- PorousFlowDictatorThe PorousFlowDictator UserObject
C++ Type:UserObjectName
Unit:(no unit assumed)
Controllable:No
Description:The PorousFlowDictator UserObject
- variableThe name of the variable that this residual object operates on
C++ Type:NonlinearVariableName
Unit:(no unit assumed)
Controllable:No
Description:The name of the variable that this residual object operates on
FVPorousFlowMassTimeDerivative
Derivative of fluid-component mass with respect to time
This FVKernel implements the strong form of where all parameters are defined in the nomenclature.
commentnote
Presently, a first-order accurate implicit Euler time derivative is hard-coded.
Input Parameters
- blockThe list of blocks (ids or names) that this object will be applied
C++ Type:std::vector<SubdomainName>
Unit:(no unit assumed)
Controllable:No
Description:The list of blocks (ids or names) that this object will be applied
- fluid_component0The fluid component for this kernel
Default:0
C++ Type:unsigned int
Unit:(no unit assumed)
Controllable:No
Description:The fluid component for this kernel
- 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
Unit:(no unit assumed)
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.
Optional Parameters
- absolute_value_vector_tagsThe tags for the vectors this residual object should fill with the absolute value of the residual contribution
C++ Type:std::vector<TagName>
Unit:(no unit assumed)
Controllable:No
Description:The tags for the vectors this residual object should fill with the absolute value of the residual contribution
- extra_matrix_tagsThe extra tags for the matrices this Kernel should fill
C++ Type:std::vector<TagName>
Unit:(no unit assumed)
Controllable:No
Description:The extra tags for the matrices this Kernel should fill
- extra_vector_tagsThe extra tags for the vectors this Kernel should fill
C++ Type:std::vector<TagName>
Unit:(no unit assumed)
Controllable:No
Description:The extra tags for the vectors this Kernel should fill
- matrix_tagssystem timeThe tag for the matrices this Kernel should fill
Default:system time
C++ Type:MultiMooseEnum
Unit:(no unit assumed)
Options:nontime, system, time
Controllable:No
Description:The tag for the matrices this Kernel should fill
- vector_tagstimeThe tag for the vectors this Kernel should fill
Default:time
C++ Type:MultiMooseEnum
Unit:(no unit assumed)
Options:nontime, time
Controllable:No
Description:The tag for the vectors this Kernel should fill
Tagging Parameters
- control_tagsAdds user-defined labels for accessing object parameters via control logic.
C++ Type:std::vector<std::string>
Unit:(no unit assumed)
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
Unit:(no unit assumed)
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
Unit:(no unit assumed)
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
Unit:(no unit assumed)
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
Unit:(no unit assumed)
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
- ghost_layers1The number of layers of elements to ghost.
Default:1
C++ Type:unsigned short
Unit:(no unit assumed)
Controllable:No
Description:The number of layers of elements to ghost.
- use_point_neighborsFalseWhether to use point neighbors, which introduces additional ghosting to that used for simple face neighbors.
Default:False
C++ Type:bool
Unit:(no unit assumed)
Controllable:No
Description:Whether to use point neighbors, which introduces additional ghosting to that used for simple face neighbors.
Parallel Ghosting Parameters
Input Files
- (modules/porous_flow/test/tests/pressure_pulse/pressure_pulse_1d_2phase_fv.i)
- (modules/porous_flow/test/tests/aux_kernels/darcy_velocity_fv.i)
- (modules/porous_flow/test/tests/fluidstate/brineco2_fv.i)
- (modules/porous_flow/test/tests/heat_advection/heat_advection_1d_fv.i)
- (modules/porous_flow/test/tests/pressure_pulse/pressure_pulse_1d_fully_saturated_fv.i)
- (modules/porous_flow/test/tests/pressure_pulse/pressure_pulse_1d_fv.i)
- (modules/porous_flow/test/tests/jacobian/fv_mass_flux.i)
- (modules/porous_flow/test/tests/dispersion/diff01_fv.i)
- (modules/porous_flow/test/tests/pressure_pulse/pressure_pulse_1d_2phasePS_fv.i)
- (modules/porous_flow/test/tests/dispersion/disp01_fv.i)
- (modules/porous_flow/test/tests/gravity/grav02e_fv.i)
- (modules/porous_flow/examples/fluidflower/fluidflower.i)
- (modules/porous_flow/test/tests/mass_conservation/mass14.i)
- (modules/porous_flow/test/tests/heterogeneous_materials/constant_poroperm_fv.i)
(modules/porous_flow/test/tests/pressure_pulse/pressure_pulse_1d_2phase_fv.i)
# Pressure pulse in 1D with 2 phases (with one having zero saturation), 2components - transient using FV
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
nx = 10
xmin = 0
xmax = 100
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[ppwater]
type = MooseVariableFVReal
initial_condition = 2E6
[]
[ppgas]
type = MooseVariableFVReal
initial_condition = 2E6
[]
[]
[AuxVariables]
[massfrac_ph0_sp0]
type = MooseVariableFVReal
initial_condition = 1
[]
[massfrac_ph1_sp0]
type = MooseVariableFVReal
initial_condition = 0
[]
[]
[FVKernels]
[mass0]
type = FVPorousFlowMassTimeDerivative
fluid_component = 0
variable = ppwater
[]
[flux0]
type = FVPorousFlowAdvectiveFlux
variable = ppwater
gravity = '0 0 0'
fluid_component = 0
[]
[mass1]
type = FVPorousFlowMassTimeDerivative
fluid_component = 1
variable = ppgas
[]
[flux1]
type = FVPorousFlowAdvectiveFlux
variable = ppgas
gravity = '0 0 0'
fluid_component = 1
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'ppwater ppgas'
number_fluid_phases = 2
number_fluid_components = 2
[]
[pc]
type = PorousFlowCapillaryPressureVG
m = 0.5
alpha = 1
[]
[]
[FluidProperties]
[simple_fluid0]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 1000
thermal_expansion = 0
viscosity = 1e-3
[]
[simple_fluid1]
type = SimpleFluidProperties
bulk_modulus = 2e6
density0 = 1
thermal_expansion = 0
viscosity = 1e-5
[]
[]
[Materials]
[temperature]
type = ADPorousFlowTemperature
[]
[ppss]
type = ADPorousFlow2PhasePP
phase0_porepressure = ppwater
phase1_porepressure = ppgas
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
[]
[leftgas]
type = FVDirichletBC
boundary = left
value = 3E6
variable = ppgas
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-ksp_type -pc_type -sub_pc_type -sub_pc_factor_shift_type -pc_asm_overlap -snes_atol'
petsc_options_value = 'gmres asm lu NONZERO 2 1E-12'
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1E3
end_time = 1E4
[]
[Postprocessors]
[p005]
type = PointValue
variable = ppwater
point = '5 0 0'
execute_on = 'initial timestep_end'
[]
[p015]
type = PointValue
variable = ppwater
point = '15 0 0'
execute_on = 'initial timestep_end'
[]
[p025]
type = PointValue
variable = ppwater
point = '25 0 0'
execute_on = 'initial timestep_end'
[]
[p035]
type = PointValue
variable = ppwater
point = '35 0 0'
execute_on = 'initial timestep_end'
[]
[p045]
type = PointValue
variable = ppwater
point = '45 0 0'
execute_on = 'initial timestep_end'
[]
[p055]
type = PointValue
variable = ppwater
point = '55 0 0'
execute_on = 'initial timestep_end'
[]
[p065]
type = PointValue
variable = ppwater
point = '65 0 0'
execute_on = 'initial timestep_end'
[]
[p075]
type = PointValue
variable = ppwater
point = '75 0 0'
execute_on = 'initial timestep_end'
[]
[p085]
type = PointValue
variable = ppwater
point = '85 0 0'
execute_on = 'initial timestep_end'
[]
[p095]
type = PointValue
variable = ppwater
point = '95 0 0'
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
file_base = pressure_pulse_1d_2phase_fv
print_linear_residuals = false
csv = true
[]
(modules/porous_flow/test/tests/aux_kernels/darcy_velocity_fv.i)
# checking that the PorousFlowDarcyVelocityComponent AuxKernel works as expected
# for the fully-saturated case (relative-permeability = 1) using finite volumes
[Mesh]
type = GeneratedMesh
dim = 3
xmin = 0
xmax = 1
ymin = 0
ymax = 1
zmin = 0
zmax = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '1 -2 3'
[]
[Variables]
[pp]
family = MONOMIAL
order = CONSTANT
fv = true
[]
[]
[ICs]
[pinit]
type = FunctionIC
function = x
variable = pp
[]
[]
[FVKernels]
[mass0]
type = FVPorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[]
[AuxVariables]
[vel_x]
order = CONSTANT
family = MONOMIAL
[]
[vel_y]
order = CONSTANT
family = MONOMIAL
[]
[vel_z]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[vel_x]
type = ADPorousFlowDarcyVelocityComponent
variable = vel_x
component = x
fluid_phase = 0
[]
[vel_y]
type = ADPorousFlowDarcyVelocityComponent
variable = vel_y
component = y
fluid_phase = 0
[]
[vel_z]
type = ADPorousFlowDarcyVelocityComponent
variable = 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 = PorousFlowCapillaryPressureVG
m = 0.5
alpha = 1
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 1e6
viscosity = 3.2
density0 = 1
thermal_expansion = 0
[]
[]
[Postprocessors]
[vel_x]
type = PointValue
variable = vel_x
point = '0.5 0.5 0.5'
[]
[vel_y]
type = PointValue
variable = vel_y
point = '0.5 0.5 0.5'
[]
[vel_z]
type = PointValue
variable = vel_z
point = '0.5 0.5 0.5'
[]
[]
[Materials]
[temperature]
type = ADPorousFlowTemperature
[]
[ppss]
type = ADPorousFlow1PhaseP
porepressure = pp
capillary_pressure = pc
[]
[massfrac]
type = ADPorousFlowMassFraction
[]
[simple_fluid]
type = ADPorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[permeability]
type = ADPorousFlowPermeabilityConst
permeability = '1 0 0 0 2 0 0 0 3'
[]
[relperm]
type = ADPorousFlowRelativePermeabilityConst
phase = 0
kr = 1
[]
[porosity]
type = ADPorousFlowPorosityConst
porosity = 0.1
[]
[]
[Executioner]
type = Transient
solve_type = Newton
nl_abs_tol = 1e-16
dt = 1
end_time = 1
[]
[Outputs]
execute_on = 'timestep_end'
csv = true
[]
(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/test/tests/heat_advection/heat_advection_1d_fv.i)
# 1phase, heat advecting with a moving fluid using FV
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
nx = 50
xmin = 0
xmax = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[temp]
type = MooseVariableFVReal
[]
[pp]
type = MooseVariableFVReal
[]
[]
[FVICs]
[pp]
type = FVFunctionIC
variable = pp
function = '1-x'
[]
[temp]
type = FVFunctionIC
variable = temp
function = 'if(x<0.02, 300, 200)'
[]
[]
[FVBCs]
[pp0]
type = FVDirichletBC
variable = pp
boundary = left
value = 1
[]
[pp1]
type = FVDirichletBC
variable = pp
boundary = right
value = 0
[]
[hot]
type = FVDirichletBC
variable = temp
boundary = left
value = 300
[]
[cold]
type = FVDirichletBC
variable = temp
boundary = right
value = 200
[]
[]
[FVKernels]
[mass_dot]
type = FVPorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[advection]
type = FVPorousFlowAdvectiveFlux
fluid_component = 0
variable = pp
[]
[energy_dot]
type = FVPorousFlowEnergyTimeDerivative
variable = temp
[]
[heat_advection]
type = FVPorousFlowHeatAdvection
variable = temp
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'temp pp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureVG
m = 0.6
alpha = 1.3
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 100
density0 = 1000
viscosity = 4.4
thermal_expansion = 0
cv = 2
[]
[]
[Materials]
[temperature]
type = ADPorousFlowTemperature
temperature = temp
[]
[porosity]
type = ADPorousFlowPorosityConst
porosity = 0.2
[]
[rock_heat]
type = ADPorousFlowMatrixInternalEnergy
specific_heat_capacity = 1.0
density = 125
[]
[simple_fluid]
type = ADPorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[permeability]
type = ADPorousFlowPermeabilityConst
permeability = '1.1 0 0 0 2 0 0 0 3'
[]
[relperm]
type = ADPorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[massfrac]
type = ADPorousFlowMassFraction
[]
[PS]
type = ADPorousFlow1PhaseP
porepressure = pp
capillary_pressure = pc
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 0.01
end_time = 0.6
[]
[VectorPostprocessors]
[T]
type = ElementValueSampler
sort_by = x
variable = 'temp'
[]
[]
[Outputs]
[csv]
type = CSV
execute_vector_postprocessors_on = final
[]
[]
(modules/porous_flow/test/tests/pressure_pulse/pressure_pulse_1d_fully_saturated_fv.i)
# Pressure pulse in 1D with 1 phase fully saturated - transient FV model
[Mesh]
type = GeneratedMesh
dim = 1
nx = 10
xmin = 0
xmax = 100
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pp]
type = MooseVariableFVReal
initial_condition = 2E6
[]
[]
[FVKernels]
[mass0]
type = FVPorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[flux]
type = FVPorousFlowAdvectiveFlux
variable = pp
gravity = '0 0 0'
fluid_component = 0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 1000
thermal_expansion = 0
viscosity = 1e-3
[]
[]
[Materials]
[temperature]
type = ADPorousFlowTemperature
temperature = 293
[]
[ppss]
type = ADPorousFlow1PhaseFullySaturated
porepressure = pp
[]
[massfrac]
type = ADPorousFlowMassFraction
[]
[simple_fluid]
type = ADPorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[porosity]
type = ADPorousFlowPorosityConst
porosity = 0.1
[]
[permeability]
type = ADPorousFlowPermeabilityConst
permeability = '1E-15 0 0 0 1E-15 0 0 0 1E-15'
[]
[relperm]
type = ADPorousFlowRelativePermeabilityConst
kr = 1
phase = 0
[]
[]
[FVBCs]
[left]
type = FVPorousFlowAdvectiveFluxBC
boundary = left
porepressure_value = 3E6
variable = pp
gravity = '0 0 0'
fluid_component = 0
phase = 0
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1E3
end_time = 1E4
[]
[Postprocessors]
[p005]
type = PointValue
variable = pp
point = '5 0 0'
execute_on = 'initial timestep_end'
[]
[p015]
type = PointValue
variable = pp
point = '15 0 0'
execute_on = 'initial timestep_end'
[]
[p025]
type = PointValue
variable = pp
point = '25 0 0'
execute_on = 'initial timestep_end'
[]
[p035]
type = PointValue
variable = pp
point = '35 0 0'
execute_on = 'initial timestep_end'
[]
[p045]
type = PointValue
variable = pp
point = '45 0 0'
execute_on = 'initial timestep_end'
[]
[p055]
type = PointValue
variable = pp
point = '55 0 0'
execute_on = 'initial timestep_end'
[]
[p065]
type = PointValue
variable = pp
point = '65 0 0'
execute_on = 'initial timestep_end'
[]
[p075]
type = PointValue
variable = pp
point = '75 0 0'
execute_on = 'initial timestep_end'
[]
[p085]
type = PointValue
variable = pp
point = '85 0 0'
execute_on = 'initial timestep_end'
[]
[p095]
type = PointValue
variable = pp
point = '95 0 0'
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
file_base = pressure_pulse_1d_fv
print_linear_residuals = false
csv = true
[]
(modules/porous_flow/test/tests/pressure_pulse/pressure_pulse_1d_fv.i)
# Pressure pulse in 1D with 1 phase - transient FV model
[Mesh]
type = GeneratedMesh
dim = 1
nx = 10
xmin = 0
xmax = 100
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pp]
family = MONOMIAL
order = CONSTANT
fv = true
initial_condition = 2E6
[]
[]
[FVKernels]
[mass0]
type = FVPorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[flux]
type = FVPorousFlowAdvectiveFlux
variable = pp
gravity = '0 0 0'
fluid_component = 0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureVG
m = 0.5
alpha = 1e-7
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 1000
thermal_expansion = 0
viscosity = 1e-3
[]
[]
[Materials]
[temperature]
type = ADPorousFlowTemperature
temperature = 293
[]
[ppss]
type = ADPorousFlow1PhaseP
porepressure = pp
capillary_pressure = pc
[]
[massfrac]
type = ADPorousFlowMassFraction
[]
[simple_fluid]
type = ADPorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[porosity]
type = ADPorousFlowPorosityConst
porosity = 0.1
[]
[permeability]
type = ADPorousFlowPermeabilityConst
permeability = '1E-15 0 0 0 1E-15 0 0 0 1E-15'
[]
[relperm]
type = ADPorousFlowRelativePermeabilityConst
kr = 1
phase = 0
[]
[]
[FVBCs]
[left]
type = FVPorousFlowAdvectiveFluxBC
boundary = left
porepressure_value = 3E6
variable = pp
gravity = '0 0 0'
fluid_component = 0
phase = 0
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1E3
end_time = 1E4
[]
[Postprocessors]
[p005]
type = PointValue
variable = pp
point = '5 0 0'
execute_on = 'initial timestep_end'
[]
[p015]
type = PointValue
variable = pp
point = '15 0 0'
execute_on = 'initial timestep_end'
[]
[p025]
type = PointValue
variable = pp
point = '25 0 0'
execute_on = 'initial timestep_end'
[]
[p035]
type = PointValue
variable = pp
point = '35 0 0'
execute_on = 'initial timestep_end'
[]
[p045]
type = PointValue
variable = pp
point = '45 0 0'
execute_on = 'initial timestep_end'
[]
[p055]
type = PointValue
variable = pp
point = '55 0 0'
execute_on = 'initial timestep_end'
[]
[p065]
type = PointValue
variable = pp
point = '65 0 0'
execute_on = 'initial timestep_end'
[]
[p075]
type = PointValue
variable = pp
point = '75 0 0'
execute_on = 'initial timestep_end'
[]
[p085]
type = PointValue
variable = pp
point = '85 0 0'
execute_on = 'initial timestep_end'
[]
[p095]
type = PointValue
variable = pp
point = '95 0 0'
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
file_base = pressure_pulse_1d_fv
print_linear_residuals = false
csv = true
[]
(modules/porous_flow/test/tests/jacobian/fv_mass_flux.i)
# Verify Jacobian of FV advective flux and mass time derivative kernels
[Mesh]
type = GeneratedMesh
dim = 2
nx = 2
ny = 2
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pp]
family = MONOMIAL
order = CONSTANT
fv = true
[]
[]
[FVKernels]
[mass0]
type = FVPorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[flux]
type = FVPorousFlowAdvectiveFlux
variable = pp
gravity = '0 -10 0'
fluid_component = 0
[]
[]
[ICs]
[pp]
type = RandomIC
variable = pp
min = 1e6
max = 2e6
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureVG
m = 0.5
alpha = 1e-5
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 1000
thermal_expansion = 0
viscosity = 1e-3
[]
[]
[Materials]
[temperature]
type = ADPorousFlowTemperature
temperature = 293
[]
[ppss]
type = ADPorousFlow1PhaseP
porepressure = pp
capillary_pressure = pc
[]
[massfrac]
type = ADPorousFlowMassFraction
[]
[simple_fluid]
type = ADPorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[porosity]
type = ADPorousFlowPorosityConst
porosity = 0.1
[]
[permeability]
type = ADPorousFlowPermeabilityConst
permeability = '1E-12 0 0 0 1E-12 0 0 0 1E-12'
[]
[relperm]
type = ADPorousFlowRelativePermeabilityConst
kr = 1
phase = 0
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 1
[]
(modules/porous_flow/test/tests/dispersion/diff01_fv.i)
# Test diffusive part of FVPorousFlowDispersiveFlux kernel by setting dispersion
# coefficients to zero. Pressure is held constant over the mesh, and gravity is
# set to zero so that no advective transport of mass takes place.
# Mass fraction is set to 1 on the left hand side and 0 on the right hand side.
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
nx = 20
xmax = 10
bias_x = 1.2
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[pp]
type = MooseVariableFVReal
[]
[massfrac0]
type = MooseVariableFVReal
[]
[]
[AuxVariables]
[velocity]
family = MONOMIAL
order = FIRST
[]
[]
[AuxKernels]
[velocity]
type = ADPorousFlowDarcyVelocityComponent
variable = velocity
component = x
[]
[]
[ICs]
[pp]
type = ConstantIC
variable = pp
value = 1e5
[]
[massfrac0]
type = ConstantIC
variable = massfrac0
value = 0
[]
[]
[FVBCs]
[left]
type = FVDirichletBC
value = 1
variable = massfrac0
boundary = left
[]
[right]
type = FVDirichletBC
value = 0
variable = massfrac0
boundary = right
[]
[pright]
type = FVDirichletBC
variable = pp
boundary = right
value = 1e5
[]
[pleft]
type = FVDirichletBC
variable = pp
boundary = left
value = 1e5
[]
[]
[FVKernels]
[mass0]
type = FVPorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[diff0_pp]
type = FVPorousFlowDispersiveFlux
fluid_component = 0
variable = pp
disp_trans = 0
disp_long = 0
[]
[mass1]
type = FVPorousFlowMassTimeDerivative
fluid_component = 1
variable = massfrac0
[]
[diff1_x]
type = FVPorousFlowDispersiveFlux
fluid_component = 1
variable = massfrac0
disp_trans = 0
disp_long = 0
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp massfrac0'
number_fluid_phases = 1
number_fluid_components = 2
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 1e7
density0 = 1000
viscosity = 0.001
thermal_expansion = 0
[]
[]
[Materials]
[temperature]
type = ADPorousFlowTemperature
[]
[ppss]
type = ADPorousFlow1PhaseFullySaturated
porepressure = pp
[]
[massfrac]
type = ADPorousFlowMassFraction
mass_fraction_vars = massfrac0
[]
[simple_fluid]
type = ADPorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[poro]
type = ADPorousFlowPorosityConst
porosity = 0.3
[]
[diff]
type = ADPorousFlowDiffusivityConst
diffusion_coeff = '1 1'
tortuosity = 0.1
[]
[relp]
type = ADPorousFlowRelativePermeabilityConst
phase = 0
[]
[permeability]
type = ADPorousFlowPermeabilityConst
permeability = '1e-9 0 0 0 1e-9 0 0 0 1e-9'
[]
[]
[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
dt = 1
end_time = 20
[]
[VectorPostprocessors]
[xmass]
type = ElementValueSampler
sort_by = id
variable = massfrac0
[]
[]
[Outputs]
[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]
family = MONOMIAL
order = CONSTANT
[]
[]
[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/dispersion/disp01_fv.i)
# Test dispersive part of FVPorousFlowDispersiveFlux kernel by setting diffusion
# coefficients to zero. A pressure gradient is applied over the mesh to give a
# uniform velocity. Gravity is set to zero.
# Mass fraction is set to 1 on the left hand side and 0 on the right hand side.
[Mesh]
type = GeneratedMesh
dim = 2
nx = 20
xmax = 10
bias_x = 1.1
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[pp]
type = MooseVariableFVReal
[]
[massfrac0]
type = MooseVariableFVReal
[]
[]
[AuxVariables]
[velocity]
family = MONOMIAL
order = FIRST
[]
[]
[AuxKernels]
[velocity]
type = ADPorousFlowDarcyVelocityComponent
variable = velocity
component = x
[]
[]
[ICs]
[pp]
type = FunctionIC
variable = pp
function = pic
[]
[massfrac0]
type = ConstantIC
variable = massfrac0
value = 0
[]
[]
[Functions]
[pic]
type = ParsedFunction
expression = '1.1e5-x*1e3'
[]
[]
[FVBCs]
[xleft]
type = FVDirichletBC
value = 1
variable = massfrac0
boundary = left
[]
[xright]
type = FVDirichletBC
value = 0
variable = massfrac0
boundary = right
[]
[pright]
type = FVDirichletBC
variable = pp
boundary = right
value = 1e5
[]
[pleft]
type = FVDirichletBC
variable = pp
boundary = left
value = 1.1e5
[]
[]
[FVKernels]
[mass0]
type = FVPorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[adv0]
type = FVPorousFlowAdvectiveFlux
fluid_component = 0
variable = pp
[]
[diff0]
type = FVPorousFlowDispersiveFlux
variable = pp
disp_trans = 0
disp_long = 0.2
[]
[mass1]
type = FVPorousFlowMassTimeDerivative
fluid_component = 1
variable = massfrac0
[]
[adv1]
type = FVPorousFlowAdvectiveFlux
fluid_component = 1
variable = massfrac0
[]
[diff1]
type = FVPorousFlowDispersiveFlux
fluid_component = 1
variable = massfrac0
disp_trans = 0
disp_long = 0.2
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp massfrac0'
number_fluid_phases = 1
number_fluid_components = 2
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 1e9
density0 = 1000
viscosity = 0.001
thermal_expansion = 0
[]
[]
[Materials]
[temperature]
type = ADPorousFlowTemperature
[]
[ppss]
type = ADPorousFlow1PhaseFullySaturated
porepressure = pp
[]
[massfrac]
type = ADPorousFlowMassFraction
mass_fraction_vars = massfrac0
[]
[simple_fluid]
type = ADPorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[poro]
type = ADPorousFlowPorosityConst
porosity = 0.3
[]
[diff]
type = ADPorousFlowDiffusivityConst
diffusion_coeff = '0 0'
tortuosity = 0.1
[]
[relp]
type = ADPorousFlowRelativePermeabilityConst
phase = 0
[]
[permeability]
type = ADPorousFlowPermeabilityConst
permeability = '1e-9 0 0 0 1e-9 0 0 0 1e-9'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-ksp_type -pc_type -sub_pc_type -sub_pc_factor_shift_type'
petsc_options_value = 'gmres asm lu NONZERO'
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
end_time = 3e2
dtmax = 100
nl_abs_tol = 1e-12
[TimeStepper]
type = IterationAdaptiveDT
growth_factor = 2
cutback_factor = 0.5
dt = 10
[]
[]
[VectorPostprocessors]
[xmass]
type = ElementValueSampler
sort_by = id
variable = 'massfrac0 velocity'
[]
[]
[Outputs]
[out]
type = CSV
execute_on = final
[]
[]
(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/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/mass_conservation/mass14.i)
# checking that the mass postprocessor correctly calculates the mass
# 1phase, 1component, constant porosity
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 1
nx = 3
xmin = -1
xmax = 1
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pp]
type = MooseVariableFVReal
[]
[]
[ICs]
[pinit]
type = FunctionIC
function = x
variable = pp
[]
[]
[FVKernels]
[mass0]
type = FVPorousFlowMassTimeDerivative
fluid_component = 0
variable = pp
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureVG
m = 0.5
alpha = 1
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 1
density0 = 1
thermal_expansion = 0
[]
[]
[Materials]
[temperature]
type = ADPorousFlowTemperature
[]
[ppss]
type = ADPorousFlow1PhaseP
porepressure = pp
capillary_pressure = pc
[]
[massfrac]
type = ADPorousFlowMassFraction
[]
[simple_fluid]
type = ADPorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[porosity]
type = ADPorousFlowPorosityConst
porosity = 0.1
[]
[]
[Postprocessors]
[total_mass]
type = FVPorousFlowFluidMass
base_name = incorrect_base_name
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 1
end_time = 1
[]
[Outputs]
execute_on = 'timestep_end'
[]
(modules/porous_flow/test/tests/heterogeneous_materials/constant_poroperm_fv.i)
# Assign porosity and permeability variables from constant AuxVariables to create
# a heterogeneous model and solve with FV variables
[Mesh]
[mesh]
type = GeneratedMeshGenerator
dim = 3
nx = 3
ny = 3
nz = 3
xmax = 3
ymax = 3
zmax = 3
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 -10'
[]
[Variables]
[ppwater]
type = MooseVariableFVReal
initial_condition = 1.5e6
[]
[]
[AuxVariables]
[poro]
type = MooseVariableFVReal
[]
[permxx]
type = MooseVariableFVReal
[]
[permxy]
type = MooseVariableFVReal
[]
[permxz]
type = MooseVariableFVReal
[]
[permyx]
type = MooseVariableFVReal
[]
[permyy]
type = MooseVariableFVReal
[]
[permyz]
type = MooseVariableFVReal
[]
[permzx]
type = MooseVariableFVReal
[]
[permzy]
type = MooseVariableFVReal
[]
[permzz]
type = MooseVariableFVReal
[]
[poromat]
family = MONOMIAL
order = CONSTANT
[]
[permxxmat]
family = MONOMIAL
order = CONSTANT
[]
[permxymat]
family = MONOMIAL
order = CONSTANT
[]
[permxzmat]
family = MONOMIAL
order = CONSTANT
[]
[permyxmat]
family = MONOMIAL
order = CONSTANT
[]
[permyymat]
family = MONOMIAL
order = CONSTANT
[]
[permyzmat]
family = MONOMIAL
order = CONSTANT
[]
[permzxmat]
family = MONOMIAL
order = CONSTANT
[]
[permzymat]
family = MONOMIAL
order = CONSTANT
[]
[permzzmat]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[poromat]
type = ADPorousFlowPropertyAux
property = porosity
variable = poromat
[]
[permxxmat]
type = ADPorousFlowPropertyAux
property = permeability
variable = permxxmat
column = 0
row = 0
[]
[permxymat]
type = ADPorousFlowPropertyAux
property = permeability
variable = permxymat
column = 1
row = 0
[]
[permxzmat]
type = ADPorousFlowPropertyAux
property = permeability
variable = permxzmat
column = 2
row = 0
[]
[permyxmat]
type = ADPorousFlowPropertyAux
property = permeability
variable = permyxmat
column = 0
row = 1
[]
[permyymat]
type = ADPorousFlowPropertyAux
property = permeability
variable = permyymat
column = 1
row = 1
[]
[permyzmat]
type = ADPorousFlowPropertyAux
property = permeability
variable = permyzmat
column = 2
row = 1
[]
[permzxmat]
type = ADPorousFlowPropertyAux
property = permeability
variable = permzxmat
column = 0
row = 2
[]
[permzymat]
type = ADPorousFlowPropertyAux
property = permeability
variable = permzymat
column = 1
row = 2
[]
[permzzmat]
type = ADPorousFlowPropertyAux
property = permeability
variable = permzzmat
column = 2
row = 2
[]
[]
[ICs]
[poro]
type = RandomIC
seed = 0
variable = poro
max = 0.5
min = 0.1
[]
[permx]
type = FunctionIC
function = permx
variable = permxx
[]
[permy]
type = FunctionIC
function = permy
variable = permyy
[]
[permz]
type = FunctionIC
function = permz
variable = permzz
[]
[]
[Functions]
[permx]
type = ParsedFunction
expression = '(1+x)*1e-11'
[]
[permy]
type = ParsedFunction
expression = '(1+y)*1e-11'
[]
[permz]
type = ParsedFunction
expression = '(1+z)*1e-11'
[]
[]
[FVKernels]
[mass0]
type = FVPorousFlowMassTimeDerivative
variable = ppwater
[]
[flux0]
type = FVPorousFlowAdvectiveFlux
variable = ppwater
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'ppwater'
number_fluid_phases = 1
number_fluid_components = 1
[]
[]
[FluidProperties]
[simple_fluid]
type = SimpleFluidProperties
bulk_modulus = 2e9
density0 = 1000
viscosity = 1e-3
thermal_expansion = 0
cv = 2
[]
[]
[Materials]
[temperature]
type = ADPorousFlowTemperature
[]
[ppss]
type = ADPorousFlow1PhaseFullySaturated
porepressure = ppwater
[]
[massfrac]
type = ADPorousFlowMassFraction
[]
[simple_fluid]
type = ADPorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[porosity]
type = ADPorousFlowPorosityConst
porosity = poro
[]
[permeability]
type = ADPorousFlowPermeabilityConstFromVar
perm_xx = permxx
perm_yy = permyy
perm_zz = permzz
[]
[relperm_water]
type = ADPorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[]
[Postprocessors]
[mass_ph0]
type = FVPorousFlowFluidMass
fluid_component = 0
execute_on = 'initial timestep_end'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
end_time = 100
dt = 100
[]
[Outputs]
execute_on = 'initial timestep_end'
exodus = true
perf_graph = true
[]