- capillary_pressureName of the UserObject defining the capillary pressure
C++ Type:UserObjectName
Description:Name of the UserObject defining the capillary pressure
- water_fpThe name of the user object for water
C++ Type:UserObjectName
Description:The name of the user object for water
PorousFlowWaterVapor
Fluid state class for water and vapor
Input Parameters
- execute_onTIMESTEP_ENDThe list of flag(s) indicating when this object should be executed, the available options include NONE, INITIAL, LINEAR, NONLINEAR, TIMESTEP_END, TIMESTEP_BEGIN, FINAL, CUSTOM.
Default:TIMESTEP_END
C++ Type:ExecFlagEnum
Options:NONE, INITIAL, LINEAR, NONLINEAR, TIMESTEP_END, TIMESTEP_BEGIN, FINAL, CUSTOM
Description:The list of flag(s) indicating when this object should be executed, the available options include NONE, INITIAL, LINEAR, NONLINEAR, TIMESTEP_END, TIMESTEP_BEGIN, FINAL, CUSTOM.
- liquid_fluid_component0The fluid component number of the primary liquid component
Default:0
C++ Type:unsigned int
Options:
Description:The fluid component number of the primary liquid component
- liquid_phase_number0The phase number of the liquid phase
Default:0
C++ Type:unsigned int
Options:
Description:The phase number of the liquid phase
- salt_component2The component number of salt
Default:2
C++ Type:unsigned int
Options:
Description:The component number of salt
Optional 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
Options:
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).
- control_tagsAdds user-defined labels for accessing object parameters via control logic.
C++ Type:std::vector<std::string>
Options:
Description:Adds user-defined labels for accessing object parameters via control logic.
- enableTrueSet the enabled status of the MooseObject.
Default:True
C++ Type:bool
Options:
Description:Set the enabled status of the MooseObject.
- force_preauxFalseForces the GeneralUserObject to be executed in PREAUX
Default:False
C++ Type:bool
Options:
Description:Forces the GeneralUserObject to be executed in PREAUX
- force_preicFalseForces the GeneralUserObject to be executed in PREIC during initial setup
Default:False
C++ Type:bool
Options:
Description:Forces the GeneralUserObject to be executed in PREIC during initial setup
- 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
Options:
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
Input Files
(modules/porous_flow/test/tests/fluidstate/coldwater_injection_radial.i)
# Cold water injection into 1D radial hot reservoir (Avdonin, 1964)
#
# To generate results presented in documentation for this problem,
# set xmax = 1000 and nx = 200 in the Mesh block, and dtmax = 1e4
# and end_time = 1e6 in the Executioner block.
[Mesh]
type = GeneratedMesh
dim = 1
nx = 50
xmin = 0.1
xmax = 5
bias_x = 1.05
[]
[Problem]
rz_coord_axis = Y
coord_type = RZ
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[AuxVariables]
[temperature]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[temperature]
type = PorousFlowPropertyAux
variable = temperature
property = temperature
execute_on = 'initial timestep_end'
[]
[]
[Variables]
[pliquid]
initial_condition = 5e6
[]
[h]
scaling = 1e-6
[]
[]
[ICs]
[hic]
type = PorousFlowFluidPropertyIC
variable = h
porepressure = pliquid
property = enthalpy
temperature = 170
temperature_unit = Celsius
fp = water
[]
[]
[Functions]
[injection_rate]
type = ParsedFunction
vals = injection_area
vars = area
value = '-0.1/area'
[]
[]
[BCs]
[source]
type = PorousFlowSink
variable = pliquid
flux_function = injection_rate
boundary = left
[]
[pright]
type = DirichletBC
variable = pliquid
value = 5e6
boundary = right
[]
[hleft]
type = DirichletBC
variable = h
value = 678.52e3
boundary = left
[]
[hright]
type = DirichletBC
variable = h
value = 721.4e3
boundary = right
[]
[]
[Kernels]
[mass]
type = PorousFlowMassTimeDerivative
variable = pliquid
[]
[massflux]
type = PorousFlowAdvectiveFlux
variable = pliquid
[]
[heat]
type = PorousFlowEnergyTimeDerivative
variable = h
[]
[heatflux]
type = PorousFlowHeatAdvection
variable = h
[]
[heatcond]
type = PorousFlowHeatConduction
variable = h
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pliquid h'
number_fluid_phases = 2
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureVG
pc_max = 1e6
sat_lr = 0.1
m = 0.5
alpha = 1e-5
[]
[fs]
type = PorousFlowWaterVapor
water_fp = water
capillary_pressure = pc
[]
[]
[Modules]
[FluidProperties]
[water]
type = Water97FluidProperties
[]
[]
[]
[Materials]
[watervapor]
type = PorousFlowFluidStateSingleComponent
porepressure = pliquid
enthalpy = h
temperature_unit = Celsius
capillary_pressure = pc
fluid_state = fs
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.2
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1.8e-11 0 0 0 1.8e-11 0 0 0 1.8e-11'
[]
[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
sum_s_res = 0.1
[]
[internal_energy]
type = PorousFlowMatrixInternalEnergy
density = 2900
specific_heat_capacity = 740
[]
[rock_thermal_conductivity]
type = PorousFlowThermalConductivityIdeal
dry_thermal_conductivity = '20 0 0 0 20 0 0 0 20'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
end_time = 1e3
nl_abs_tol = 1e-8
[TimeStepper]
type = IterationAdaptiveDT
dt = 100
[]
[]
[Postprocessors]
[injection_area]
type = AreaPostprocessor
boundary = left
execute_on = initial
[]
[]
[VectorPostprocessors]
[line]
type = ElementValueSampler
sort_by = x
variable = temperature
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
perf_graph = true
[csv]
type = CSV
execute_on = final
[]
[]
(modules/porous_flow/test/tests/fluidstate/water_vapor.i)
# Tests correct calculation of properties in PorousFlowWaterVapor in the two-phase region
[Mesh]
type = GeneratedMesh
dim = 2
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pliq]
initial_condition = 1e6
[]
[h]
initial_condition = 8e5
scaling = 1e-3
[]
[]
[AuxVariables]
[pressure_gas]
order = CONSTANT
family = MONOMIAL
[]
[pressure_water]
order = CONSTANT
family = MONOMIAL
[]
[enthalpy_gas]
order = CONSTANT
family = MONOMIAL
[]
[enthalpy_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
[]
[temperature]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[enthalpy_water]
type = PorousFlowPropertyAux
variable = enthalpy_water
property = enthalpy
phase = 0
execute_on = 'initial timestep_end'
[]
[enthalpy_gas]
type = PorousFlowPropertyAux
variable = enthalpy_gas
property = enthalpy
phase = 1
execute_on = 'initial timestep_end'
[]
[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'
[]
[temperature]
type = PorousFlowPropertyAux
variable = temperature
property = temperature
execute_on = 'initial timestep_end'
[]
[]
[Kernels]
[mass]
type = PorousFlowMassTimeDerivative
variable = pliq
[]
[heat]
type = PorousFlowEnergyTimeDerivative
variable = h
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pliq h'
number_fluid_phases = 2
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureBC
pe = 1e5
lambda = 2
pc_max = 1e6
[]
[fs]
type = PorousFlowWaterVapor
water_fp = water
capillary_pressure = pc
[]
[]
[Modules]
[FluidProperties]
[water]
type = Water97FluidProperties
[]
[]
[]
[Materials]
[watervapor]
type = PorousFlowFluidStateSingleComponent
porepressure = pliq
enthalpy = h
temperature_unit = Celsius
capillary_pressure = pc
fluid_state = fs
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-13 0 0 0 1e-13 0 0 0 1e-13'
[]
[relperm0]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[relperm1]
type = PorousFlowRelativePermeabilityCorey
n = 3
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.1
[]
[internal_energy]
type = PorousFlowMatrixInternalEnergy
density = 2500
specific_heat_capacity = 1200
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
end_time = 1
nl_abs_tol = 1e-12
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Postprocessors]
[density_water]
type = ElementAverageValue
variable = density_water
execute_on = 'initial timestep_end'
[]
[density_gas]
type = ElementAverageValue
variable = density_gas
execute_on = 'initial timestep_end'
[]
[viscosity_water]
type = ElementAverageValue
variable = viscosity_water
execute_on = 'initial timestep_end'
[]
[viscosity_gas]
type = ElementAverageValue
variable = viscosity_gas
execute_on = 'initial timestep_end'
[]
[enthalpy_water]
type = ElementAverageValue
variable = enthalpy_water
execute_on = 'initial timestep_end'
[]
[enthalpy_gas]
type = ElementAverageValue
variable = enthalpy_gas
execute_on = 'initial timestep_end'
[]
[sg]
type = ElementAverageValue
variable = saturation_gas
execute_on = 'initial timestep_end'
[]
[sw]
type = ElementAverageValue
variable = saturation_water
execute_on = 'initial timestep_end'
[]
[pwater]
type = ElementAverageValue
variable = pressure_water
execute_on = 'initial timestep_end'
[]
[pgas]
type = ElementAverageValue
variable = pressure_gas
execute_on = 'initial timestep_end'
[]
[temperature]
type = ElementAverageValue
variable = temperature
execute_on = 'initial timestep_end'
[]
[enthalpy]
type = ElementAverageValue
variable = h
execute_on = 'initial timestep_end'
[]
[liquid_mass]
type = PorousFlowFluidMass
phase = 0
execute_on = 'initial timestep_end'
[]
[vapor_mass]
type = PorousFlowFluidMass
phase = 1
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
file_base = water_vapor_twophase
csv = true
[]
(modules/porous_flow/test/tests/fluidstate/coldwater_injection.i)
# Cold water injection into 1D hot reservoir (Avdonin, 1964)
#
# To generate results presented in documentation for this problem,
# set xmax = 50 and nx = 250 in the Mesh block, and dtmax = 100 and
# end_time = 1.3e5 in the Executioner block.
[Mesh]
type = GeneratedMesh
dim = 1
nx = 25
xmax = 20
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[AuxVariables]
[temperature]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[temperature]
type = PorousFlowPropertyAux
variable = temperature
property = temperature
execute_on = 'initial timestep_end'
[]
[]
[Variables]
[pliquid]
initial_condition = 5e6
[]
[h]
scaling = 1e-6
[]
[]
[ICs]
[hic]
type = PorousFlowFluidPropertyIC
variable = h
porepressure = pliquid
property = enthalpy
temperature = 170
temperature_unit = Celsius
fp = water
[]
[]
[BCs]
[pleft]
type = DirichletBC
variable = pliquid
value = 5.05e6
boundary = left
[]
[pright]
type = DirichletBC
variable = pliquid
value = 5e6
boundary = right
[]
[hleft]
type = DirichletBC
variable = h
value = 678.52e3
boundary = left
[]
[hright]
type = DirichletBC
variable = h
value = 721.4e3
boundary = right
[]
[]
[Kernels]
[mass]
type = PorousFlowMassTimeDerivative
variable = pliquid
[]
[massflux]
type = PorousFlowAdvectiveFlux
variable = pliquid
[]
[heat]
type = PorousFlowEnergyTimeDerivative
variable = h
[]
[heatflux]
type = PorousFlowHeatAdvection
variable = h
[]
[heatcond]
type = PorousFlowHeatConduction
variable = h
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pliquid h'
number_fluid_phases = 2
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureVG
pc_max = 1e6
sat_lr = 0.1
m = 0.5
alpha = 1e-5
[]
[fs]
type = PorousFlowWaterVapor
water_fp = water
capillary_pressure = pc
[]
[]
[Modules]
[FluidProperties]
[water]
type = Water97FluidProperties
[]
[]
[]
[Materials]
[watervapor]
type = PorousFlowFluidStateSingleComponent
porepressure = pliquid
enthalpy = h
temperature_unit = Celsius
capillary_pressure = pc
fluid_state = fs
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.2
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1.8e-11 0 0 0 1.8e-11 0 0 0 1.8e-11'
[]
[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
sum_s_res = 0.1
[]
[internal_energy]
type = PorousFlowMatrixInternalEnergy
density = 2900
specific_heat_capacity = 740
[]
[rock_thermal_conductivity]
type = PorousFlowThermalConductivityIdeal
dry_thermal_conductivity = '20 0 0 0 20 0 0 0 20'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
end_time = 5e3
nl_abs_tol = 1e-10
[TimeStepper]
type = IterationAdaptiveDT
dt = 100
[]
[]
[VectorPostprocessors]
[line]
type = ElementValueSampler
sort_by = x
variable = temperature
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
perf_graph = true
[csv]
type = CSV
execute_on = final
[]
[]
(modules/porous_flow/test/tests/fluidstate/water_vapor_phasechange.i)
# Tests correct calculation of properties in PorousFlowWaterVapor as a phase change
# from liquid to a two-phase model occurs due to a pressure drop.
# A single 10 m^3 element is used, with constant mass and heat production using
# a Dirac kernel. Initial conditions correspond to just outside the two-phase region in
# the liquid state.
#
# An identical problem can be run using TOUGH2, with the following outputs after 1,000s
# Pressure: 8.58 Mpa
# Temperature: 299.92 K
# Vapor saturation: 0.00637
[Mesh]
type = GeneratedMesh
dim = 3
xmax = 10
ymax = 10
zmax = 10
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[Variables]
[pliq]
initial_condition = 9e6
[]
[h]
scaling = 1e-3
[]
[]
[ICs]
[hic]
type = PorousFlowFluidPropertyIC
variable = h
porepressure = pliq
property = enthalpy
temperature = 300
temperature_unit = Celsius
fp = water
[]
[]
[DiracKernels]
[mass]
type = ConstantPointSource
point = '5 5 5'
variable = pliq
value = -1
[]
[heat]
type = ConstantPointSource
point = '5 5 5'
variable = h
value = -1.344269e6
[]
[]
[AuxVariables]
[pressure_gas]
order = CONSTANT
family = MONOMIAL
[]
[pressure_water]
order = CONSTANT
family = MONOMIAL
[]
[enthalpy_gas]
order = CONSTANT
family = MONOMIAL
[]
[enthalpy_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
[]
[temperature]
order = CONSTANT
family = MONOMIAL
[]
[e_gas]
order = CONSTANT
family = MONOMIAL
[]
[e_water]
order = CONSTANT
family = MONOMIAL
[]
[]
[AuxKernels]
[enthalpy_water]
type = PorousFlowPropertyAux
variable = enthalpy_water
property = enthalpy
phase = 0
execute_on = 'initial timestep_end'
[]
[enthalpy_gas]
type = PorousFlowPropertyAux
variable = enthalpy_gas
property = enthalpy
phase = 1
execute_on = 'initial timestep_end'
[]
[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'
[]
[temperature]
type = PorousFlowPropertyAux
variable = temperature
property = temperature
execute_on = 'initial timestep_end'
[]
[e_water]
type = PorousFlowPropertyAux
variable = e_water
property = internal_energy
phase = 0
execute_on = 'initial timestep_end'
[]
[egas]
type = PorousFlowPropertyAux
variable = e_gas
property = internal_energy
phase = 1
execute_on = 'initial timestep_end'
[]
[]
[Kernels]
[mass]
type = PorousFlowMassTimeDerivative
variable = pliq
[]
[heat]
type = PorousFlowEnergyTimeDerivative
variable = h
[]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pliq h'
number_fluid_phases = 2
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureBC
pe = 1e5
lambda = 2
pc_max = 1e6
[]
[fs]
type = PorousFlowWaterVapor
water_fp = water
capillary_pressure = pc
[]
[]
[Modules]
[FluidProperties]
[water]
type = Water97FluidProperties
[]
[]
[]
[Materials]
[watervapor]
type = PorousFlowFluidStateSingleComponent
porepressure = pliq
enthalpy = h
temperature_unit = Celsius
capillary_pressure = pc
fluid_state = fs
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-14 0 0 0 1e-14 0 0 0 1e-14'
[]
[relperm0]
type = PorousFlowRelativePermeabilityCorey
n = 2
phase = 0
[]
[relperm1]
type = PorousFlowRelativePermeabilityCorey
n = 3
phase = 1
[]
[porosity]
type = PorousFlowPorosityConst
porosity = 0.2
[]
[internal_energy]
type = PorousFlowMatrixInternalEnergy
density = 2650
specific_heat_capacity = 1000
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
end_time = 1e3
nl_abs_tol = 1e-12
[TimeStepper]
type = IterationAdaptiveDT
dt = 10
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Postprocessors]
[density_water]
type = ElementAverageValue
variable = density_water
execute_on = 'initial timestep_end'
[]
[density_gas]
type = ElementAverageValue
variable = density_gas
execute_on = 'initial timestep_end'
[]
[viscosity_water]
type = ElementAverageValue
variable = viscosity_water
execute_on = 'initial timestep_end'
[]
[viscosity_gas]
type = ElementAverageValue
variable = viscosity_gas
execute_on = 'initial timestep_end'
[]
[enthalpy_water]
type = ElementAverageValue
variable = enthalpy_water
execute_on = 'initial timestep_end'
[]
[enthalpy_gas]
type = ElementAverageValue
variable = enthalpy_gas
execute_on = 'initial timestep_end'
[]
[sg]
type = ElementAverageValue
variable = saturation_gas
execute_on = 'initial timestep_end'
[]
[sw]
type = ElementAverageValue
variable = saturation_water
execute_on = 'initial timestep_end'
[]
[pwater]
type = ElementAverageValue
variable = pressure_water
execute_on = 'initial timestep_end'
[]
[pgas]
type = ElementAverageValue
variable = pressure_gas
execute_on = 'initial timestep_end'
[]
[temperature]
type = ElementAverageValue
variable = temperature
execute_on = 'initial timestep_end'
[]
[enthalpy]
type = ElementAverageValue
variable = h
execute_on = 'initial timestep_end'
[]
[pliq]
type = ElementAverageValue
variable = pliq
execute_on = 'initial timestep_end'
[]
[liquid_mass]
type = PorousFlowFluidMass
phase = 0
execute_on = 'initial timestep_end'
[]
[vapor_mass]
type = PorousFlowFluidMass
phase = 1
execute_on = 'initial timestep_end'
[]
[liquid_heat]
type = PorousFlowHeatEnergy
phase = 0
execute_on = 'initial timestep_end'
[]
[vapor_heat]
type = PorousFlowHeatEnergy
phase = 1
execute_on = 'initial timestep_end'
[]
[e_water]
type = ElementAverageValue
variable = e_water
execute_on = 'initial timestep_end'
[]
[e_gas]
type = ElementAverageValue
variable = e_gas
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
csv = true
perf_graph = false
[]