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pf.i
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[Mesh]
[gen]
type = GeneratedMeshGenerator
dim = 2
nx = 150
ny = 100
xmin = -2500
xmax = 3500
ymin = -1300
ymax = 1300
[]
[injection_node]
input = gen
type = ExtraNodesetGenerator
new_boundary = injection_node
coord = '-500 0 0'
[]
[]
[GlobalParams]
PorousFlowDictator = dictator
gravity = '0 0 0'
[]
[Variables]
[p]
initial_condition = 50E6
[]
[T]
initial_condition = 433.15
scaling = 1E-6 # fluid enthalpy is roughly 1E6
[]
[]
[BCs]
# [temperature]
# type = DirichletBC
# variable = temperature
# value = 423.15
# boundary = 'left right top bottom'
# []
# [pressure]
# type = FunctionDirichletBC
# variable = porepressure
# function = csv_data
# boundary = injection_node
# []
# [ttt]
# type = FunctionDirichletBC
# variable = temperature
# function = csv_datat
# boundary = injection_node
# []
[./ttt]
type = PostprocessorDirichletBC
variable = T
boundary = injection_node
postprocessor = T_receiver2
[../]
[./ppp]
type = PostprocessorDirichletBC
variable = p
boundary = injection_node
postprocessor = P_receiver2
[../]
[]
[Functions]
[mass_flux_in_func]
type = ParsedFunction
expression = '10'
[]
[mass_flux_out_func]
type = ParsedFunction
expression = '-10'
[]
[T_in_func]
type = ParsedFunction
expression = '313.15'
[]
[./csv_data]
type = Moskito2Constant
data_file = pcres.csv
direction = RIGHT
format = columns
execute_on = TIMESTEP_BEGIN
[../]
[./csv_datat]
type = Moskito2Constant
data_file = tcres.csv
direction = RIGHT_INCLUSIVE
format = columns
execute_on = TIMESTEP_BEGIN
[../]
[./csv_dataq]
type = Moskito2Constant
data_file = qcres.csv
direction = RIGHT_INCLUSIVE
format = columns
execute_on = TIMESTEP_BEGIN
[../]
[./dts]
type = PiecewiseLinear
x = '0 10000 315360 31536000 630720000'
y = '1000.0 1000.0 86400 3153600 1000000'
#x = '0 7200 72000.0 943000 315360000 3153600000'
#y = '1000 1000.0 1000.0 360000 3600000 3600000'
[../]
[]
[Kernels]
[mass_dot]
type = PorousFlowMassTimeDerivative
fluid_component = 0
variable = p
[]
[mass_flux]
type = PorousFlowAdvectiveFlux
fluid_component = 0
variable = p
[]
[energy_dot]
type = PorousFlowEnergyTimeDerivative
variable = T
[]
[heat_advection]
type = PorousFlowHeatAdvection
variable = T
[]
[heat_conduction]
type = PorousFlowHeatConduction
variable = T
[]
[]
[AuxVariables]
[./qq_aux]
[../]
# [./tt_aux]
# [../]
[]
[AuxKernels]
[./qq_aux2]
type = ConstantAux
variable = qq_aux
value = 0.01
[../]
# [./pp_aux2]
# type = ConstantAux
# variable = pp_aux
# value = 30000000
# [../]
[]
[Postprocessors]
[mass_flux_in]
type = FunctionValuePostprocessor
function = mass_flux_in_func
execute_on = 'initial timestep_begin'
[]
[mass_flux_out]
type = FunctionValuePostprocessor
function = mass_flux_out_func
execute_on = 'initial timestep_begin'
[]
[T_in]
type = FunctionValuePostprocessor
function = T_in_func
execute_on = 'initial timestep_begin'
[]
[./temp_pro]
type = PointValue
point = '1500 0 0'
variable = 'T'
[../]
[belphip]
type = PointValue
variable = p
point = '1500 0 0'
[]
[belphit]
type = PointValue
variable = T
point = '1500 0 0'
[]
[./P_value2]
type = PointValue
variable = p
point = '1500 0 0'
[../]
[./T_value2]
type = PointValue
variable = T
point = '1500 0 0'
[../]
[./Q_value2]
type = PointValue
variable = qq_aux
point = '1500 0 0'
[../]
[./P_receiver2]
type = Receiver
# execute_on = NONLINEAR
[../]
[./T_receiver2]
type = Receiver
# execute_on = NONLINEAR
[../]
[./Q_receiver2]
type = Receiver
# execute_on = NONLINEAR
[../]
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'T p'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
[]
[injected_mass]
type = PorousFlowSumQuantity
[]
[produced_mass]
type = PorousFlowSumQuantity
[]
[produced_heat]
type = PorousFlowSumQuantity
[]
[produced_mass_H2O1]
type = PorousFlowSumQuantity
[]
[produced_heat1]
type = PorousFlowSumQuantity
[]
[]
[FluidProperties]
[the_simple_fluid]
type = SimpleFluidProperties
thermal_expansion = 7E-4
bulk_modulus = 2.5E9
viscosity = 5E-4
density0 = 1000
cv = 4000.0
cp = 4000.0
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = T
[]
[phase]
type = PorousFlow1PhaseP
porepressure = p
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
[]
[water]
type = PorousFlowSingleComponentFluid
fp = the_simple_fluid
phase = 0
[]
[porosity]
type=PorousFlowPorosityConst
porosity = 0.1
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1e-12 0 0 0 1e-12 0 0 0 1e-12'
[]
[relperm]
type = PorousFlowRelativePermeabilityCorey
n = 0
phase = 0
[]
[thermal_conductivity]
type = PorousFlowThermalConductivityIdeal
dry_thermal_conductivity = '2.8 0 0 0 2.8 0 0 0 2.8'
[]
[internal_energy]
type = PorousFlowMatrixInternalEnergy
specific_heat_capacity = 1000
density = 2500
[]
[undrained_density]
type = GenericConstantMaterial
prop_names = density
prop_values = 2500
[]
[]
[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
start_time = 0
end_time = 1576800
l_max_its = 100
nl_abs_tol = 1e-6
solve_type = NEWTON
steady_state_detection = false
[./TimeStepper]
type = FunctionDT
function = dts
[../]
[]
[Outputs]
file_base = pf_out
exodus = true
csv = true
[]
[DiracKernels]
[inject_mass]
type = PorousFlowPointSourceFromPostprocessor
variable = p
mass_flux = mass_flux_in
point = '-500 0 0'
[]
# [inject_heat]
# type = PorousFlowPointEnthalpySourceFromPostprocessor
# variable = T
# mass_flux = mass_flux_in
# point = '-500 0 0'
# T_in = T_in
# pressure = porepressure
# fp = the_simple_fluid
# []
[produce_H2O_1]
type = PorousFlowPolyLineSink
SumQuantityUO = produced_mass_H2O1
fluxes = 10
p_or_t_vals = 0.0
line_length = 1.0
point_file = /Users/morteza/Documents/projects/moose/modules/porous_flow/1.bh
variable = p
[]
[remove_heat_at_production_well_1]
type = PorousFlowPolyLineSink
SumQuantityUO = produced_heat1
fluxes = 10
p_or_t_vals = 0.0
line_length = 1.0
use_enthalpy = true
point_file = /Users/morteza/Documents/projects/moose/modules/porous_flow/1.bh
variable = T
[]
[]
# [Executioner]
# type = Transient
# solve_type = Newton
# end_time = 900000000
# # dt = 2E5
# dt = 2E5
# nl_abs_tol = 1e-9
# []
# [Postprocessors]
# [belphip]
# type = PointValue
# variable = porepressure
# point = '1500 0 0'
# outputs = 'csv'
# []
# [belphit]
# type = PointValue
# variable = temperature
# point = '1500 0 0'
# outputs = 'csv'
# []
# []
# [Postprocessors]
# [belphip]
# type = PointValue
# variable = porepressure
# point = '1500 0 0'
# outputs = 'csv'
# []
# [belphit]
# type = PointValue
# variable = temperature
# point = '1500 0 0'
# outputs = 'csv'
# []
# []
[MultiApps]
[./coupled2]
positions = '1500 0 0'
type = TransientMultiApp
input_files = /Users/morteza/Documents/projects/moskito2/production.i
app_type = MoskitoApp
execute_on = TIMESTEP_END
sub_cycling = true
[../]
[]
[Transfers]
[P_transfer2]
type = MultiAppPostprocessorTransfer
to_multi_app = coupled2
from_postprocessor = P_value2
to_postprocessor = P_receiver3
[]
[T_transfer2]
type = MultiAppPostprocessorTransfer
to_multi_app = coupled2
from_postprocessor = T_value2
to_postprocessor = T_receiver3
[]
[Q_transfer2]
type = MultiAppPostprocessorTransfer
to_multi_app = coupled2
from_postprocessor = Q_value2
to_postprocessor = Q_receiver3
[]
[]