm_qp]
type = PorousFlowRelativePermeabilityCorey
n = 0
phase = 0
[]
[darcy_velocity_qp]
type = PorousFlowDarcyVelocityMaterial
gravity = '0.25 0 0'
[]
[]
[Preconditioning]
[check]
type = SMP
full = true
#petsc_options = '-snes_test_display'
petsc_options_iname = '-snes_type'
petsc_options_value = ' test'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
end_time = 1
[]
(modules/porous_flow/test/tests/aux_kernels/darcy_velocity_lower_2D.i)
# checking that the PorousFlowDarcyVelocityComponentLowerDimensional AuxKernel works as expected in 1D+2D situation
# for the fully-saturated case (relative-permeability = 1)
# The 1_frac_in_2D_example.e has size 0.3x0.2x0, and a fracture running through its
# centre, with normal = (0, 1, 0)
# Porepressure is initialised to grad(P) = (1, 2, 0)
# Fluid_density = 2
# viscosity = 10
# relative_permeability = 1
# permeability = (5, 5, 5) (in the bulk, measured in m^2)
# permeability = (10, 10, 10) (in the fracture, measured in m^3)
# aperture = 0.01
# gravity = (1, 0.5, 0)
# So Darcy velocity in the bulk = (0.5, -0.5, 0)
# in the fracture grad(P) = (1, 0, 0)
# In the fracture the projected gravity vector is
# tangential_gravity = (1, 0, 0)
# So the Darcy velocity in the fracture = (100, 0, 0)
[Mesh]
type = FileMesh
file = 1_frac_in_2D_example.e
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '1 0.5 0'
[]
[Variables]
[pp]
[]
[]
[ICs]
[pinit]
type = FunctionIC
function = 'x+2*y'
variable = pp
[]
[]
[Kernels]
[dummy]
type = TimeDerivative
variable = pp
[]
[]
[AuxVariables]
[bulk_vel_x]
order = CONSTANT
family = MONOMIAL
block = '2 3'
[]
[bulk_vel_y]
order = CONSTANT
family = MONOMIAL
block = '2 3'
[]
[bulk_vel_z]
order = CONSTANT
family = MONOMIAL
block = '2 3'
[]
[fracture_vel_x]
order = CONSTANT
family = MONOMIAL
block = 1
[]
[fracture_vel_y]
order = CONSTANT
family = MONOMIAL
block = 1
[]
[fracture_vel_z]
order = CONSTANT
family = MONOMIAL
block = 1
[]
[]
[AuxKernels]
[bulk_vel_x]
type = PorousFlowDarcyVelocityComponent
variable = bulk_vel_x
component = x
fluid_phase = 0
[]
[bulk_vel_y]
type = PorousFlowDarcyVelocityComponent
variable = bulk_vel_y
component = y
fluid_phase = 0
[]
[bulk_vel_z]
type = PorousFlowDarcyVelocityComponent
variable = bulk_vel_z
component = z
fluid_phase = 0
[]
[fracture_vel_x]
type = PorousFlowDarcyVelocityComponentLowerDimensional
variable = fracture_vel_x
component = x
fluid_phase = 0
aperture = 0.01
[]
[fracture_vel_y]
type = PorousFlowDarcyVelocityComponentLowerDimensional
variable = fracture_vel_y
component = y
fluid_phase = 0
aperture = 0.01
[]
[fracture_vel_z]
type = PorousFlowDarcyVelocityComponentLowerDimensional
variable = fracture_vel_z
component = z
fluid_phase = 0
aperture = 0.01
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 1E16
viscosity = 10
density0 = 2
thermal_expansion = 0
[]
[]
[Postprocessors]
[bulk_vel_x]
type = PointValue
variable = bulk_vel_x
point = '0 -0.05 0'
[]
[bulk_vel_y]
type = PointValue
variable = bulk_vel_y
point = '0 -0.05 0'
[]
[bulk_vel_z]
type = PointValue
variable = bulk_vel_z
point = '0 -0.05 0'
[]
[fracture_vel_x]
type = PointValue
point = '0 0 0'
variable = fracture_vel_x
[]
[fracture_vel_y]
type = PointValue
point = '0 0 0'
variable = fracture_vel_y
[]
[fracture_vel_z]
type = PointValue
point = '0 0 0'
variable = fracture_vel_z
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = pp
capillary_pressure = pc
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '5 0 0 0 5 0 0 0 5'
block = '2 3'
[]
[permeability_fracture]
type = PorousFlowPermeabilityConst
permeability = '10 0 0 0 10 0 0 0 10'
block = 1
[]
[relperm]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[]
[Executioner]
type = Transient
dt = 1
end_time = 1
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/basic_advection/except1.i)
# phase number is too high in PorousFlowBasicAdvection
[Mesh]
type = GeneratedMesh
dim = 1
nx = 100
xmin = 0
xmax = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[u]
[]
[]
[AuxVariables]
[P]
[]
[]
[ICs]
[P]
type = FunctionIC
variable = P
function = '2*(1-x)'
[]
[u]
type = FunctionIC
variable = u
function = 'if(x<0.1,1,0)'
[]
[]
[Kernels]
[u_dot]
type = TimeDerivative
variable = u
[]
[u_advection]
type = PorousFlowBasicAdvection
variable = u
phase = 1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = ''
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 4
thermal_expansion = 0
viscosity = 150.0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = P
capillary_pressure = pc
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '5 0 0 0 5 0 0 0 5'
[]
[relperm]
type = PorousFlowRelativePermeabilityCorey
n = 0
phase = 0
[]
[darcy_velocity]
type = PorousFlowDarcyVelocityMaterial
gravity = '0.25 0 0'
[]
[]
[BCs]
[left]
type = DirichletBC
boundary = left
value = 1
variable = u
[]
[right]
type = DirichletBC
boundary = right
value = 0
variable = u
[]
[]
[Preconditioning]
[basic]
type = SMP
full = true
petsc_options_iname = '-pc_type -snes_rtol'
petsc_options_value = ' lu 1E-10'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 5
[]
[Outputs]
exodus = true
print_linear_residuals = false
[]
(modules/porous_flow/test/tests/jacobian/diff03.i)
# Test the Jacobian of the diffusive component of the PorousFlowDisperiveFlux kernel for two phases.
# By setting disp_long and disp_trans to zero, the purely diffusive component of the flux
# can be isolated. Uses saturation-dependent tortuosity and diffusion coefficients from the
# Millington-Quirk model
[Mesh]
type = GeneratedMesh
dim = 2
nx = 3
xmin = 0
xmax = 1
ny = 1
ymin = 0
ymax = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[sgas]
[]
[massfrac0]
[]
[]
[AuxVariables]
[massfrac1]
[]
[]
[ICs]
[sgas]
type = RandomIC
variable = sgas
max = 1
min = 0
[]
[massfrac0]
type = RandomIC
variable = massfrac0
min = 0
max = 1
[]
[massfrac1]
type = RandomIC
variable = massfrac1
min = 0
max = 1
[]
[]
[Kernels]
[diff0]
type = PorousFlowDispersiveFlux
fluid_component = 0
variable = sgas
gravity = '1 0 0'
disp_long = '0 0'
disp_trans = '0 0'
[]
[diff1]
type = PorousFlowDispersiveFlux
fluid_component = 1
variable = massfrac0
gravity = '1 0 0'
disp_long = '0 0'
disp_trans = '0 0'
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'sgas massfrac0'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[FluidProperties]
[simple_fluid0]
type = SimpleFluidProperties
bulk_modulus = 1e7
density0 = 10
thermal_expansion = 0
viscosity = 1
[]
[simple_fluid1]
type = SimpleFluidProperties
bulk_modulus = 1e7
density0 = 1
thermal_expansion = 0
viscosity = 0.1
[]
[]
[Materials]
[temp]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = 1
phase1_saturation = sgas
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac0 massfrac1'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid0
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid1
phase = 1
[]
[poro]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[diff]
type = PorousFlowDiffusivityMillingtonQuirk
diffusion_coeff = '1e-2 1e-1 1e-2 1e-1'
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1 0 0 0 2 0 0 0 3'
[]
[relperm0]
type = PorousFlowRelativePermeabilityConst
phase = 0
[]
[relperm1]
type = PorousFlowRelativePermeabilityConst
phase = 1
[]
[]
[Preconditioning]
active = smp
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 1
[]
[Outputs]
exodus = false
[]
(modules/porous_flow/test/tests/flux_limited_TVD_pflow/pffltvd_1D_adaptivity.i)
# Using flux-limited TVD advection ala Kuzmin and Turek, mploying PorousFlow Kernels and UserObjects, with superbee flux-limiter
# 1D version with adaptivity
[Mesh]
type = GeneratedMesh
dim = 1
nx = 10
xmin = 0
xmax = 1
[]
[Adaptivity]
initial_steps = 1
initial_marker = tracer_marker
marker = tracer_marker
max_h_level = 1
[Markers]
[tracer_marker]
type = ValueRangeMarker
variable = tracer
lower_bound = 0.02
upper_bound = 0.98
[]
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[porepressure]
[]
[tracer]
[]
[]
[ICs]
[porepressure]
type = FunctionIC
variable = porepressure
function = '1 - x'
[]
[tracer]
type = FunctionIC
variable = tracer
function = 'if(x<0.1,0,if(x>0.3,0,1))'
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = tracer
[]
[flux0]
type = PorousFlowFluxLimitedTVDAdvection
variable = tracer
advective_flux_calculator = advective_flux_calculator_0
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = porepressure
[]
[flux1]
type = PorousFlowFluxLimitedTVDAdvection
variable = porepressure
advective_flux_calculator = advective_flux_calculator_1
[]
[]
[BCs]
[constant_injection_porepressure]
type = DirichletBC
variable = porepressure
value = 1
boundary = left
[]
[no_tracer_on_left]
type = DirichletBC
variable = tracer
value = 0
boundary = left
[]
[remove_component_1]
type = PorousFlowPiecewiseLinearSink
variable = porepressure
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 1
use_mobility = true
flux_function = 1E3
[]
[remove_component_0]
type = PorousFlowPiecewiseLinearSink
variable = tracer
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 0
use_mobility = true
flux_function = 1E3
[]
[]
[FluidProperties]
[the_simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2E9
thermal_expansion = 0
viscosity = 1.0
density0 = 1000.0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure tracer'
number_fluid_phases = 1
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[advective_flux_calculator_0]
type = PorousFlowAdvectiveFluxCalculatorSaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 0
[]
[advective_flux_calculator_1]
type = PorousFlowAdvectiveFluxCalculatorSaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 1
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = tracer
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = the_simple_fluid
phase = 0
[]
[relperm]
type = PorousFlowRelativePermeabilityConst
phase = 0
[]
[porosity]
type = PorousFlowPorosity
porosity_zero = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1E-2 0 0 0 1E-2 0 0 0 1E-2'
[]
[]
[Preconditioning]
active = basic
[basic]
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 lu NONZERO 2'
[]
[preferred_but_might_not_be_installed]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_mat_solver_package'
petsc_options_value = ' lu mumps'
[]
[]
[VectorPostprocessors]
[tracer]
type = LineValueSampler
start_point = '0 0 0'
end_point = '1 0 0'
num_points = 11
sort_by = x
variable = tracer
[]
[]
[Executioner]
type = Transient
solve_type = Newton
end_time = 6
dt = 6E-2
nl_abs_tol = 1E-8
timestep_tolerance = 1E-3
[]
[Outputs]
[out]
type = CSV
execute_on = final
[]
[]
(modules/porous_flow/test/tests/flux_limited_TVD_pflow/pffltvd_1D.i)
# Using flux-limited TVD advection ala Kuzmin and Turek, mploying PorousFlow Kernels and UserObjects, with superbee flux-limiter
# 1D version
[Mesh]
type = GeneratedMesh
dim = 1
nx = 10
xmin = 0
xmax = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[porepressure]
[]
[tracer]
[]
[]
[ICs]
[porepressure]
type = FunctionIC
variable = porepressure
function = '1 - x'
[]
[tracer]
type = FunctionIC
variable = tracer
function = 'if(x<0.1,0,if(x>0.3,0,1))'
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = tracer
[]
[flux0]
type = PorousFlowFluxLimitedTVDAdvection
variable = tracer
advective_flux_calculator = advective_flux_calculator_0
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = porepressure
[]
[flux1]
type = PorousFlowFluxLimitedTVDAdvection
variable = porepressure
advective_flux_calculator = advective_flux_calculator_1
[]
[]
[BCs]
[constant_injection_porepressure]
type = DirichletBC
variable = porepressure
value = 1
boundary = left
[]
[no_tracer_on_left]
type = DirichletBC
variable = tracer
value = 0
boundary = left
[]
[remove_component_1]
type = PorousFlowPiecewiseLinearSink
variable = porepressure
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 1
use_mobility = true
flux_function = 1E3
[]
[remove_component_0]
type = PorousFlowPiecewiseLinearSink
variable = tracer
boundary = right
fluid_phase = 0
pt_vals = '0 1E3'
multipliers = '0 1E3'
mass_fraction_component = 0
use_mobility = true
flux_function = 1E3
[]
[]
[FluidProperties]
[the_simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2E9
thermal_expansion = 0
viscosity = 1.0
density0 = 1000.0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure tracer'
number_fluid_phases = 1
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[advective_flux_calculator_0]
type = PorousFlowAdvectiveFluxCalculatorSaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 0
[]
[advective_flux_calculator_1]
type = PorousFlowAdvectiveFluxCalculatorSaturatedMultiComponent
flux_limiter_type = superbee
fluid_component = 1
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = tracer
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = the_simple_fluid
phase = 0
[]
[relperm]
type = PorousFlowRelativePermeabilityConst
phase = 0
[]
[porosity]
type = PorousFlowPorosity
porosity_zero = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1E-2 0 0 0 1E-2 0 0 0 1E-2'
[]
[]
[Preconditioning]
active = basic
[basic]
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 lu NONZERO 2'
[]
[preferred_but_might_not_be_installed]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_mat_solver_package'
petsc_options_value = ' lu mumps'
[]
[]
[VectorPostprocessors]
[tracer]
type = LineValueSampler
start_point = '0 0 0'
end_point = '1 0 0'
num_points = 11
sort_by = x
variable = tracer
[]
[]
[Executioner]
type = Transient
solve_type = Newton
end_time = 6
dt = 6E-2
nl_abs_tol = 1E-8
timestep_tolerance = 1E-3
[]
[Outputs]
[out]
type = CSV
execute_on = final
[]
[]
(modules/porous_flow/test/tests/sinks/s12.i)
# The PorousFlowEnthalpy sink adds heat energy corresponding to injecting a 1kg/s/m^2 (flux_function = -1)
# of fluid at pressure 0.5 (given by the AuxVariable p_aux) and the input temperature is 300 (given by the T_in parameter).
# SimpleFluidProperties are used, with density0 = 10, bulk_modulus = 1, thermal_expansion = 0, and cv = 1E-4
# density = 10 * exp(0.5 / 1 + 0) = 16.4872
# internal energy = 1E-4 * 300 = 0.03
# enthalpy = 0.03 + 0.5/16.3872 = 0.0603265
# This is applied over an area of 100, so the total energy flux is 6.03265 J/s.
# This the the rate of change of the heat energy reported by the PorousFlowHeatEnergy Postprocessor
[Mesh]
type = GeneratedMesh
dim = 3
nx = 2
ny = 2
nz = 2
xmin = 0
xmax = 10
ymin = 0
ymax = 10
zmin = 0
zmax = 10
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp temp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[AuxVariables]
[p_aux]
initial_condition = 0.5
[]
[]
[Variables]
[pp]
initial_condition = 1
[]
[temp]
initial_condition = 2
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[heat_conduction]
type = PorousFlowEnergyTimeDerivative
variable = temp
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 1
density0 = 10
thermal_expansion = 0
cv = 1E-4
[]
[]
[Materials]
[ppss]
type = PorousFlow1PhaseFullySaturated
porepressure = pp
[]
[massfrac]
type = PorousFlowMassFraction
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[temperature]
type = PorousFlowTemperature
temperature = temp
[]
[heat]
type = PorousFlowMatrixInternalEnergy
specific_heat_capacity = 2
density = 3
[]
[]
[BCs]
[left_p]
type = PorousFlowSink
variable = pp
boundary = left
flux_function = -1
[]
[left_T]
type = PorousFlowEnthalpySink
variable = temp
boundary = left
T_in = 300
fp = simple_fluid
flux_function = -1
porepressure_var = p_aux
[]
[]
[Postprocessors]
[total_heat_energy]
type = PorousFlowHeatEnergy
phase = 0
[]
[]
[Preconditioning]
[andy]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 0.25
num_steps = 2
[]
[Outputs]
file_base = s12
[csv]
type = CSV
[]
[]
(modules/porous_flow/test/tests/fluidstate/brineco2_2.i)
# Injection of supercritical CO2 into a single brine saturated cell. The CO2 initially fully
# dissolves into the brine, increasing its density slightly. After a few time steps,
# the brine is saturated with CO2, and subsequently a supercritical gas phase of CO2 saturated
# with a small amount of H2O is formed. Salt is included as a nonlinear variable.
[Mesh]
type = GeneratedMesh
dim = 2
[]
[GlobalParams]
PorousFlowDictator = dictator
temperature = 30
[]
[Variables]
[pgas]
initial_condition = 20e6
[]
[z]
[]
[xnacl]
initial_condition = 0.1
[]
[]
[DiracKernels]
[source]
type = PorousFlowSquarePulsePointSource
variable = z
point = '0.5 0.5 0'
mass_flux = 2
[]
[]
[BCs]
[left]
type = DirichletBC
value = 20e6
variable = pgas
boundary = left
[]
[right]
type = DirichletBC
value = 20e6
variable = pgas
boundary = right
[]
[]
[AuxVariables]
[pressure_gas]
order = CONSTANT
family = MONOMIAL
[]
[pressure_water]
order = CONSTANT
family = MONOMIAL
[]
[saturation_gas]
order = CONSTANT
family = MONOMIAL
[]
[saturation_water]
order = CONSTANT
family = MONOMIAL
[]
[density_water]
order = CONSTANT
family = MONOMIAL
[]
[density_gas]
order = CONSTANT
family = MONOMIAL
[]
[viscosity_water]
order = CONSTANT
family = MONOMIAL
[]
[viscosity_gas]
order = CONSTANT
family = MONOMIAL
[]
[x0_water]
order = CONSTANT
family = MONOMIAL
[]
[x0_gas]
order = CONSTANT
family = MONOMIAL
[]
[x1_water]
order = CONSTANT
family = MONOMIAL
[]
[x1_gas]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[pressure_water]
type = PorousFlowPropertyAux
variable = pressure_water
property = pressure
phase = 0
execute_on = 'initial timestep_end'
[]
[pressure_gas]
type = PorousFlowPropertyAux
variable = pressure_gas
property = pressure
phase = 1
execute_on = 'initial timestep_end'
[]
[saturation_water]
type = PorousFlowPropertyAux
variable = saturation_water
property = saturation
phase = 0
execute_on = 'initial timestep_end'
[]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = 'initial timestep_end'
[]
[density_water]
type = PorousFlowPropertyAux
variable = density_water
property = density
phase = 0
execute_on = 'initial timestep_end'
[]
[density_gas]
type = PorousFlowPropertyAux
variable = density_gas
property = density
phase = 1
execute_on = 'initial timestep_end'
[]
[viscosity_water]
type = PorousFlowPropertyAux
variable = viscosity_water
property = viscosity
phase = 0
execute_on = 'initial timestep_end'
[]
[viscosity_gas]
type = PorousFlowPropertyAux
variable = viscosity_gas
property = viscosity
phase = 1
execute_on = 'initial timestep_end'
[]
[x1_water]
type = PorousFlowPropertyAux
variable = x1_water
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = 'initial timestep_end'
[]
[x1_gas]
type = PorousFlowPropertyAux
variable = x1_gas
property = mass_fraction
phase = 1
fluid_component = 1
execute_on = 'initial timestep_end'
[]
[x0_water]
type = PorousFlowPropertyAux
variable = x0_water
property = mass_fraction
phase = 0
fluid_component = 0
execute_on = 'initial timestep_end'
[]
[x0_gas]
type = PorousFlowPropertyAux
variable = x0_gas
property = mass_fraction
phase = 1
fluid_component = 0
execute_on = 'initial timestep_end'
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
variable = pgas
fluid_component = 0
[]
[mass1]
type = PorousFlowMassTimeDerivative
variable = z
fluid_component = 1
[]
[mass2]
type = PorousFlowMassTimeDerivative
variable = xnacl
fluid_component = 2
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas z xnacl'
number_fluid_phases = 2
number_fluid_components = 3
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowBrineCO2
brine_fp = brine
co2_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2]
type = CO2FluidProperties
[]
[brine]
type = BrineFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[brineco2]
type = PorousFlowFluidState
gas_porepressure = pgas
z = z
temperature_unit = Celsius
xnacl = xnacl
capillary_pressure = pc
fluid_state = fs
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm0]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[relperm1]
type = PorousFlowRelativePermeabilityCorey
n = 3
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
dt = 1
end_time = 10
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Postprocessors]
[density_water]
type = ElementIntegralVariablePostprocessor
variable = density_water
execute_on = 'initial timestep_end'
[]
[density_gas]
type = ElementIntegralVariablePostprocessor
variable = density_gas
execute_on = 'initial timestep_end'
[]
[viscosity_water]
type = ElementIntegralVariablePostprocessor
variable = viscosity_water
execute_on = 'initial timestep_end'
[]
[viscosity_gas]
type = ElementIntegralVariablePostprocessor
variable = viscosity_gas
execute_on = 'initial timestep_end'
[]
[x1_water]
type = ElementIntegralVariablePostprocessor
variable = x1_water
execute_on = 'initial timestep_end'
[]
[x0_water]
type = ElementIntegralVariablePostprocessor
variable = x0_water
execute_on = 'initial timestep_end'
[]
[x1_gas]
type = ElementIntegralVariablePostprocessor
variable = x1_gas
execute_on = 'initial timestep_end'
[]
[x0_gas]
type = ElementIntegralVariablePostprocessor
variable = x0_gas
execute_on = 'initial timestep_end'
[]
[sg]
type = ElementIntegralVariablePostprocessor
variable = saturation_gas
execute_on = 'initial timestep_end'
[]
[sw]
type = ElementIntegralVariablePostprocessor
variable = saturation_water
execute_on = 'initial timestep_end'
[]
[pwater]
type = ElementIntegralVariablePostprocessor
variable = pressure_water
execute_on = 'initial timestep_end'
[]
[pgas]
type = ElementIntegralVariablePostprocessor
variable = pressure_gas
execute_on = 'initial timestep_end'
[]
[xnacl]
type = ElementIntegralVariablePostprocessor
variable = xnacl
execute_on = 'initial timestep_end'
[]
[x0mass]
type = PorousFlowFluidMass
fluid_component = 0
phase = '0 1'
execute_on = 'initial timestep_end'
[]
[x1mass]
type = PorousFlowFluidMass
fluid_component = 1
phase = '0 1'
execute_on = 'initial timestep_end'
[]
[x2mass]
type = PorousFlowFluidMass
fluid_component = 2
phase = '0 1'
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
csv = true
file_base = brineco2_2
execute_on = 'initial timestep_end'
perf_graph = true
[]
(modules/porous_flow/test/tests/fluidstate/waterncg.i)
# Tests correct calculation of properties in PorousFlowWaterNCG.
# This test is run three times, with the initial condition of z (the total mass
# fraction of NCG in all phases) varied to give either a single phase liquid, a
# single phase gas, or two phases.
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 2
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pgas]
initial_condition = 1e6
[]
[z]
initial_condition = 0.005
[]
[]
[AuxVariables]
[pressure_gas]
order = CONSTANT
family = MONOMIAL
[]
[pressure_water]
order = CONSTANT
family = MONOMIAL
[]
[saturation_gas]
order = CONSTANT
family = MONOMIAL
[]
[saturation_water]
order = CONSTANT
family = MONOMIAL
[]
[density_water]
order = CONSTANT
family = MONOMIAL
[]
[density_gas]
order = CONSTANT
family = MONOMIAL
[]
[viscosity_water]
order = CONSTANT
family = MONOMIAL
[]
[viscosity_gas]
order = CONSTANT
family = MONOMIAL
[]
[enthalpy_water]
order = CONSTANT
family = MONOMIAL
[]
[enthalpy_gas]
order = CONSTANT
family = MONOMIAL
[]
[internal_energy_water]
order = CONSTANT
family = MONOMIAL
[]
[internal_energy_gas]
order = CONSTANT
family = MONOMIAL
[]
[x0_water]
order = CONSTANT
family = MONOMIAL
[]
[x0_gas]
order = CONSTANT
family = MONOMIAL
[]
[x1_water]
order = CONSTANT
family = MONOMIAL
[]
[x1_gas]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[pressure_water]
type = PorousFlowPropertyAux
variable = pressure_water
property = pressure
phase = 0
execute_on = timestep_end
[]
[pressure_gas]
type = PorousFlowPropertyAux
variable = pressure_gas
property = pressure
phase = 1
execute_on = timestep_end
[]
[saturation_water]
type = PorousFlowPropertyAux
variable = saturation_water
property = saturation
phase = 0
execute_on = timestep_end
[]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = timestep_end
[]
[density_water]
type = PorousFlowPropertyAux
variable = density_water
property = density
phase = 0
execute_on = timestep_end
[]
[density_gas]
type = PorousFlowPropertyAux
variable = density_gas
property = density
phase = 1
execute_on = timestep_end
[]
[viscosity_water]
type = PorousFlowPropertyAux
variable = viscosity_water
property = viscosity
phase = 0
execute_on = timestep_end
[]
[viscosity_gas]
type = PorousFlowPropertyAux
variable = viscosity_gas
property = viscosity
phase = 1
execute_on = timestep_end
[]
[enthalpy_water]
type = PorousFlowPropertyAux
variable = enthalpy_water
property = enthalpy
phase = 0
execute_on = timestep_end
[]
[enthalpy_gas]
type = PorousFlowPropertyAux
variable = enthalpy_gas
property = enthalpy
phase = 1
execute_on = timestep_end
[]
[internal_energy_water]
type = PorousFlowPropertyAux
variable = internal_energy_water
property = internal_energy
phase = 0
execute_on = timestep_end
[]
[internal_energy_gas]
type = PorousFlowPropertyAux
variable = internal_energy_gas
property = internal_energy
phase = 1
execute_on = timestep_end
[]
[x1_water]
type = PorousFlowPropertyAux
variable = x1_water
property = mass_fraction
phase = 0
fluid_component = 1
execute_on = timestep_end
[]
[x1_gas]
type = PorousFlowPropertyAux
variable = x1_gas
property = mass_fraction
phase = 1
fluid_component = 1
execute_on = timestep_end
[]
[x0_water]
type = PorousFlowPropertyAux
variable = x0_water
property = mass_fraction
phase = 0
fluid_component = 0
execute_on = timestep_end
[]
[x0_gas]
type = PorousFlowPropertyAux
variable = x0_gas
property = mass_fraction
phase = 1
fluid_component = 0
execute_on = timestep_end
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
variable = pgas
fluid_component = 0
[]
[mass1]
type = PorousFlowMassTimeDerivative
variable = z
fluid_component = 1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas z'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowWaterNCG
water_fp = water
gas_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2]
type = CO2FluidProperties
[]
[water]
type = Water97FluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = 50
[]
[waterncg]
type = PorousFlowFluidState
gas_porepressure = pgas
z = z
temperature_unit = Celsius
capillary_pressure = pc
fluid_state = fs
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm0]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[relperm1]
type = PorousFlowRelativePermeabilityCorey
n = 3
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
dt = 1
end_time = 1
nl_abs_tol = 1e-12
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Postprocessors]
[density_water]
type = ElementIntegralVariablePostprocessor
variable = density_water
[]
[density_gas]
type = ElementIntegralVariablePostprocessor
variable = density_gas
[]
[viscosity_water]
type = ElementIntegralVariablePostprocessor
variable = viscosity_water
[]
[viscosity_gas]
type = ElementIntegralVariablePostprocessor
variable = viscosity_gas
[]
[enthalpy_water]
type = ElementIntegralVariablePostprocessor
variable = enthalpy_water
[]
[enthalpy_gas]
type = ElementIntegralVariablePostprocessor
variable = enthalpy_gas
[]
[internal_energy_water]
type = ElementIntegralVariablePostprocessor
variable = internal_energy_water
[]
[internal_energy_gas]
type = ElementIntegralVariablePostprocessor
variable = internal_energy_gas
[]
[x1_water]
type = ElementIntegralVariablePostprocessor
variable = x1_water
[]
[x0_water]
type = ElementIntegralVariablePostprocessor
variable = x0_water
[]
[x1_gas]
type = ElementIntegralVariablePostprocessor
variable = x1_gas
[]
[x0_gas]
type = ElementIntegralVariablePostprocessor
variable = x0_gas
[]
[sg]
type = ElementIntegralVariablePostprocessor
variable = saturation_gas
[]
[sw]
type = ElementIntegralVariablePostprocessor
variable = saturation_water
[]
[pwater]
type = ElementIntegralVariablePostprocessor
variable = pressure_water
[]
[pgas]
type = ElementIntegralVariablePostprocessor
variable = pressure_gas
[]
[x0mass]
type = PorousFlowFluidMass
fluid_component = 0
phase = '0 1'
[]
[x1mass]
type = PorousFlowFluidMass
fluid_component = 1
phase = '0 1'
[]
[]
[Outputs]
exodus = true
file_base = waterncg_liquid
[]
(modules/porous_flow/test/tests/fluidstate/waterncg_ic.i)
# Tests correct calculation of z (total mass fraction of NCG summed over all
# phases) using the PorousFlowFluidStateIC initial condition. Once z is
# calculated by the initial condition, the thermophysical properties are calculated
# and the resulting gas saturation should be equal to that given in the intial condition
[Mesh]
type = GeneratedMesh
dim = 2
[]
[GlobalParams]
PorousFlowDictator = dictator
temperature_unit = Celsius
[]
[Variables]
[pgas]
initial_condition = 1e6
[]
[z]
[]
[]
[ICs]
[z]
type = PorousFlowFluidStateIC
saturation = 0.5
gas_porepressure = pgas
temperature = 50
variable = z
fluid_state = fs
[]
[]
[AuxVariables]
[saturation_gas]
order = CONSTANT
family = MONOMIAL
[]
[saturation_water]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[saturation_water]
type = PorousFlowPropertyAux
variable = saturation_water
property = saturation
phase = 0
execute_on = timestep_end
[]
[saturation_gas]
type = PorousFlowPropertyAux
variable = saturation_gas
property = saturation
phase = 1
execute_on = timestep_end
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
variable = pgas
fluid_component = 0
[]
[mass1]
type = PorousFlowMassTimeDerivative
variable = z
fluid_component = 1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pgas z'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[fs]
type = PorousFlowWaterNCG
water_fp = water
gas_fp = co2
capillary_pressure = pc
[]
[]
[FluidProperties]
[co2]
type = CO2FluidProperties
[]
[water]
type = Water97FluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = 50
[]
[waterncg]
type = PorousFlowFluidState
gas_porepressure = pgas
z = z
fluid_state = fs
capillary_pressure = pc
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm0]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[relperm1]
type = PorousFlowRelativePermeabilityCorey
n = 3
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
dt = 1
end_time = 1
nl_abs_tol = 1e-12
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Postprocessors]
[sg]
type = ElementIntegralVariablePostprocessor
variable = saturation_gas
execute_on = 'initial timestep_end'
[]
[sw]
type = ElementIntegralVariablePostprocessor
variable = saturation_water
execute_on = 'initial timestep_end'
[]
[z]
type = ElementIntegralVariablePostprocessor
variable = z
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
csv = true
[]
(modules/porous_flow/test/tests/pressure_pulse/pressure_pulse_1d_2phasePS_KT.i)
# Pressure pulse in 1D with 2 phases, 2components - transient
# Using KT stabilization
[Mesh]
type = GeneratedMesh
dim = 1
nx = 10
xmin = 0
xmax = 100
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[ppwater]
initial_condition = 2e6
[]
[sgas]
initial_condition = 0.3
[]
[]
[AuxVariables]
[massfrac_ph0_sp0]
initial_condition = 1
[]
[massfrac_ph1_sp0]
initial_condition = 0
[]
[ppgas]
family = MONOMIAL
order = FIRST
[]
[]
[Kernels]
[mass_component0]
type = PorousFlowMassTimeDerivative
variable = ppwater
fluid_component = 0
[]
[flux_component0_phase0]
type = PorousFlowFluxLimitedTVDAdvection
variable = ppwater
advective_flux_calculator = afc_component0_phase0
[]
[flux_component0_phase1]
type = PorousFlowFluxLimitedTVDAdvection
variable = ppwater
advective_flux_calculator = afc_component0_phase1
[]
[mass_component1]
type = PorousFlowMassTimeDerivative
variable = sgas
fluid_component = 1
[]
[flux_component1_phase0]
type = PorousFlowFluxLimitedTVDAdvection
variable = sgas
advective_flux_calculator = afc_component1_phase0
[]
[flux_component1_phase1]
type = PorousFlowFluxLimitedTVDAdvection
variable = sgas
advective_flux_calculator = afc_component1_phase1
[]
[]
[AuxKernels]
[ppgas]
type = PorousFlowPropertyAux
property = pressure
phase = 1
variable = ppgas
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'ppwater sgas'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 1e5
[]
[afc_component0_phase0]
type = PorousFlowAdvectiveFluxCalculatorUnsaturatedMultiComponent
fluid_component = 0
phase = 0
flux_limiter_type = superbee
[]
[afc_component0_phase1]
type = PorousFlowAdvectiveFluxCalculatorUnsaturatedMultiComponent
fluid_component = 0
phase = 1
flux_limiter_type = superbee
[]
[afc_component1_phase0]
type = PorousFlowAdvectiveFluxCalculatorUnsaturatedMultiComponent
fluid_component = 1
phase = 0
flux_limiter_type = superbee
[]
[afc_component1_phase1]
type = PorousFlowAdvectiveFluxCalculatorUnsaturatedMultiComponent
fluid_component = 1
phase = 1
flux_limiter_type = superbee
[]
[]
[FluidProperties]
[simple_fluid0]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 1000
thermal_expansion = 0
viscosity = 1e-3
[]
[simple_fluid1]
type = SimpleFluidProperties
bulk_modulus = 2e7
density0 = 1
thermal_expansion = 0
viscosity = 1e-5
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = ppwater
phase1_saturation = sgas
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid0
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid1
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-15 0 0 0 1e-15 0 0 0 1e-15'
[]
[relperm_water]
type = PorousFlowRelativePermeabilityCorey
n = 1
phase = 0
[]
[relperm_gas]
type = PorousFlowRelativePermeabilityCorey
n = 1
phase = 1
[]
[]
[BCs]
[leftwater]
type = DirichletBC
boundary = left
value = 3e6
variable = ppwater
[]
[rightwater]
type = DirichletBC
boundary = right
value = 2e6
variable = ppwater
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-ksp_type -pc_type -snes_atol -snes_rtol -snes_max_it'
petsc_options_value = 'bcgs bjacobi 1E-15 1E-20 10000'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1e3
end_time = 1e4
[]
[VectorPostprocessors]
[pp]
type = LineValueSampler
warn_discontinuous_face_values = false
sort_by = x
variable = 'ppwater ppgas'
start_point = '0 0 0'
end_point = '100 0 0'
num_points = 11
[]
[]
[Outputs]
file_base = pressure_pulse_1d_2phasePS_KT
print_linear_residuals = false
[csv]
type = CSV
execute_on = final
[]
[]
(modules/porous_flow/test/tests/basic_advection/1phase.i)
# Basic advection of u in a 1-phase situation
#
# grad(P) = -2
# density * gravity = 4 * 0.25
# grad(P) - density * gravity = -3
# permeability = 5
# viscosity = 150
# so Darcy velocity = 0.1
[Mesh]
type = GeneratedMesh
dim = 1
nx = 10
xmin = 0
xmax = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[u]
[]
[]
[AuxVariables]
[P]
[]
[]
[ICs]
[P]
type = FunctionIC
variable = P
function = '2*(1-x)'
[]
[u]
type = FunctionIC
variable = u
function = 'if(x<0.1,1,0)'
[]
[]
[Kernels]
[u_dot]
type = TimeDerivative
variable = u
[]
[u_advection]
type = PorousFlowBasicAdvection
variable = u
phase = 0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = ''
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 4
thermal_expansion = 0
viscosity = 150.0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = P
capillary_pressure = pc
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '5 0 0 0 5 0 0 0 5'
[]
[relperm]
type = PorousFlowRelativePermeabilityCorey
n = 0
phase = 0
[]
[darcy_velocity]
type = PorousFlowDarcyVelocityMaterial
gravity = '0.25 0 0'
[]
[]
[BCs]
[left]
type = DirichletBC
boundary = left
value = 1
variable = u
[]
[right]
type = DirichletBC
boundary = right
value = 0
variable = u
[]
[]
[Preconditioning]
[basic]
type = SMP
full = true
petsc_options_iname = '-pc_type -snes_rtol'
petsc_options_value = ' lu 1E-10'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 5
[]
[Outputs]
exodus = true
print_linear_residuals = false
[]
(modules/porous_flow/test/tests/flux_limited_TVD_pflow/jacobian_01.i)
# Checking the Jacobian of Flux-Limited TVD Advection, 1 phase, 1 component, full saturation, using flux_limiter_type = none
# This is quite a heavy test, but we need a fairly big mesh to check the upwinding is happening correctly
[Mesh]
type = GeneratedMesh
dim = 3
nx = 3
xmin = 0
xmax = 1
ny = 4
ymin = -1
ymax = 2
bias_y = 1.5
nz = 4
zmin = 1
zmax = 2
bias_z = 0.8
[]
[GlobalParams]
gravity = '1 2 -0.5'
PorousFlowDictator = dictator
[]
[Variables]
[pp]
[]
[]
[ICs]
[pp]
variable = pp
type = RandomIC
min = 1
max = 2
[]
[]
[Kernels]
[flux0]
type = PorousFlowFluxLimitedTVDAdvection
variable = pp
advective_flux_calculator = advective_flux_calculator
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 1
density0 = 0.4
viscosity = 1.1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[advective_flux_calculator]
type = PorousFlowAdvectiveFluxCalculatorSaturated
flux_limiter_type = None
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = pp
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[relperm]
type = PorousFlowRelativePermeabilityConst
phase = 0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1.21 0 0 0 1.5 0 0 0 0.8'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-snes_type'
petsc_options_value = 'test'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
end_time = 1
num_steps = 1
dt = 1
[]
(modules/porous_flow/test/tests/gravity/grav02e.i)
# Checking that gravity head is established in the transient situation when 0<=saturation<=1 (note the less-than-or-equal-to).
# 2phase (PS), 2components, constant capillary pressure, constant fluid bulk-moduli for each phase, constant viscosity,
# constant permeability, Corey relative permeabilities with no residual saturation
[Mesh]
type = GeneratedMesh
dim = 2
ny = 10
ymax = 100
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 -10 0'
[]
[Variables]
[ppwater]
initial_condition = 1.5e6
[]
[sgas]
initial_condition = 0.3
[]
[]
[AuxVariables]
[massfrac_ph0_sp0]
initial_condition = 1
[]
[massfrac_ph1_sp0]
initial_condition = 0
[]
[ppgas]
family = MONOMIAL
order = FIRST
[]
[swater]
family = MONOMIAL
order = FIRST
[]
[relpermwater]
family = MONOMIAL
order = FIRST
[]
[relpermgas]
family = MONOMIAL
order = FIRST
[]
[]
[Kernels]
[mass0]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = ppwater
[]
[flux0]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = ppwater
[]
[mass1]
type = PorousFlowMassTimeDerivative
fluid_component = 1
variable = sgas
[]
[flux1]
type = PorousFlowAdvectiveFlux
fluid_component = 1
variable = sgas
[]
[]
[AuxKernels]
[ppgas]
type = PorousFlowPropertyAux
property = pressure
phase = 1
variable = ppgas
[]
[swater]
type = PorousFlowPropertyAux
property = saturation
phase = 0
variable = swater
[]
[relpermwater]
type = PorousFlowPropertyAux
property = relperm
phase = 0
variable = relpermwater
[]
[relpermgas]
type = PorousFlowPropertyAux
property = relperm
phase = 1
variable = relpermgas
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'ppwater sgas'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 1e5
[]
[]
[FluidProperties]
[simple_fluid0]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 1000
viscosity = 1e-3
thermal_expansion = 0
[]
[simple_fluid1]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 10
viscosity = 1e-5
thermal_expansion = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = ppwater
phase1_saturation = sgas
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
mass_fraction_vars = 'massfrac_ph0_sp0 massfrac_ph1_sp0'
[]
[simple_fluid0]
type = PorousFlowSingleComponentFluid
fp = simple_fluid0
phase = 0
[]
[simple_fluid1]
type = PorousFlowSingleComponentFluid
fp = simple_fluid1
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-11 0 0 0 1e-11 0 0 0 1e-11'
[]
[relperm_water]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[relperm_gas]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 1
[]
[]
[Postprocessors]
[mass_ph0]
type = PorousFlowFluidMass
fluid_component = 0
execute_on = 'initial timestep_end'
[]
[mass_ph1]
type = PorousFlowFluidMass
fluid_component = 1
execute_on = 'initial timestep_end'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-ksp_type -pc_type -snes_atol -snes_rtol'
petsc_options_value = 'bcgs bjacobi 1E-12 1E-10'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
end_time = 1e5
[TimeStepper]
type = IterationAdaptiveDT
dt = 1e4
[]
[]
[Outputs]
execute_on = 'initial timestep_end'
file_base = grav02e
exodus = true
perf_graph = true
csv = false
[]
(modules/porous_flow/test/tests/relperm/brooks_corey2.i)
# Test Brooks-Corey relative permeability curve by varying saturation over the mesh
# Exponent lambda = 2 for both phases
# Residual saturation of phase 0: s0r = 0.2
# Residual saturation of phase 1: s1r = 0.3
[Mesh]
type = GeneratedMesh
dim = 1
nx = 20
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[p0]
initial_condition = 1e6
[]
[s1]
[]
[]
[AuxVariables]
[s0aux]
family = MONOMIAL
order = CONSTANT
[]
[s1aux]
family = MONOMIAL
order = CONSTANT
[]
[kr0aux]
family = MONOMIAL
order = CONSTANT
[]
[kr1aux]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[s0]
type = PorousFlowPropertyAux
property = saturation
phase = 0
variable = s0aux
[]
[s1]
type = PorousFlowPropertyAux
property = saturation
phase = 1
variable = s1aux
[]
[kr0]
type = PorousFlowPropertyAux
property = relperm
phase = 0
variable = kr0aux
[]
[kr1]
type = PorousFlowPropertyAux
property = relperm
phase = 1
variable = kr1aux
[]
[]
[Functions]
[s1]
type = ParsedFunction
expression = x
[]
[]
[ICs]
[s1]
type = FunctionIC
variable = s1
function = s1
[]
[]
[Kernels]
[p0]
type = Diffusion
variable = p0
[]
[s1]
type = Diffusion
variable = s1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'p0 s1'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
[]
[ppss]
type = PorousFlow2PhasePS
phase0_porepressure = p0
phase1_saturation = s1
capillary_pressure = pc
[]
[kr0]
type = PorousFlowRelativePermeabilityBC
phase = 0
lambda = 2
s_res = 0.2
sum_s_res = 0.5
[]
[kr1]
type = PorousFlowRelativePermeabilityBC
phase = 1
lambda = 2
nw_phase = true
s_res = 0.3
sum_s_res = 0.5
[]
[]
[VectorPostprocessors]
[vpp]
type = LineValueSampler
warn_discontinuous_face_values = false
variable = 's0aux s1aux kr0aux kr1aux'
start_point = '0 0 0'
end_point = '1 0 0'
num_points = 20
sort_by = id
[]
[]
[Executioner]
type = Steady
solve_type = NEWTON
nl_abs_tol = 1e-8
[]
[BCs]
[sleft]
type = DirichletBC
variable = s1
value = 0
boundary = left
[]
[sright]
type = DirichletBC
variable = s1
value = 1
boundary = right
[]
[]
[Outputs]
csv = true
execute_on = timestep_end
[]
(modules/porous_flow/test/tests/poroperm/except1.i)
# Exception test: thermal=true but no thermal_expansion_coeff provided
[Mesh]
type = GeneratedMesh
dim = 3
[]
[GlobalParams]
PorousFlowDictator = dictator
displacements = 'disp_x disp_y disp_z'
biot_coefficient = 0.7
[]
[Variables]
[porepressure]
initial_condition = 2
[]
[temperature]
initial_condition = 4
[]
[disp_x]
[]
[disp_y]
[]
[disp_z]
[]
[]
[ICs]
[disp_x]
type = FunctionIC
function = '0.5 * x'
variable = disp_x
[]
[]
[Kernels]
[dummy_p]
type = TimeDerivative
variable = porepressure
[]
[dummy_t]
type = TimeDerivative
variable = temperature
[]
[dummy_x]
type = TimeDerivative
variable = disp_x
[]
[dummy_y]
type = TimeDerivative
variable = disp_y
[]
[dummy_z]
type = TimeDerivative
variable = disp_z
[]
[]
[AuxVariables]
[porosity]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[porosity]
type = PorousFlowPropertyAux
property = porosity
variable = porosity
[]
[]
[Postprocessors]
[porosity]
type = PointValue
variable = porosity
point = '0 0 0'
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'porepressure temperature'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = temperature
[]
[eff_fluid_pressure]
type = PorousFlowEffectiveFluidPressure
[]
[vol_strain]
type = PorousFlowVolumetricStrain
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = porepressure
capillary_pressure = pc
[]
[porosity]
type = PorousFlowPorosity
mechanical = true
fluid = true
thermal = true
ensure_positive = false
porosity_zero = 0.5
solid_bulk = 0.3
reference_porepressure = 3
reference_temperature = 3.5
[]
[]
[Executioner]
solve_type = Newton
type = Transient
num_steps = 1
[]
[Outputs]
csv = true
[]