- T_c0Critical temperature, K
Default:0
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Critical temperature, K
- e_c0Internal energy at the critical point, J/kg
Default:0
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Internal energy at the critical point, J/kg
- e_ref0Reference specific internal energy [J/kg]
Default:0
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Reference specific internal energy [J/kg]
- emit_on_nannoneWhether to raise a warning, an exception (usually triggering a retry with a smaller time step) or an error (ending the simulation)
Default:none
C++ Type:MooseEnum
Controllable:No
Description:Whether to raise a warning, an exception (usually triggering a retry with a smaller time step) or an error (ending the simulation)
- gamma1.4gamma value (cp/cv)
Default:1.4
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:gamma value (cp/cv)
- k0.02568Thermal conductivity, W/(m-K)
Default:0.02568
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Thermal conductivity, W/(m-K)
- molar_mass0.029Constant molar mass of the fluid (kg/mol)
Default:0.029
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Constant molar mass of the fluid (kg/mol)
- mu1.823e-05Dynamic viscosity, Pa.s
Default:1.823e-05
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Dynamic viscosity, Pa.s
- rho_c0Critical density, kg/m3
Default:0
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Critical density, kg/m3
IdealGasFluidProperties
These fluid properties implement the ideal gas law:
where
is pressure,
is specific volume,
is the universal gas constant,
is the temperature (in absolute units), and
is the molar mass.
The specific heats (isobaric, , and isochoric, ) are assumed constant, and thus their ratio is constant as well:
The specific internal energy is computed as
where is a reference specific internal energy value (corresponding to ).
The dynamic viscosity and thermal conductivity are assumed constant, though this assumption could later be dropped.
Input Parameters
- T_initial_guess400Temperature initial guess for Newton Method variable set conversion
Default:400
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Temperature initial guess for Newton Method variable set conversion
- max_newton_its100Maximum number of Newton iterations for variable set conversions
Default:100
C++ Type:unsigned int
Controllable:No
Description:Maximum number of Newton iterations for variable set conversions
- p_initial_guess200000Pressure initial guess for Newton Method variable set conversion
Default:200000
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Pressure initial guess for Newton Method variable set conversion
- tolerance1e-08Tolerance for 2D Newton variable set conversion
Default:1e-08
C++ Type:double
Unit:(no unit assumed)
Controllable:No
Description:Tolerance for 2D Newton variable set conversion
Variable Set Conversions Newton Solve Parameters
- allow_imperfect_jacobiansFalsetrue to allow unimplemented property derivative terms to be set to zero for the AD API
Default:False
C++ Type:bool
Controllable:No
Description:true to allow unimplemented property derivative terms to be set to zero for the AD API
- control_tagsAdds user-defined labels for accessing object parameters via control logic.
C++ Type:std::vector<std::string>
Controllable:No
Description:Adds user-defined labels for accessing object parameters via control logic.
- enableTrueSet the enabled status of the MooseObject.
Default:True
C++ Type:bool
Controllable:Yes
Description:Set the enabled status of the MooseObject.
- fp_typesingle-phase-fpType of the fluid property object
Default:single-phase-fp
C++ Type:FPType
Controllable:No
Description:Type of the fluid property object
Advanced Parameters
- prop_getter_suffixAn optional suffix parameter that can be appended to any attempt to retrieve/get material properties. The suffix will be prepended with a '_' character.
C++ Type:MaterialPropertyName
Unit:(no unit assumed)
Controllable:No
Description:An optional suffix parameter that can be appended to any attempt to retrieve/get material properties. The suffix will be prepended with a '_' character.
- use_interpolated_stateFalseFor the old and older state use projected material properties interpolated at the quadrature points. To set up projection use the ProjectedStatefulMaterialStorageAction.
Default:False
C++ Type:bool
Controllable:No
Description:For the old and older state use projected material properties interpolated at the quadrature points. To set up projection use the ProjectedStatefulMaterialStorageAction.
Material Property Retrieval Parameters
Input Files
- (modules/navier_stokes/test/tests/finite_volume/cns/straight_channel_porosity_step/hllc.i)
- (modules/thermal_hydraulics/test/tests/problems/area_constriction/area_constriction.i)
- (modules/thermal_hydraulics/test/tests/problems/william_louis/3pipes_open.i)
- (modules/fluid_properties/test/tests/fp_interrogator/1ph.rho_e.i)
- (modules/thermal_hydraulics/test/tests/output/paraview_component_annotation_map/test.i)
- (modules/fluid_properties/test/tests/two_phase_ncg_partial_pressure/test.i)
- (modules/thermal_hydraulics/test/tests/components/shaft_connected_turbine_1phase/shaft_motor_turbine.i)
- (modules/thermal_hydraulics/tutorials/single_phase_flow/04_loop.i)
- (modules/thermal_hydraulics/test/tests/problems/super_sonic_tube/test.i)
- (modules/navier_stokes/test/tests/ics/test_function.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/heated-channel/transient-porous-kt-primitive.i)
- (modules/thermal_hydraulics/tutorials/single_phase_flow/03_upper_loop.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/varying-eps-hllc.i)
- (modules/fluid_properties/fp_interrogator/fp_interrogator.i)
- (modules/fluid_properties/test/tests/fp_interrogator/2ph.T.i)
- (modules/thermal_hydraulics/test/tests/components/junction_parallel_channels_1phase/phy.shower.i)
- (modules/thermal_hydraulics/test/tests/components/shaft_connected_pump_1phase/shaft_motor_pump.i)
- (modules/thermal_hydraulics/test/tests/components/junction_one_to_one_1phase/no_junction_1phase.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/porous-hllc.i)
- (modules/thermal_hydraulics/test/tests/components/inlet_stagnation_enthalpy_1phase/phy.h_rhou_3eqn.i)
- (modules/fluid_properties/test/tests/fp_interrogator/2ph.p.i)
- (modules/porous_flow/test/tests/newton_cooling/nc08.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/scalar_advection/mass-frac-advection.i)
- (modules/navier_stokes/test/tests/finite_element/cns/step/step.i)
- (modules/thermal_hydraulics/test/tests/components/simple_turbine_1phase/phy.conservation.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/varying-eps-basic-kt-mixed.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/straight-channel-hllc.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/userobject/HLLC/hllc_uo_2D_tri.i)
- (modules/fluid_properties/test/tests/fp_interrogator/vapor_mixture_rho_e.i)
- (modules/navier_stokes/test/tests/finite_element/cns/bump/bump.i)
- (modules/thermal_hydraulics/test/tests/components/shaft_connected_compressor_1phase/shaft_motor_compressor.i)
- (modules/fluid_properties/test/tests/ideal_gas/test.i)
- (modules/fluid_properties/test/tests/fp_interrogator/2ph.p_T.i)
- (modules/fluid_properties/test/tests/ideal_gas/test2.i)
- (modules/navier_stokes/test/tests/finite_volume/materials/ergun/ergun.i)
- (modules/porous_flow/test/tests/jacobian/esbc01.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/implicit_bcs/hllc_sod_shocktube.i)
- (modules/thermal_hydraulics/test/tests/components/flow_channel_1phase/steady.i)
- (modules/thermal_hydraulics/tutorials/single_phase_flow/01_flow_channel.i)
- (modules/thermal_hydraulics/test/tests/components/simple_turbine_1phase/phy.test.i)
- (modules/thermal_hydraulics/test/tests/problems/natural_circulation/base.i)
- (modules/thermal_hydraulics/test/tests/components/shaft_connected_pump_1phase/pump_coastdown.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/symmetry_test/2D_symmetry.i)
- (modules/thermal_hydraulics/test/tests/materials/binary_diffusion_coef/binary_diffusion_coef.i)
- (modules/navier_stokes/test/tests/finite_volume/two_phase/mixture_interface_area_model/turbulent_driven_growth.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/stagnation_inlet/supersonic_nozzle_hllc.i)
- (modules/thermal_hydraulics/test/tests/components/deprecated/gate_valve.i)
- (modules/fluid_properties/test/tests/fp_interrogator/1ph.rho_p.i)
- (modules/thermal_hydraulics/test/tests/components/heat_transfer_from_external_app_1phase/phy.q_wall_transfer_3eqn.child.i)
- (modules/thermal_hydraulics/test/tests/problems/sod_shock_tube/sod_shock_tube.i)
- (modules/thermal_hydraulics/test/tests/problems/mms/mms_1phase.i)
- (modules/thermal_hydraulics/tutorials/single_phase_flow/06_custom_closures.i)
- (modules/thermal_hydraulics/test/tests/materials/fluid_properties_gas_mix_material/fluid_properties_gas_mix_material.i)
- (modules/thermal_hydraulics/test/tests/components/deprecated/solid_wall.i)
- (modules/fluid_properties/test/tests/fp_interrogator/2ph_ncg_p_T.i)
- (modules/porous_flow/test/tests/fluids/ideal_gas.i)
- (modules/fluid_properties/test/tests/two_phase_fluid_properties_independent/test.i)
- (modules/navier_stokes/test/tests/finite_volume/two_phase/mixture_interface_area_model/pressure_driven_growth.i)
- (modules/thermal_hydraulics/test/tests/ics/flow_model_gas_mix_ic/flow_model_gas_mix_ic.i)
- (modules/thermal_hydraulics/test/tests/components/heat_transfer_from_specified_temperature_1phase/err.no_phf.i)
- (modules/thermal_hydraulics/test/tests/misc/coupling_mD_flow/thm_non_overlapping.i)
- (modules/thermal_hydraulics/test/tests/postprocessors/heat_rate_convection_1phase/heat_rate_convection_1phase.i)
- (modules/thermal_hydraulics/test/tests/components/heat_transfer_from_heat_structure_1phase/err.1phase.i)
- (modules/thermal_hydraulics/test/tests/problems/pressure_drop/pressure_drop_with_junction.i)
- (modules/thermal_hydraulics/tutorials/single_phase_flow/02_core.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/regular-straight-channel.i)
- (modules/fluid_properties/test/tests/fluid_properties/ideal_gas_mixture/ideal_gas_mixture.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/straight_channel_porosity_step/rotated-2d-bkt-function-porosity.i)
- (modules/navier_stokes/test/tests/finite_volume/two_phase/mixture_interface_area_model/pressure_driven_growth_transient.i)
- (modules/thermal_hydraulics/test/tests/components/heat_transfer_from_heat_structure_1phase/jac.1phase.i)
- (modules/navier_stokes/test/tests/ics/test.i)
- (modules/thermal_hydraulics/test/tests/problems/lax_shock_tube/lax_shock_tube.i)
- (modules/thermal_hydraulics/test/tests/postprocessors/flow_junction_flux_1phase/flow_junction_flux_1phase.i)
- (modules/thermal_hydraulics/test/tests/components/deprecated/junction_one_to_one.i)
- (modules/thermal_hydraulics/test/tests/components/supersonic_inlet/err.i)
- (modules/thermal_hydraulics/test/tests/problems/woodward_colella_blast_wave/woodward_colella_blast_wave.i)
- (modules/thermal_hydraulics/test/tests/closures/wall_temperature_1phase/base.i)
- (modules/thermal_hydraulics/test/tests/components/deprecated/free_boundary.i)
- (modules/navier_stokes/test/tests/finite_volume/wcns/natural_convection/natural_circulation_pipe.i)
- (modules/navier_stokes/test/tests/finite_volume/ins/boussinesq/wcnsfv.i)
- (modules/thermal_hydraulics/test/tests/problems/area_constriction/area_constriction_junction.i)
- (modules/thermal_hydraulics/test/tests/postprocessors/specific_impulse_1phase/Isp_1ph.i)
- (modules/thermal_hydraulics/test/tests/auxkernels/flow_model_gas_mix_aux/flow_model_gas_mix_aux.i)
- (modules/thermal_hydraulics/test/tests/materials/ad_wall_htc_gnielinski_annular/ad_wall_htc_gnielinski_annular.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/basic-conserved-pcnsfv-kt.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/straight_channel_porosity_step/implicit-euler-basic-kt-primitive.i)
- (modules/thermal_hydraulics/test/tests/components/junction_one_to_one_1phase/junction_one_to_one_1phase.i)
- (modules/fluid_properties/test/tests/fp_interrogator/1ph.rho_rhou_rhoE.i)
- (modules/fluid_properties/test/tests/fp_interrogator/1ph.p_T.i)
- (modules/thermal_hydraulics/tutorials/single_phase_flow/05_secondary_side.i)
- (modules/porous_flow/test/tests/jacobian/esbc02.i)
- (modules/fluid_properties/test/tests/materials/fluid_properties_material/test_ve.i)
- (modules/thermal_hydraulics/test/tests/problems/square_wave/square_wave.i)
- (modules/thermal_hydraulics/test/tests/problems/sedov_blast_wave/sedov_blast_wave.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/pressure_outlet/subsonic_nozzle_fixed_inflow_hllc.i)
- (modules/thermal_hydraulics/test/tests/components/component/err.nonexisting_component.i)
- (modules/thermal_hydraulics/test/tests/components/gate_valve_1phase/gate_valve_1phase.i)
- (modules/fluid_properties/test/tests/tabulated/tabulated_v_e.i)
- (modules/thermal_hydraulics/test/tests/components/flow_channel_gasmix/flow_channel_gasmix.i)
- (modules/navier_stokes/test/tests/finite_volume/pwcns/channel-flow/2d-transient-gas.i)
- (modules/navier_stokes/test/tests/ics/pns_test.i)
- (modules/fluid_properties/test/tests/functions/saturation_pressure_function/saturation_pressure_function.i)
- (modules/thermal_hydraulics/test/tests/problems/brayton_cycle/recuperated_brayton_cycle.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/userobject/HLLC/hllc_uo_1D.i)
- (modules/thermal_hydraulics/test/tests/components/flow_connection/err.connection_format.i)
- (modules/thermal_hydraulics/test/tests/problems/brayton_cycle/closed_brayton_cycle.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/basic-primitive-pcnsfv-kt.i)
- (modules/thermal_hydraulics/test/tests/problems/double_rarefaction/1phase.i)
- (modules/thermal_hydraulics/test/tests/components/shaft_connected_turbine_1phase/turbine_startup.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/straight_channel_porosity_step/rotated-2d-bkt-function-porosity-mixed.i)
- (modules/fluid_properties/test/tests/fp_interrogator/err.no_params.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/free-flow-hllc.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/varying-eps-basic-kt-primitive.i)
- (modules/thermal_hydraulics/test/tests/components/junction_one_to_one_1phase/constriction_1phase.i)
- (modules/thermal_hydraulics/test/tests/problems/pressure_drop/pressure_drop.i)
- (modules/thermal_hydraulics/test/tests/components/heat_transfer_from_heat_structure_1phase/hs_boundary.i)
- (modules/navier_stokes/test/tests/finite_volume/ins/boussinesq/transient-wcnsfv.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/benchmark_shock_tube_1D/hllc_sod_shocktube.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/straight_channel_porosity_step/dc.i)
- (modules/fluid_properties/test/tests/fp_interrogator/2ph_ncg_partial_pressure_p_T.i)
- (modules/fluid_properties/test/tests/materials/fluid_properties_material/test_ph.i)
- (modules/fluid_properties/test/tests/functions/saturation_density_function/saturation_density_function.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/pwcnsfv.i)
- (modules/navier_stokes/test/tests/finite_volume/cns/shock_tube_2D_cavity/hllc_sod_shocktube_2D.i)
- (modules/thermal_hydraulics/test/tests/components/heat_transfer_from_heat_structure_1phase/phy.heat_structure_multiple_3eqn.i)
- (modules/thermal_hydraulics/test/tests/problems/william_louis/4pipes_closed.i)
- (modules/thermal_hydraulics/test/tests/functormaterials/conjugate_ht_numbers/conjugate_ht_numbers.i)
- (modules/thermal_hydraulics/test/tests/output/vector_velocity/test.i)
- (modules/fluid_properties/test/tests/materials/fluid_properties_material/test_pt.i)
- (modules/thermal_hydraulics/test/tests/problems/brayton_cycle/open_brayton_cycle.i)
- (modules/fluid_properties/test/tests/ics/rho_vapor_mixture_from_pressure_temperature/test.i)
- (modules/fluid_properties/test/tests/functions/saturation_temperature_function/saturation_temperature_function.i)
Child Objects
(modules/navier_stokes/test/tests/finite_volume/cns/straight_channel_porosity_step/hllc.i)
p_initial=1.01e5
T=273.15
# u refers to the superficial velocity
u_in=1
[GlobalParams]
fp = fp
two_term_boundary_expansion = true
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 1
xmin = 0
xmax = 18
nx = 180
[]
[to_pt5]
input = cartesian
type = SubdomainBoundingBoxGenerator
bottom_left = '2 0 0'
top_right = '4 1 0'
block_id = 1
[]
[pt5]
input = to_pt5
type = SubdomainBoundingBoxGenerator
bottom_left = '4 0 0'
top_right = '6 1 0'
block_id = 2
[]
[to_pt25]
input = pt5
type = SubdomainBoundingBoxGenerator
bottom_left = '6 0 0'
top_right = '8 1 0'
block_id = 3
[]
[pt25]
input = to_pt25
type = SubdomainBoundingBoxGenerator
bottom_left = '8 0 0'
top_right = '10 1 0'
block_id = 4
[]
[to_pt5_again]
input = pt25
type = SubdomainBoundingBoxGenerator
bottom_left = '10 0 0'
top_right = '12 1 0'
block_id = 5
[]
[pt5_again]
input = to_pt5_again
type = SubdomainBoundingBoxGenerator
bottom_left = '12 0 0'
top_right = '14 1 0'
block_id = 6
[]
[to_one]
input = pt5_again
type = SubdomainBoundingBoxGenerator
bottom_left = '14 0 0'
top_right = '16 1 0'
block_id = 7
[]
[one]
input = to_one
type = SubdomainBoundingBoxGenerator
bottom_left = '16 0 0'
top_right = '18 1 0'
block_id = 8
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Problem]
fv_bcs_integrity_check = false
[]
[Variables]
[pressure]
type = MooseVariableFVReal
initial_condition = ${p_initial}
[]
[sup_vel_x]
type = MooseVariableFVReal
initial_condition = 1
scaling = 1e-2
[]
[T_fluid]
type = MooseVariableFVReal
initial_condition = ${T}
scaling = 1e-5
[]
[]
[AuxVariables]
[vel_x]
type = MooseVariableFVReal
[]
[sup_mom_x]
type = MooseVariableFVReal
[]
[rho]
type = MooseVariableFVReal
[]
[worst_courant]
type = MooseVariableFVReal
[]
[porosity]
type = MooseVariableFVReal
[]
[]
[AuxKernels]
[vel_x]
type = ADMaterialRealAux
variable = vel_x
property = vel_x
execute_on = 'timestep_end'
[]
[sup_mom_x]
type = ADMaterialRealAux
variable = sup_mom_x
property = superficial_rhou
execute_on = 'timestep_end'
[]
[rho]
type = ADMaterialRealAux
variable = rho
property = rho
execute_on = 'timestep_end'
[]
[worst_courant]
type = Courant
variable = worst_courant
u = sup_vel_x
execute_on = 'timestep_end'
[]
[porosity]
type = MaterialRealAux
variable = porosity
property = porosity
execute_on = 'timestep_end'
[]
[]
[FVKernels]
[mass_advection]
type = PCNSFVMassHLLC
variable = pressure
[]
[momentum_advection]
type = PCNSFVMomentumHLLC
variable = sup_vel_x
momentum_component = 'x'
[]
[eps_grad]
type = PNSFVPGradEpsilon
variable = sup_vel_x
momentum_component = 'x'
epsilon_function = 'eps'
[]
[energy_advection]
type = PCNSFVFluidEnergyHLLC
variable = T_fluid
[]
[]
[FVBCs]
[rho_left]
type = PCNSFVStrongBC
boundary = 'left'
variable = pressure
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'mass'
[]
[rhou_left]
type = PCNSFVStrongBC
boundary = 'left'
variable = sup_vel_x
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'momentum'
momentum_component = 'x'
[]
[rho_et_left]
type = PCNSFVStrongBC
boundary = 'left'
variable = T_fluid
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'energy'
[]
[rho_right]
type = PCNSFVStrongBC
boundary = 'right'
variable = pressure
pressure = ${p_initial}
eqn = 'mass'
[]
[rhou_right]
type = PCNSFVStrongBC
boundary = 'right'
variable = sup_vel_x
pressure = ${p_initial}
eqn = 'momentum'
momentum_component = 'x'
[]
[rho_et_right]
type = PCNSFVStrongBC
boundary = 'right'
variable = T_fluid
pressure = ${p_initial}
eqn = 'energy'
[]
# Use these to help create more accurate cell centered gradients for cells adjacent to boundaries
[T_left]
type = FVDirichletBC
variable = T_fluid
value = ${T}
boundary = 'left'
[]
[sup_vel_left]
type = FVDirichletBC
variable = sup_vel_x
value = ${u_in}
boundary = 'left'
[]
[p_right]
type = FVDirichletBC
variable = pressure
value = ${p_initial}
boundary = 'right'
[]
[]
[Functions]
[ud_in]
type = ParsedVectorFunction
expression_x = '${u_in}'
[]
[eps]
type = ParsedFunction
expression = 'if(x < 2, 1,
if(x < 4, 1 - .5 / 2 * (x - 2),
if(x < 6, .5,
if(x < 8, .5 - .25 / 2 * (x - 6),
if(x < 10, .25,
if(x < 12, .25 + .25 / 2 * (x - 10),
if(x < 14, .5,
if(x < 16, .5 + .5 / 2 * (x - 14),
1))))))))'
[]
[]
[Materials]
[var_mat]
type = PorousPrimitiveVarMaterial
pressure = pressure
T_fluid = T_fluid
superficial_vel_x = sup_vel_x
porosity = porosity
[]
[porosity]
type = GenericFunctionMaterial
prop_names = 'porosity'
prop_values = 'eps'
[]
[]
[Executioner]
solve_type = NEWTON
line_search = 'bt'
type = Steady
[]
[Outputs]
[out]
type = Exodus
execute_on = 'final'
[]
checkpoint = true
[]
[Debug]
show_var_residual_norms = true
[]
(modules/thermal_hydraulics/test/tests/problems/area_constriction/area_constriction.i)
# This test features air flowing through a channel whose cross-sectional area
# shrinks to half its value in the right half. Assuming incompressible flow
# conditions, such as having a low Mach number, the velocity should approximately
# double from inlet to outlet.
p_outlet = 1e5
[GlobalParams]
gravity_vector = '0 0 0'
initial_T = 300
initial_p = ${p_outlet}
initial_vel = initial_vel_fn
fp = fp
closures = simple_closures
f = 0
scaling_factor_1phase = '1 1 1e-5'
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Functions]
[A_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.5 1.0'
y = '1.0 0.5'
[]
[initial_vel_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.5 1.0'
y = '1.0 2'
[]
[]
[Components]
[inlet]
type = InletDensityVelocity1Phase
input = 'pipe:in'
rho = 1.16263315948279 # rho @ (p = 1e5 Pa, T = 300 K)
vel = 1
[]
[pipe]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 1
n_elems = 100
A = A_fn
[]
[outlet]
type = Outlet1Phase
input = 'pipe:out'
p = ${p_outlet}
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'bdf2'
end_time = 10
[TimeStepper]
type = IterationAdaptiveDT
dt = 0.001
optimal_iterations = 5
iteration_window = 1
growth_factor = 1.2
[]
steady_state_detection = true
solve_type = PJFNK
nl_rel_tol = 1e-10
nl_abs_tol = 1e-8
nl_max_its = 15
l_tol = 1e-3
l_max_its = 10
[]
[Outputs]
exodus = true
velocity_as_vector = false
show = 'A rho vel p'
[]
(modules/thermal_hydraulics/test/tests/problems/william_louis/3pipes_open.i)
# Junction of 3 pipes:
#
# 1 3
# -----*-----
# | 2
#
# The left end of Pipe 1 is a high-pressure region, and the rest of the system
# is at a low pressure.
#
# Pipe 1 is closed, while Pipes 2 and 3 are open.
end_time = 0.07
D_pipe = 0.01
A_pipe = ${fparse 0.25 * pi * D_pipe^2}
length_pipe1_HP = 0.53
length_pipe1_LP = 3.10
length_pipe2 = 2.595
length_pipe3 = 1.725
x_junction = ${fparse length_pipe1_HP + length_pipe1_LP}
# Numbers of elements correspond to dx ~ 1/3 cm
n_elems_pipe1_HP = 159
n_elems_pipe1_LP = 930
n_elems_pipe2 = 779
n_elems_pipe3 = 518
S_junction = ${fparse 3 * A_pipe}
r_junction = ${fparse sqrt(S_junction / (4 * pi))}
V_junction = ${fparse 4/3 * pi * r_junction^3}
p_low = 1e5
p_high = 1.15e5
T_low = 283.5690633 # at p = 1e5 Pa, rho = 1.23 kg/m^3
T_high = 283.5690633 # at p = 1.15e5 Pa, rho = 1.4145 kg/m^3
cfl = 0.95
[GlobalParams]
# common FlowChannel1Phase parameters
A = ${A_pipe}
initial_vel = 0
fp = fp_air
closures = closures
f = 0
gravity_vector = '0 0 0'
scaling_factor_1phase = '1 1 1e-5'
[]
[FluidProperties]
[fp_air]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.029
[]
[]
[Closures]
[closures]
type = Closures1PhaseSimple
[]
[]
[Functions]
[initial_T_pipe1_fn]
type = PiecewiseConstant
axis = x
x = '0 ${length_pipe1_HP}'
y = '${T_high} ${T_low}'
[]
[initial_p_pipe1_fn]
type = PiecewiseConstant
axis = x
x = '0 ${length_pipe1_HP}'
y = '${p_high} ${p_low}'
[]
[]
[Components]
[pipe1_wall]
type = SolidWall1Phase
input = 'pipe1:in'
[]
[pipe1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = '${length_pipe1_HP} ${length_pipe1_LP}'
n_elems = '${n_elems_pipe1_HP} ${n_elems_pipe1_LP}'
initial_p = initial_p_pipe1_fn
initial_T = initial_T_pipe1_fn
[]
[junction]
type = VolumeJunction1Phase
position = '${x_junction} 0 0'
connections = 'pipe1:out pipe2:in pipe3:in'
initial_p = ${p_low}
initial_T = ${T_low}
initial_vel_x = 0
initial_vel_y = 0
initial_vel_z = 0
volume = ${V_junction}
scaling_factor_rhoEV = 1e-5
apply_velocity_scaling = true
[]
[pipe2]
type = FlowChannel1Phase
position = '${x_junction} 0 0'
orientation = '0 -1 0'
length = ${length_pipe2}
n_elems = ${n_elems_pipe2}
initial_p = ${p_low}
initial_T = ${T_low}
[]
[pipe2_outlet]
type = Outlet1Phase
input = 'pipe2:out'
p = ${p_low}
[]
[pipe3]
type = FlowChannel1Phase
position = '${x_junction} 0 0'
orientation = '1 0 0'
length = ${length_pipe3}
n_elems = ${n_elems_pipe3}
initial_p = ${p_low}
initial_T = ${T_low}
[]
[pipe3_outlet]
type = Outlet1Phase
input = 'pipe3:out'
p = ${p_low}
[]
[]
[Postprocessors]
[cfl_dt]
type = ADCFLTimeStepSize
block = 'pipe1 pipe2 pipe3'
CFL = ${cfl}
c_names = 'c'
vel_names = 'vel'
[]
[p_pipe1_048]
type = PointValue
variable = p
point = '${fparse x_junction - 0.48} 0 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_pipe2_052]
type = PointValue
variable = p
point = '${fparse x_junction} -0.52 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_pipe3_048]
type = PointValue
variable = p
point = '${fparse x_junction + 0.48} 0 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
end_time = ${end_time}
[TimeIntegrator]
type = ExplicitSSPRungeKutta
order = 1
[]
[TimeStepper]
type = PostprocessorDT
postprocessor = cfl_dt
[]
abort_on_solve_fail = true
solve_type = LINEAR
[]
[Times]
[output_times]
type = TimeIntervalTimes
time_interval = 7e-4
[]
[]
[Outputs]
file_base = '3pipes_open'
[csv]
type = CSV
show = 'p_pipe1_048 p_pipe2_052 p_pipe3_048'
sync_only = true
sync_times_object = output_times
[]
[console]
type = Console
execute_postprocessors_on = 'NONE'
[]
[]
(modules/fluid_properties/test/tests/fp_interrogator/1ph.rho_e.i)
[FluidPropertiesInterrogator]
fp = fp
rho = 1
e = 2.1502500000e+05
[]
[FluidProperties]
[./fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02900055737704918
mu = 1.823e-05
k = 0.02568
[../]
[]
(modules/thermal_hydraulics/test/tests/output/paraview_component_annotation_map/test.i)
[GlobalParams]
initial_p = 1e5
initial_T = 300
initial_vel = 0
closures = simple_closures
f = 0
fp = fp
gravity_vector = '0 0 0'
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[SolidProperties]
[m]
type = ThermalFunctionSolidProperties
rho = 1
cp = 1
k = 1
[]
[]
[Components]
[fch1]
type = FlowChannel1Phase
position = '-0.1 0 0'
orientation = '0 0 1'
length = 1
A = 1
n_elems = 10
[]
[wall1i]
type = SolidWall1Phase
input = fch1:in
[]
[wall1o]
type = SolidWall1Phase
input = fch1:out
[]
[hs1]
type = HeatStructureCylindrical
position = '-0.2 0 0'
orientation = '0 0 1'
length = 1
n_elems = 10
names = '1 2'
widths = '0.2 0.3'
solid_properties = 'm m'
solid_properties_T_ref = '300 300'
n_part_elems = '1 1'
rotation = 90
[]
[fch2]
type = FlowChannel1Phase
position = '0.1 0 0'
orientation = '0 0 1'
length = '0.6 0.4'
A = 1
n_elems = '5 5'
axial_region_names = 'longer shorter'
[]
[wall2i]
type = SolidWall1Phase
input = fch2:in
[]
[wall2o]
type = SolidWall1Phase
input = fch2:out
[]
[hs2]
type = HeatStructureCylindrical
position = '0.2 0 0'
orientation = '0 0 1'
length = '0.6 0.4'
axial_region_names = 'longer shorter'
n_elems = '5 5'
names = '1 2'
widths = '0.2 0.3'
solid_properties = 'm m'
solid_properties_T_ref = '300 300'
n_part_elems = '1 1'
rotation = 270
[]
[]
[Executioner]
type = Transient
dt = 0.1
num_steps = 1
automatic_scaling = true
nl_abs_tol = 1e-7
[]
[Outputs]
[map]
type = ParaviewComponentAnnotationMap
[]
[]
(modules/fluid_properties/test/tests/two_phase_ncg_partial_pressure/test.i)
p = 40e3
T = 300
[Mesh]
type = GeneratedMesh
dim = 1
nx = 1
[]
[FluidProperties]
[fp_water]
type = StiffenedGasFluidProperties
gamma = 2.35
cv = 1816.0
q = -1.167e6
p_inf = 1.0e9
q_prime = 0
k = 0.5
mu = 281.8e-6
M = 0.01801488
[]
[fp_steam]
type = IdealGasFluidProperties
gamma = 1.43
molar_mass = 0.01801488
[]
[fp_air]
type = IdealGasFluidProperties
[]
[fp_2phase]
type = TestTwoPhaseFluidProperties
fp_liquid = fp_water
fp_vapor = fp_steam
[]
[fp_2phase_ncg]
type = TwoPhaseNCGPartialPressureFluidProperties
fp_2phase = fp_2phase
fp_ncg = fp_air
[]
[]
[Functions]
[p_sat_fn]
type = TwoPhaseNCGPartialPressureFunction
fluid_properties = fp_2phase_ncg
property_call = p_sat
arg1 = ${T}
[]
[x_sat_ncg_fn]
type = TwoPhaseNCGPartialPressureFunction
fluid_properties = fp_2phase_ncg
property_call = x_sat_ncg_from_p_T
arg1 = ${p}
arg2 = ${T}
[]
[]
[Postprocessors]
[p_sat]
type = FunctionValuePostprocessor
function = p_sat_fn
execute_on = 'INITIAL'
[]
[x_sat_ncg]
type = FunctionValuePostprocessor
function = x_sat_ncg_fn
execute_on = 'INITIAL'
[]
[]
[Problem]
solve = false
[]
[Executioner]
type = Steady
[]
[Outputs]
execute_on = 'INITIAL'
csv = true
[]
(modules/thermal_hydraulics/test/tests/components/shaft_connected_turbine_1phase/shaft_motor_turbine.i)
area = 0.2359
dt = 1.e-3
[GlobalParams]
initial_p = 2e5
initial_T = 600
initial_vel = 100
initial_vel_x = 100
initial_vel_y = 0
initial_vel_z = 0
A = ${area}
A_ref = ${area}
f = 100
scaling_factor_1phase = '0.04 0.04 0.04e-5'
closures = simple_closures
fp = fp
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[turbine]
type = ShaftConnectedTurbine1Phase
inlet = 'pipe:out'
outlet = 'pipe:in'
position = '0 0 0'
volume = 0.2
inertia_coeff = '1 1 1 1'
inertia_const = 1.61397
speed_cr_I = 1e12
speed_cr_fr = 0
tau_fr_coeff = '0 0 0 0'
tau_fr_const = 0
omega_rated = 100
D_wheel = 0.4
head_coefficient = head
power_coefficient = power
[]
[pipe]
type = FlowChannel1Phase
position = '0.1 0 0'
orientation = '1 0 0'
length = 10
n_elems = 20
initial_p = 2e6
[]
[dyno]
type = ShaftConnectedMotor
inertia = 1e2
torque = -1e3
[]
[shaft]
type = Shaft
connected_components = 'dyno turbine'
initial_speed = 300
[]
[]
[Functions]
[head]
type = PiecewiseLinear
x = '0 7e-3 1e-2'
y = '0 15 20'
[]
[power]
type = PiecewiseLinear
x = '0 6e-3 1e-2'
y = '0 0.05 0.18'
[]
[S_energy_fcn]
type = ParsedFunction
expression = '-(tau_driving+tau_fr)*omega'
symbol_names = 'tau_driving tau_fr omega'
symbol_values = 'driving_torque friction_torque shaft:omega'
[]
[energy_conservation_fcn]
type = ParsedFunction
expression = '(E_change - S_energy * dt) / E_tot'
symbol_names = 'E_change S_energy dt E_tot'
symbol_values = 'E_change S_energy ${dt} E_tot'
[]
[]
[Postprocessors]
[driving_torque]
type = ElementAverageValue
variable = driving_torque
block = 'turbine'
execute_on = 'initial timestep_end'
[]
[friction_torque]
type = ElementAverageValue
variable = friction_torque
block = 'turbine'
execute_on = 'initial timestep_end'
[]
# mass conservation
[mass_pipes]
type = ElementIntegralVariablePostprocessor
variable = rhoA
block = 'pipe'
execute_on = 'initial timestep_end'
[]
[mass_turbine]
type = ElementAverageValue
variable = rhoV
block = 'turbine'
execute_on = 'initial timestep_end'
[]
[mass_tot]
type = SumPostprocessor
values = 'mass_pipes mass_turbine'
execute_on = 'initial timestep_end'
[]
[mass_conservation]
type = ChangeOverTimePostprocessor
postprocessor = mass_tot
change_with_respect_to_initial = true
compute_relative_change = true
execute_on = 'initial timestep_end'
[]
# energy conservation
[E_pipes]
type = ElementIntegralVariablePostprocessor
variable = rhoEA
block = 'pipe'
execute_on = 'initial timestep_end'
[]
[E_turbine]
type = ElementAverageValue
variable = rhoEV
block = 'turbine'
execute_on = 'initial timestep_end'
[]
[E_tot]
type = LinearCombinationPostprocessor
pp_coefs = '1 1'
pp_names = 'E_pipes E_turbine'
execute_on = 'initial timestep_end'
[]
[S_energy]
type = FunctionValuePostprocessor
function = S_energy_fcn
indirect_dependencies = 'driving_torque friction_torque'
execute_on = 'initial timestep_end'
[]
[E_change]
type = ChangeOverTimePostprocessor
postprocessor = E_tot
execute_on = 'initial timestep_end'
[]
# This should also execute on initial. This value is
# lagged by one timestep as a workaround to moose issue #13262.
[energy_conservation]
type = FunctionValuePostprocessor
function = energy_conservation_fcn
execute_on = 'timestep_end'
[]
[]
[Preconditioning]
[SMP]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'implicit-euler'
dt = ${dt}
num_steps = 6
solve_type = NEWTON
nl_rel_tol = 1e-8
nl_abs_tol = 1e-6
nl_max_its = 15
l_tol = 1e-4
l_max_its = 10
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
[Quadrature]
type = GAUSS
order = SECOND
[]
[]
[Outputs]
velocity_as_vector = false
[]
(modules/thermal_hydraulics/tutorials/single_phase_flow/04_loop.i)
T_in = 300. # K
m_dot_in = 1e-2 # kg/s
press = 10e5 # Pa
# core parameters
core_length = 1. # m
core_n_elems = 25
core_dia = '${units 2. cm -> m}'
core_pitch = '${units 8.7 cm -> m}'
# pipe parameters
pipe_dia = '${units 10. cm -> m}'
A_pipe = '${fparse 0.25 * pi * pipe_dia^2}'
A_core = '${fparse core_pitch^2 - 0.25 *pi * core_dia^2}'
P_wet_core = '${fparse 4*core_pitch + pi * core_dia}'
Dh_core = '${fparse 4 * A_core / P_wet_core}'
tot_power = 2000 # W
[GlobalParams]
initial_p = ${press}
initial_vel = 0.0001
initial_T = ${T_in}
initial_vel_x = 0
initial_vel_y = 0
initial_vel_z = 0
gravity_vector = '0 0 0'
rdg_slope_reconstruction = minmod
scaling_factor_1phase = '1 1e-2 1e-4'
scaling_factor_rhoV = 1
scaling_factor_rhouV = 1e-2
scaling_factor_rhovV = 1e-2
scaling_factor_rhowV = 1e-2
scaling_factor_rhoEV = 1e-4
closures = simple_closures
fp = he
[]
[FluidProperties]
[he]
type = IdealGasFluidProperties
molar_mass = 4e-3
gamma = 1.67
k = 0.2556
mu = 3.22639e-5
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseTHM
[]
[]
[SolidProperties]
[steel]
type = ThermalFunctionSolidProperties
rho = 8050
k = 45
cp = 466
[]
[]
[Components]
[total_power]
type = TotalPower
power = ${tot_power}
[]
[up_pipe_1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '0 0 1'
length = 0.5
n_elems = 15
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct1]
type = JunctionParallelChannels1Phase
position = '0 0 0.5'
connections = 'up_pipe_1:out core_chan:in'
volume = 1e-5
[]
[core_chan]
type = FlowChannel1Phase
position = '0 0 0.5'
orientation = '0 0 1'
length = ${core_length}
n_elems = ${core_n_elems}
roughness = .0001
A = '${A_core}'
D_h = ${Dh_core}
[]
[core_hs]
type = HeatStructureCylindrical
position = '0 0 0.5'
orientation = '0 0 1'
length = ${core_length}
n_elems = ${core_n_elems}
names = 'block'
widths = '${fparse core_dia / 2.}'
solid_properties = 'steel'
solid_properties_T_ref = '300'
n_part_elems = 3
[]
[core_heating]
type = HeatSourceFromTotalPower
hs = core_hs
regions = block
power = total_power
[]
[core_ht]
type = HeatTransferFromHeatStructure1Phase
flow_channel = core_chan
hs = core_hs
hs_side = outer
P_hf = '${fparse pi * core_dia}'
[]
[jct2]
type = JunctionParallelChannels1Phase
position = '0 0 1.5'
connections = 'core_chan:out up_pipe_2:in'
volume = 1e-5
[]
[up_pipe_2]
type = FlowChannel1Phase
position = '0 0 1.5'
orientation = '0 0 1'
length = 0.5
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct3]
type = JunctionOneToOne1Phase
connections = 'up_pipe_2:out top_pipe_1:in'
[]
[top_pipe_1]
type = FlowChannel1Phase
position = '0 0 2'
orientation = '1 0 0'
length = 0.5
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[top_pipe_2]
type = FlowChannel1Phase
position = '0.5 0 2'
orientation = '1 0 0'
length = 0.5
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct4]
type = VolumeJunction1Phase
position = '0.5 0 2'
volume = 1e-5
connections = 'top_pipe_1:out top_pipe_2:in press_pipe:in'
[]
[press_pipe]
type = FlowChannel1Phase
position = '0.5 0 2'
orientation = '0 0 1'
length = 0.2
n_elems = 5
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[pressurizer]
type = InletStagnationPressureTemperature1Phase
p0 = ${press}
T0 = ${T_in}
input = press_pipe:out
[]
[jct5]
type = JunctionOneToOne1Phase
connections = 'top_pipe_2:out down_pipe_1:in'
[]
[down_pipe_1]
type = FlowChannel1Phase
position = '1 0 2'
orientation = '0 0 -1'
length = 0.25
A = ${A_pipe}
n_elems = 5
[]
[jct6]
type = JunctionOneToOne1Phase
connections = 'down_pipe_1:out cooling_pipe:in'
[]
[cooling_pipe]
type = FlowChannel1Phase
position = '1 0 1.75'
orientation = '0 0 -1'
length = 1.5
n_elems = 25
A = ${A_pipe}
[]
[cold_wall]
type = HeatTransferFromSpecifiedTemperature1Phase
flow_channel = cooling_pipe
T_wall = 300
P_hf = '${fparse pi * pipe_dia}'
[]
[jct7]
type = JunctionOneToOne1Phase
connections = 'cooling_pipe:out down_pipe_2:in'
[]
[down_pipe_2]
type = FlowChannel1Phase
position = '1 0 0.25'
orientation = '0 0 -1'
length = 0.25
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct8]
type = JunctionOneToOne1Phase
connections = 'down_pipe_2:out bottom_1:in'
[]
[bottom_1]
type = FlowChannel1Phase
position = '1 0 0'
orientation = '-1 0 0'
length = 0.5
n_elems = 5
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[pump]
type = Pump1Phase
position = '0.5 0 0'
connections = 'bottom_1:out bottom_2:in'
volume = 1e-4
A_ref = ${A_pipe}
head = 0
[]
[bottom_2]
type = FlowChannel1Phase
position = '0.5 0 0'
orientation = '-1 0 0'
length = 0.5
n_elems = 5
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct10]
type = JunctionOneToOne1Phase
connections = 'bottom_2:out up_pipe_1:in'
[]
[]
[ControlLogic]
[set_point]
type = GetFunctionValueControl
function = ${m_dot_in}
[]
[pid]
type = PIDControl
initial_value = 0
set_point = set_point:value
input = m_dot_pump
K_p = 1.
K_i = 4.
K_d = 0
[]
[set_pump_head]
type = SetComponentRealValueControl
component = pump
parameter = head
value = pid:output
[]
[]
[Postprocessors]
[power_to_coolant]
type = ADHeatRateConvection1Phase
block = core_chan
P_hf = '${fparse pi *core_dia}'
[]
[m_dot_pump]
type = ADFlowJunctionFlux1Phase
boundary = core_chan:in
connection_index = 1
equation = mass
junction = jct7
[]
[core_T_out]
type = SideAverageValue
boundary = core_chan:out
variable = T
[]
[core_p_in]
type = SideAverageValue
boundary = core_chan:in
variable = p
[]
[core_p_out]
type = SideAverageValue
boundary = core_chan:out
variable = p
[]
[core_delta_p]
type = ParsedPostprocessor
pp_names = 'core_p_in core_p_out'
expression = 'core_p_in - core_p_out'
[]
[hx_pri_T_out]
type = SideAverageValue
boundary = cooling_pipe:out
variable = T
[]
[pump_head]
type = RealComponentParameterValuePostprocessor
component = pump
parameter = head
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
start_time = 0
[TimeStepper]
type = IterationAdaptiveDT
dt = 1
[]
dtmax = 5
end_time = 500
line_search = basic
solve_type = NEWTON
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_rel_tol = 0
nl_abs_tol = 1e-8
nl_max_its = 25
[]
[Outputs]
exodus = true
[console]
type = Console
max_rows = 1
outlier_variable_norms = false
[]
print_linear_residuals = false
[]
(modules/thermal_hydraulics/test/tests/problems/super_sonic_tube/test.i)
[GlobalParams]
gravity_vector = '0 0 0'
scaling_factor_1phase = '1 1e-2 1e-4'
initial_p = 101325
initial_T = 300
initial_vel = 522.676
closures = simple_closures
spatial_discretization = cg
[]
[FluidProperties]
[ig]
type = IdealGasFluidProperties
gamma = 1.41
molar_mass = 0.028966206103678928
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[pipe]
type = FlowChannel1Phase
fp = ig
# geometry
position = '0 0 0'
orientation = '1 0 0'
A = 1.
D_h = 1.12837916709551
f = 0.0
length = 1
n_elems = 100
[]
[inlet]
type = SupersonicInlet
input = 'pipe:in'
p = 101325
T = 300.0
vel = 522.676
[]
[outlet]
type = FreeBoundary1Phase
input = 'pipe:out'
[]
[]
[Preconditioning]
[SMP_PJFNK]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'bdf2'
start_time = 0
dt = 1e-5
num_steps = 10
abort_on_solve_fail = true
solve_type = 'PJFNK'
nl_rel_tol = 1e-9
nl_abs_tol = 1e-8
nl_max_its = 30
l_tol = 1e-3
l_max_its = 100
[Quadrature]
type = TRAP
order = FIRST
[]
[]
[Outputs]
[out]
type = Exodus
[]
[]
(modules/navier_stokes/test/tests/ics/test_function.i)
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 2
xmin = 0
xmax = 1
ymin = 1
ymax = 2
nx = 3
ny = 3
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Problem]
kernel_coverage_check = false
solve = false
skip_nl_system_check = true
[]
[AuxVariables]
[pressure]
type = MooseVariableFVReal
[]
[vel_x]
type = MooseVariableFVReal
[]
[vel_y]
type = MooseVariableFVReal
[]
[vel_z]
type = MooseVariableFVReal
[]
[temperature]
type = MooseVariableFVReal
[]
[ht]
type = MooseVariableFVReal
[]
[e]
type = MooseVariableFVReal
[]
[Mach]
type = MooseVariableFVReal
[]
[rho]
type = MooseVariableFVReal
[]
[rhou]
type = MooseVariableFVReal
[]
[rhov]
type = MooseVariableFVReal
[]
[rhow]
type = MooseVariableFVReal
[]
[rho_et]
type = MooseVariableFVReal
[]
[specific_volume]
type = MooseVariableFVReal
[]
[pressure_2]
[]
[vel_x_2]
[]
[vel_y_2]
[]
[vel_z_2]
[]
[temperature_2]
[]
[ht_2]
[]
[e_2]
[]
[Mach_2]
[]
[rho_2]
[]
[rhou_2]
[]
[rhov_2]
[]
[rhow_2]
[]
[rho_et_2]
[]
[specific_volume_2]
[]
[]
[GlobalParams]
fluid_properties = 'fp'
initial_pressure = p_func
initial_temperature = T_func
initial_velocity = 'vx vy vz'
[]
[Functions]
[p_func]
type = ParsedFunction
expression = '3+3+1e5 - x'
[]
[T_func]
type = ParsedFunction
expression = '273.15 + x*y*2'
[]
[vx]
type = ParsedFunction
expression = '14'
[]
[vy]
type = ParsedFunction
expression = '10 + x'
[]
[vz]
type = ParsedFunction
expression = '12 -7*y'
[]
[]
[ICs]
[p]
type = NSFunctionInitialCondition
variable = 'pressure'
[]
[vel_x]
type = NSFunctionInitialCondition
variable = 'vel_x'
[]
[vel_y]
type = NSFunctionInitialCondition
variable = 'vel_y'
[]
[vel_z]
type = NSFunctionInitialCondition
variable = 'vel_z'
[]
[temperature]
type = NSFunctionInitialCondition
variable = 'temperature'
[]
[ht]
type = NSFunctionInitialCondition
variable = 'ht'
[]
[e]
type = NSFunctionInitialCondition
variable = 'e'
[]
[Mach]
type = NSFunctionInitialCondition
variable = 'Mach'
[]
[rho]
type = NSFunctionInitialCondition
fluid_properties = 'fp'
initial_pressure = p_func
initial_temperature = T_func
initial_velocity = 'vx vy vz'
variable = 'rho'
[]
[rhou]
type = NSFunctionInitialCondition
variable = 'rhou'
[]
[rhov]
type = NSFunctionInitialCondition
variable = 'rhov'
[]
[rhow]
type = NSFunctionInitialCondition
variable = 'rhow'
[]
[rho_et]
type = NSFunctionInitialCondition
variable = 'rho_et'
[]
[specific_volume]
type = NSFunctionInitialCondition
variable = 'specific_volume'
[]
[p_2]
type = NSFunctionInitialCondition
variable = 'pressure_2'
variable_type = 'pressure'
[]
[vel_x_2]
type = NSFunctionInitialCondition
variable = 'vel_x_2'
variable_type = 'vel_x'
[]
[vel_y_2]
type = NSFunctionInitialCondition
variable = 'vel_y_2'
variable_type = 'vel_y'
[]
[vel_z_2]
type = NSFunctionInitialCondition
variable = 'vel_z_2'
variable_type = 'vel_z'
[]
[temperature_2]
type = NSFunctionInitialCondition
variable = 'temperature_2'
variable_type = 'temperature'
[]
[ht_2]
type = NSFunctionInitialCondition
variable = 'ht_2'
variable_type = 'ht'
[]
[e_2]
type = NSFunctionInitialCondition
variable = 'e_2'
variable_type = 'e'
[]
[Mach_2]
type = NSFunctionInitialCondition
variable = 'Mach_2'
variable_type = 'Mach'
[]
[rho_2]
type = NSFunctionInitialCondition
variable = 'rho_2'
variable_type = 'rho'
[]
[rhou_2]
type = NSFunctionInitialCondition
variable = 'rhou_2'
variable_type = 'rhou'
[]
[rhov_2]
type = NSFunctionInitialCondition
variable = 'rhov_2'
variable_type = 'rhov'
[]
[rhow_2]
type = NSFunctionInitialCondition
variable = 'rhow_2'
variable_type = 'rhow'
[]
[rho_et_2]
type = NSFunctionInitialCondition
variable = 'rho_et_2'
variable_type = 'rho_et'
[]
[specific_volume_2]
type = NSFunctionInitialCondition
variable = 'specific_volume_2'
variable_type = 'specific_volume'
[]
[]
[Executioner]
type = Steady
[]
[Debug]
show_actions = true
[]
[Outputs]
exodus = true
[]
(modules/navier_stokes/test/tests/finite_volume/cns/heated-channel/transient-porous-kt-primitive.i)
p_initial=1.01e5
T=273.15
u_in=10
eps=1
superficial_vel_in=${fparse u_in * eps}
[GlobalParams]
fp = fp
limiter = 'vanLeer'
two_term_boundary_expansion = true
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 1
xmin = 0
xmax = 10
nx = 100
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Problem]
fv_bcs_integrity_check = false
[]
[Variables]
[pressure]
type = MooseVariableFVReal
initial_condition = ${p_initial}
[]
[superficial_vel_x]
type = MooseVariableFVReal
initial_condition = ${superficial_vel_in}
[]
[temperature]
type = MooseVariableFVReal
initial_condition = ${T}
[]
[]
[AuxVariables]
[rho]
type = MooseVariableFVReal
[]
[superficial_rhou]
type = MooseVariableFVReal
[]
[]
[AuxKernels]
[rho]
type = ADMaterialRealAux
variable = rho
property = rho
execute_on = 'timestep_end'
[]
[superficial_rhou]
type = ADMaterialRealAux
variable = superficial_rhou
property = superficial_rhou
execute_on = 'timestep_end'
[]
[]
[FVKernels]
[mass_time]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rho_dt'
variable = pressure
[]
[mass_advection]
type = PCNSFVKT
variable = pressure
eqn = "mass"
[]
[momentum_time]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rhou_dt'
variable = superficial_vel_x
[]
[momentum_advection]
type = PCNSFVKT
variable = superficial_vel_x
eqn = "momentum"
momentum_component = 'x'
[]
[energy_time]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rho_et_dt'
variable = temperature
[]
[energy_advection]
type = PCNSFVKT
variable = temperature
eqn = "energy"
[]
[heat]
type = FVBodyForce
variable = temperature
value = 1e6
[]
[]
[FVBCs]
[rho_left]
type = PCNSFVStrongBC
boundary = 'left'
variable = pressure
superficial_velocity = 'superficial_vel_in'
T_fluid = ${T}
eqn = 'mass'
[]
[rhou_left]
type = PCNSFVStrongBC
boundary = 'left'
variable = superficial_vel_x
superficial_velocity = 'superficial_vel_in'
T_fluid = ${T}
eqn = 'momentum'
momentum_component = 'x'
[]
[rho_et_left]
type = PCNSFVStrongBC
boundary = 'left'
variable = temperature
superficial_velocity = 'superficial_vel_in'
T_fluid = ${T}
eqn = 'energy'
[]
[rho_right]
type = PCNSFVStrongBC
boundary = 'right'
variable = pressure
pressure = ${p_initial}
eqn = 'mass'
[]
[rhou_right]
type = PCNSFVStrongBC
boundary = 'right'
variable = superficial_vel_x
pressure = ${p_initial}
eqn = 'momentum'
momentum_component = 'x'
[]
[rho_et_right]
type = PCNSFVStrongBC
boundary = 'right'
variable = temperature
pressure = ${p_initial}
eqn = 'energy'
[]
# Use these to help create more accurate cell centered gradients for cells adjacent to boundaries
[T_left]
type = FVDirichletBC
variable = temperature
value = ${T}
boundary = 'left'
[]
[sup_vel_left]
type = FVDirichletBC
variable = superficial_vel_x
value = ${superficial_vel_in}
boundary = 'left'
[]
[p_right]
type = FVDirichletBC
variable = pressure
value = ${p_initial}
boundary = 'right'
[]
[]
[Functions]
[superficial_vel_in]
type = ParsedVectorFunction
expression_x = '${superficial_vel_in}'
[]
[]
[Materials]
[var_mat]
type = PorousPrimitiveVarMaterial
pressure = pressure
T_fluid = temperature
superficial_vel_x = superficial_vel_x
fp = fp
porosity = porosity
[]
[fluid_only]
type = GenericConstantMaterial
prop_names = 'porosity'
prop_values = '${eps}'
[]
[]
[Executioner]
solve_type = NEWTON
type = Transient
nl_max_its = 20
[TimeStepper]
type = IterationAdaptiveDT
dt = 5e-5
optimal_iterations = 10
[]
steady_state_detection = false
steady_state_tolerance = 1e-12
abort_on_solve_fail = false
end_time = 100
nl_abs_tol = 1e-8
dtmin = 5e-5
automatic_scaling = true
compute_scaling_once = false
verbose = true
petsc_options_iname = '-pc_type -pc_factor_mat_solver_type -pc_factor_shift_type -snes_linesearch_minlambda'
petsc_options_value = 'lu mumps NONZERO 1e-3 '
[]
[Outputs]
[exo]
type = Exodus
execute_on = 'final'
[]
[dof]
type = DOFMap
execute_on = 'initial'
[]
checkpoint = true
[]
[Debug]
show_var_residual_norms = true
[]
(modules/thermal_hydraulics/tutorials/single_phase_flow/03_upper_loop.i)
T_in = 300. # K
m_dot_in = 1e-2 # kg/s
press = 10e5 # Pa
# core parameters
core_length = 1. # m
core_n_elems = 25
core_dia = '${units 2. cm -> m}'
core_pitch = '${units 8.7 cm -> m}'
A_core = '${fparse core_pitch^2 - 0.25 *pi * core_dia^2}'
P_wet_core = '${fparse 4*core_pitch + pi * core_dia}'
Dh_core = '${fparse 4 * A_core / P_wet_core}'
# pipe parameters
pipe_dia = '${units 10. cm -> m}'
A_pipe = '${fparse 0.25 * pi * pipe_dia^2}'
tot_power = 2000 # W
[GlobalParams]
initial_p = ${press}
initial_vel = 0.0001
initial_T = ${T_in}
initial_vel_x = 0
initial_vel_y = 0
initial_vel_z = 0
gravity_vector = '0 0 0'
rdg_slope_reconstruction = minmod
scaling_factor_1phase = '1 1e-2 1e-4'
scaling_factor_rhoV = 1
scaling_factor_rhouV = 1e-2
scaling_factor_rhovV = 1e-2
scaling_factor_rhowV = 1e-2
scaling_factor_rhoEV = 1e-4
closures = thm_closures
fp = he
[]
[FluidProperties]
[he]
type = IdealGasFluidProperties
molar_mass = 4e-3
gamma = 1.67
k = 0.2556
mu = 3.22639e-5
[]
[]
[Closures]
[thm_closures]
type = Closures1PhaseTHM
[]
[]
[SolidProperties]
[steel]
type = ThermalFunctionSolidProperties
rho = 8050
k = 45
cp = 466
[]
[]
[Components]
[total_power]
type = TotalPower
power = ${tot_power}
[]
[inlet]
type = InletMassFlowRateTemperature1Phase
input = 'up_pipe_1:in'
m_dot = ${m_dot_in}
T = ${T_in}
[]
[up_pipe_1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '0 0 1'
length = 0.5
n_elems = 15
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct1]
type = JunctionParallelChannels1Phase
position = '0 0 0.5'
connections = 'up_pipe_1:out core_chan:in'
volume = 1e-5
[]
[core_chan]
type = FlowChannel1Phase
position = '0 0 0.5'
orientation = '0 0 1'
length = ${core_length}
n_elems = ${core_n_elems}
roughness = .0001
A = '${A_core}'
D_h = ${Dh_core}
[]
[core_hs]
type = HeatStructureCylindrical
position = '0 0 0.5'
orientation = '0 0 1'
length = ${core_length}
n_elems = ${core_n_elems}
names = 'block'
widths = '${fparse core_dia / 2.}'
solid_properties = 'steel'
solid_properties_T_ref = '300'
n_part_elems = 3
[]
[core_heating]
type = HeatSourceFromTotalPower
hs = core_hs
regions = block
power = total_power
[]
[core_ht]
type = HeatTransferFromHeatStructure1Phase
flow_channel = core_chan
hs = core_hs
hs_side = outer
P_hf = '${fparse pi * core_dia}'
[]
[jct2]
type = JunctionParallelChannels1Phase
position = '0 0 1.5'
connections = 'core_chan:out up_pipe_2:in'
volume = 1e-5
[]
[up_pipe_2]
type = FlowChannel1Phase
position = '0 0 1.5'
orientation = '0 0 1'
length = 0.5
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct3]
type = JunctionOneToOne1Phase
connections = 'up_pipe_2:out top_pipe:in'
[]
[top_pipe]
type = FlowChannel1Phase
position = '0 0 2'
orientation = '1 0 0'
length = 1
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct4]
type = JunctionOneToOne1Phase
connections = 'top_pipe:out down_pipe_1:in'
[]
[down_pipe_1]
type = FlowChannel1Phase
position = '1 0 2'
orientation = '0 0 -1'
length = 0.25
A = ${A_pipe}
n_elems = 5
[]
[jct5]
type = JunctionOneToOne1Phase
connections = 'down_pipe_1:out cooling_pipe:in'
[]
[cooling_pipe]
type = FlowChannel1Phase
position = '1 0 1.75'
orientation = '0 0 -1'
length = 1.5
n_elems = 25
A = ${A_pipe}
[]
[cold_wall]
type = HeatTransferFromSpecifiedTemperature1Phase
flow_channel = cooling_pipe
T_wall = 300
P_hf = '${fparse pi * pipe_dia}'
[]
[jct6]
type = JunctionOneToOne1Phase
connections = 'cooling_pipe:out down_pipe_2:in'
[]
[down_pipe_2]
type = FlowChannel1Phase
position = '1 0 0.25'
orientation = '0 0 -1'
length = 0.25
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[outlet]
type = Outlet1Phase
input = 'down_pipe_2:out'
p = ${press}
[]
[]
[Postprocessors]
[power_to_coolant]
type = ADHeatRateConvection1Phase
block = core_chan
P_hf = '${fparse pi *core_dia}'
[]
[core_T_out]
type = SideAverageValue
boundary = core_chan:out
variable = T
[]
[core_p_in]
type = SideAverageValue
boundary = core_chan:in
variable = p
[]
[core_p_out]
type = SideAverageValue
boundary = core_chan:out
variable = p
[]
[core_delta_p]
type = ParsedPostprocessor
pp_names = 'core_p_in core_p_out'
expression = 'core_p_in - core_p_out'
[]
[hx_pri_T_out]
type = SideAverageValue
boundary = cooling_pipe:out
variable = T
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
start_time = 0
[TimeStepper]
type = IterationAdaptiveDT
dt = 1
[]
end_time = 500
line_search = basic
solve_type = NEWTON
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_rel_tol = 1e-8
nl_abs_tol = 1e-8
nl_max_its = 25
[]
[Outputs]
exodus = true
[console]
type = Console
max_rows = 1
outlier_variable_norms = false
[]
print_linear_residuals = false
[]
(modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/varying-eps-hllc.i)
[GlobalParams]
fp = fp
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 1
xmin = .1
xmax = .6
nx = 2
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Problem]
fv_bcs_integrity_check = false
[]
[Variables]
[pressure]
type = MooseVariableFVReal
[]
[sup_mom_x]
type = MooseVariableFVReal
[]
[T_fluid]
type = MooseVariableFVReal
[]
[]
[ICs]
[pressure]
type = FunctionIC
variable = pressure
function = 'exact_p'
[]
[sup_mom_x]
type = FunctionIC
variable = sup_mom_x
function = 'exact_rho_ud'
[]
[T_fluid]
type = FunctionIC
variable = T_fluid
function = 'exact_T'
[]
[]
[FVKernels]
[mass_advection]
type = PCNSFVMassHLLC
variable = pressure
[]
[mass_fn]
type = FVBodyForce
variable = pressure
function = 'forcing_rho'
[]
[momentum_x_advection]
type = PCNSFVMomentumHLLC
variable = sup_mom_x
momentum_component = x
[]
[eps_grad]
type = PNSFVPGradEpsilon
variable = sup_mom_x
momentum_component = 'x'
epsilon_function = 'eps'
[]
[momentum_fn]
type = FVBodyForce
variable = sup_mom_x
function = 'forcing_rho_ud'
[]
[fluid_energy_advection]
type = PCNSFVFluidEnergyHLLC
variable = T_fluid
[]
[energy_fn]
type = FVBodyForce
variable = T_fluid
function = 'forcing_rho_et'
[]
[]
[FVBCs]
[mass_left]
variable = pressure
type = PCNSFVStrongBC
boundary = left
T_fluid = 'exact_T'
superficial_velocity = 'exact_superficial_velocity'
eqn = 'mass'
[]
[momentum_left]
variable = sup_mom_x
type = PCNSFVStrongBC
boundary = left
T_fluid = 'exact_T'
superficial_velocity = 'exact_superficial_velocity'
eqn = 'momentum'
momentum_component = 'x'
[]
[energy_left]
variable = T_fluid
type = PCNSFVStrongBC
boundary = left
T_fluid = 'exact_T'
superficial_velocity = 'exact_superficial_velocity'
eqn = 'energy'
[]
[mass_right]
variable = pressure
type = PCNSFVStrongBC
boundary = right
eqn = 'mass'
pressure = 'exact_p'
[]
[momentum_right]
variable = sup_mom_x
type = PCNSFVStrongBC
boundary = right
eqn = 'momentum'
momentum_component = 'x'
pressure = 'exact_p'
[]
[energy_right]
variable = T_fluid
type = PCNSFVStrongBC
boundary = right
eqn = 'energy'
pressure = 'exact_p'
[]
[]
[Materials]
[var_mat]
type = PorousMixedVarMaterial
pressure = pressure
superficial_rhou = sup_mom_x
T_fluid = T_fluid
porosity = porosity
[]
[porosity]
type = GenericFunctionMaterial
prop_names = 'porosity'
prop_values = 'eps'
[]
[]
[Functions]
[exact_rho]
type = ParsedFunction
expression = '3.48788261470924*cos(x)'
[]
[forcing_rho]
type = ParsedFunction
expression = '-3.83667087618017*sin(1.1*x)*cos(1.3*x) - 4.53424739912202*sin(1.3*x)*cos(1.1*x)'
[]
[exact_rho_ud]
type = ParsedFunction
expression = '3.48788261470924*cos(1.1*x)*cos(1.3*x)'
[]
[forcing_rho_ud]
type = ParsedFunction
expression = '(-(10.6975765229419*cos(1.5*x)/cos(x) - 0.697576522941849*cos(1.1*x)^2/cos(x)^2)*sin(x) + (10.6975765229419*sin(x)*cos(1.5*x)/cos(x)^2 - 1.3951530458837*sin(x)*cos(1.1*x)^2/cos(x)^3 + 1.53466835047207*sin(1.1*x)*cos(1.1*x)/cos(x)^2 - 16.0463647844128*sin(1.5*x)/cos(x))*cos(x))*cos(1.3*x) + 3.48788261470924*sin(x)*cos(1.1*x)^2*cos(1.3*x)/cos(x)^2 - 7.67334175236034*sin(1.1*x)*cos(1.1*x)*cos(1.3*x)/cos(x) - 4.53424739912202*sin(1.3*x)*cos(1.1*x)^2/cos(x)'
[]
[exact_rho_et]
type = ParsedFunction
expression = '26.7439413073546*cos(1.5*x)'
[]
[forcing_rho_et]
type = ParsedFunction
expression = '1.0*(3.48788261470924*(3.06706896551724*cos(1.5*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.5*x))*sin(x)*cos(1.1*x)*cos(1.3*x)/cos(x)^2 - 1.1*(3.48788261470924*(3.06706896551724*cos(1.5*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.5*x))*sin(1.1*x)*cos(1.3*x)/cos(x) - 1.3*(3.48788261470924*(3.06706896551724*cos(1.5*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.5*x))*sin(1.3*x)*cos(1.1*x)/cos(x) + 1.0*(-(10.6975765229419*cos(1.5*x)/cos(x) - 0.697576522941849*cos(1.1*x)^2/cos(x)^2)*sin(x) + (10.6975765229419*sin(x)*cos(1.5*x)/cos(x)^2 - 1.3951530458837*sin(x)*cos(1.1*x)^2/cos(x)^3 + 1.53466835047207*sin(1.1*x)*cos(1.1*x)/cos(x)^2 - 16.0463647844128*sin(1.5*x)/cos(x))*cos(x) - 40.1159119610319*sin(1.5*x))*cos(1.1*x)*cos(1.3*x)/cos(x)'
[]
[exact_T]
type = ParsedFunction
expression = '0.0106975765229418*cos(1.5*x)/cos(x) - 0.000697576522941848*cos(1.1*x)^2/cos(x)^2'
[]
[exact_eps_p]
type = ParsedFunction
expression = '3.48788261470924*(3.06706896551724*cos(1.5*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x)*cos(1.3*x)'
[]
[exact_p]
type = ParsedFunction
expression = '3.48788261470924*(3.06706896551724*cos(1.5*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x)'
[]
[exact_sup_vel_x]
type = ParsedFunction
expression = '1.0*cos(1.1*x)*cos(1.3*x)/cos(x)'
[]
[eps]
type = ParsedFunction
expression = 'cos(1.3*x)'
[]
[exact_superficial_velocity]
type = ParsedVectorFunction
expression_x = '1.0*cos(1.1*x)*cos(1.3*x)/cos(x)'
[]
[]
[Executioner]
solve_type = NEWTON
type = Steady
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_max_its = 50
line_search = bt
nl_rel_tol = 1e-12
nl_abs_tol = 1e-12
[]
[Outputs]
exodus = true
csv = true
[]
[Debug]
show_var_residual_norms = true
[]
[Postprocessors]
[h]
type = AverageElementSize
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2pressure]
type = ElementL2Error
variable = pressure
function = exact_p
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2sup_mom_x]
variable = sup_mom_x
function = exact_rho_ud
type = ElementL2Error
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2T_fluid]
variable = T_fluid
function = exact_T
type = ElementL2Error
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[]
(modules/fluid_properties/fp_interrogator/fp_interrogator.i)
# The parameters in this block are used to specify the thermodynamic state
# at which to query the fluid properties package
[FluidPropertiesInterrogator]
fp = fp
p = 1e5
T = 300
vel = 10
[]
# The fluid properties (equation of state) to query is defined here
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
(modules/fluid_properties/test/tests/fp_interrogator/2ph.T.i)
[FluidPropertiesInterrogator]
fp = fp
T = 300
[]
[FluidProperties]
[./fp_liquid]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02900055737704918
mu = 1.823e-05
k = 0.02568
[../]
[./fp_vapor]
type = IdealGasFluidProperties
gamma = 1.1
molar_mass = 0.027714866
mu = 1.7e-05
k = 0.05
[../]
[./fp]
type = TestTwoPhaseFluidProperties
fp_liquid = fp_liquid
fp_vapor = fp_vapor
[../]
[]
(modules/thermal_hydraulics/test/tests/components/junction_parallel_channels_1phase/phy.shower.i)
# This problem models a "shower": water from two pipes, one hot and one cold,
# mixes together to produce a temperature between the two.
[GlobalParams]
gravity_vector = '0 0 0'
initial_T = 300
initial_p = 1e5
initial_vel = 1
initial_vel_x = 1
initial_vel_y = 0
initial_vel_z = 0
# global parameters for pipes
fp = eos
orientation = '1 0 0'
length = 1
n_elems = 20
f = 0
scaling_factor_1phase = '1 1 1e-6'
closures = simple_closures
[]
[FluidProperties]
[eos]
type = IdealGasFluidProperties
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[inlet_hot]
type = InletDensityVelocity1Phase
input = 'pipe_hot:in'
# rho @ (p = 1e5, T = 310 K)
rho = 1315.9279785683
vel = 1
[]
[inlet_cold]
type = InletDensityVelocity1Phase
input = 'pipe_cold:in'
# rho @ (p = 1e5, T = 280 K)
rho = 1456.9202619863
vel = 1
[]
[outlet]
type = Outlet1Phase
input = 'pipe_warm:out'
p = 1e5
[]
[pipe_hot]
type = FlowChannel1Phase
position = '0 1 0'
A = 1
[]
[pipe_cold]
type = FlowChannel1Phase
position = '0 0 0'
A = 1
[]
[pipe_warm]
type = FlowChannel1Phase
position = '1 0.5 0'
A = 2
initial_vel = 0.5
[]
[junction]
type = JunctionParallelChannels1Phase
connections = 'pipe_cold:out pipe_hot:out pipe_warm:in'
position = '1 0.5 0'
volume = 1e-8
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'bdf2'
solve_type = 'NEWTON'
line_search = 'basic'
nl_rel_tol = 1e-8
nl_abs_tol = 1e-5
nl_max_its = 10
l_tol = 1e-2
l_max_its = 10
start_time = 0
end_time = 5
dt = 0.05
abort_on_solve_fail = true
[]
[Postprocessors]
# These post-processors are used to test that the energy flux on
# the warm side of the junction is equal to the sum of the energy
# fluxes of the hot and cold inlets to the junction.
[energy_flux_hot]
type = EnergyFluxIntegral
boundary = pipe_hot:out
arhouA = rhouA
H = H
[]
[energy_flux_cold]
type = EnergyFluxIntegral
boundary = pipe_cold:out
arhouA = rhouA
H = H
[]
[energy_flux_warm]
type = EnergyFluxIntegral
boundary = pipe_warm:in
arhouA = rhouA
H = H
[]
[energy_flux_inlet_sum]
type = SumPostprocessor
values = 'energy_flux_hot energy_flux_cold'
[]
[test_rel_err]
type = RelativeDifferencePostprocessor
value1 = energy_flux_warm
value2 = energy_flux_inlet_sum
[]
[]
[Outputs]
[out]
type = CSV
show = test_rel_err
sync_only = true
sync_times = '3 4 5'
[]
[]
(modules/thermal_hydraulics/test/tests/components/shaft_connected_pump_1phase/shaft_motor_pump.i)
# Pump data used in this test comes from the Semiscale Program, summarized in NUREG/CR-4945
initial_T = 393.15
area = 1e-2
dt = 1.e-2
[GlobalParams]
initial_p = 1.4E+07
initial_T = ${initial_T}
initial_vel = 10
initial_vel_x = 10
initial_vel_y = 0
initial_vel_z = 0
A = ${area}
A_ref = ${area}
f = 100
scaling_factor_1phase = '0.04 0.04 0.04e-5'
closures = simple_closures
fp = fp
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[pump]
type = ShaftConnectedPump1Phase
inlet = 'pipe:out'
outlet = 'pipe:in'
position = '0 0 0'
scaling_factor_rhoEV = 1e-5
volume = 0.3
inertia_coeff = '1 1 1 1'
inertia_const = 1.61397
omega_rated = 314
speed_cr_I = 1e12
speed_cr_fr = 0
torque_rated = 47.1825
volumetric_rated = 1
head_rated = 58.52
tau_fr_coeff = '0 0 9.084 0'
tau_fr_const = 0
head = head_fcn
torque_hydraulic = torque_fcn
density_rated = 124.2046
[]
[pipe]
type = FlowChannel1Phase
position = '0.6096 0 0'
orientation = '1 0 0'
length = 10
n_elems = 20
[]
[motor]
type = ShaftConnectedMotor
inertia = 2
torque = 47
[]
[shaft]
type = Shaft
connected_components = 'motor pump'
initial_speed = 30
[]
[]
[Functions]
[head_fcn]
type = PiecewiseLinear
data_file = semiscale_head_data.csv
format = columns
[]
[torque_fcn]
type = PiecewiseLinear
data_file = semiscale_torque_data.csv
format = columns
[]
[S_energy_fcn]
type = ParsedFunction
expression = '-tau_hyd * omega'
symbol_names = 'tau_hyd omega'
symbol_values = 'hydraulic_torque shaft:omega'
[]
[energy_conservation_fcn]
type = ParsedFunction
expression = '(E_change - S_energy * dt) / E_tot'
symbol_names = 'E_change S_energy dt E_tot'
symbol_values = 'E_change S_energy ${dt} E_tot'
[]
[]
[Postprocessors]
[hydraulic_torque]
type = ElementAverageValue
variable = hydraulic_torque
block = 'pump'
execute_on = 'initial timestep_end'
[]
# mass conservation
[mass_pipes]
type = ElementIntegralVariablePostprocessor
variable = rhoA
block = 'pipe'
execute_on = 'initial timestep_end'
[]
[mass_pump]
type = ElementAverageValue
variable = rhoV
block = 'pump'
execute_on = 'initial timestep_end'
[]
[mass_tot]
type = SumPostprocessor
values = 'mass_pipes mass_pump'
execute_on = 'initial timestep_end'
[]
[mass_conservation]
type = ChangeOverTimePostprocessor
postprocessor = mass_tot
change_with_respect_to_initial = true
compute_relative_change = true
execute_on = 'initial timestep_end'
[]
# energy conservation
[E_pipes]
type = ElementIntegralVariablePostprocessor
variable = rhoEA
block = 'pipe'
execute_on = 'initial timestep_end'
[]
[E_pump]
type = ElementAverageValue
variable = rhoEV
block = 'pump'
execute_on = 'initial timestep_end'
[]
[E_tot]
type = LinearCombinationPostprocessor
pp_coefs = '1 1'
pp_names = 'E_pipes E_pump'
execute_on = 'initial timestep_end'
[]
[S_energy]
type = FunctionValuePostprocessor
function = S_energy_fcn
indirect_dependencies = 'hydraulic_torque'
execute_on = 'initial timestep_end'
[]
[E_change]
type = ChangeOverTimePostprocessor
postprocessor = E_tot
execute_on = 'initial timestep_end'
[]
# This should also execute on initial. This value is
# lagged by one timestep as a workaround to moose issue #13262.
[energy_conservation]
type = FunctionValuePostprocessor
function = energy_conservation_fcn
execute_on = 'timestep_end'
indirect_dependencies = 'E_tot E_change S_energy'
[]
[]
[Preconditioning]
[SMP_PJFNK]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'implicit-euler'
dt = ${dt}
num_steps = 6
solve_type = 'NEWTON'
line_search = 'basic'
petsc_options_iname = '-pc_type'
petsc_options_value = ' lu'
nl_rel_tol = 1e-8
nl_abs_tol = 1e-6
nl_max_its = 15
l_tol = 1e-4
l_max_its = 10
[Quadrature]
type = GAUSS
order = SECOND
[]
[]
[Outputs]
velocity_as_vector = false
[]
(modules/thermal_hydraulics/test/tests/components/junction_one_to_one_1phase/no_junction_1phase.i)
# This input file is used to generate gold values for the junction_one_to_one_1phase.i
# test. Unlike junction_one_to_one_1phase.i, this file has no junction in the
# middle of the domain. In junction_one_to_one_1phase.i, the post-processors are
# side post-processors, but in this input file, side post-processors cannot be
# used to obtain the solution at these positions since there are no sides there.
# Therefore, the solution is sampled at points just to the left and right of
# the middle to obtain the piecewise constant solution values to either side of
# the interface.
[GlobalParams]
gravity_vector = '0 0 0'
closures = simple_closures
[]
[Functions]
[p_ic_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.5 1.0'
y = '1.0 0.1'
[]
[T_ic_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.5 1.0'
y = '1.4 1.12'
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 11.64024372
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[left_boundary]
type = FreeBoundary1Phase
input = 'channel:in'
[]
[channel]
type = FlowChannel1Phase
fp = fp
position = '0 0 0'
orientation = '1 0 0'
length = 1.0
n_elems = 100
A = 1.0
initial_T = T_ic_fn
initial_p = p_ic_fn
initial_vel = 0
f = 0
[]
[right_boundary]
type = FreeBoundary1Phase
input = 'channel:out'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
solve_type = NEWTON
nl_rel_tol = 1e-10
nl_abs_tol = 1e-8
nl_max_its = 60
l_tol = 1e-4
start_time = 0.0
dt = 1e-3
num_steps = 5
abort_on_solve_fail = true
[]
[Postprocessors]
[rhoA_left]
type = PointValue
variable = rhoA
point = '0.4999 0 0'
execute_on = 'initial timestep_end'
[]
[rhouA_left]
type = PointValue
variable = rhouA
point = '0.4999 0 0'
execute_on = 'initial timestep_end'
[]
[rhoEA_left]
type = PointValue
variable = rhoEA
point = '0.4999 0 0'
execute_on = 'initial timestep_end'
[]
[rhoA_right]
type = PointValue
variable = rhoA
point = '0.5001 0 0'
execute_on = 'initial timestep_end'
[]
[rhouA_right]
type = PointValue
variable = rhouA
point = '0.5001 0 0'
execute_on = 'initial timestep_end'
[]
[rhoEA_right]
type = PointValue
variable = rhoEA
point = '0.5001 0 0'
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
csv = true
file_base = 'junction_one_to_one_1phase_out'
execute_on = 'initial timestep_end'
[]
(modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/porous-hllc.i)
eps=0.9
[GlobalParams]
fp = fp
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 1
xmin = .1
xmax = 1.1
nx = 2
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Variables]
[rho]
type = MooseVariableFVReal
[]
[rho_ud]
type = MooseVariableFVReal
[]
[rho_et]
type = MooseVariableFVReal
[]
[]
[ICs]
[rho]
type = FunctionIC
variable = rho
function = 'exact_rho'
[]
[rho_ud]
type = FunctionIC
variable = rho_ud
function = 'exact_rho_ud'
[]
[rho_et]
type = FunctionIC
variable = rho_et
function = 'exact_rho_et'
[]
[]
[FVKernels]
[mass_advection]
type = PCNSFVMassHLLC
variable = rho
fp = fp
[]
[mass_fn]
type = FVBodyForce
variable = rho
function = 'forcing_rho'
[]
[momentum_x_advection]
type = PCNSFVMomentumHLLC
variable = rho_ud
momentum_component = x
fp = fp
[]
[momentum_fn]
type = FVBodyForce
variable = rho_ud
function = 'forcing_rho_ud'
[]
[fluid_energy_advection]
type = PCNSFVFluidEnergyHLLC
variable = rho_et
fp = fp
[]
[energy_fn]
type = FVBodyForce
variable = rho_et
function = 'forcing_rho_et'
[]
[]
[FVBCs]
[mass_in]
variable = rho
type = PCNSFVHLLCSpecifiedMassFluxAndTemperatureMassBC
boundary = left
temperature = 'exact_T'
superficial_rhou = 'exact_rho_ud'
[]
[momentum_in]
variable = rho_ud
type = PCNSFVHLLCSpecifiedMassFluxAndTemperatureMomentumBC
boundary = left
temperature = 'exact_T'
superficial_rhou = 'exact_rho_ud'
momentum_component = 'x'
[]
[energy_in]
variable = rho_et
type = PCNSFVHLLCSpecifiedMassFluxAndTemperatureFluidEnergyBC
boundary = left
temperature = 'exact_T'
superficial_rhou = 'exact_rho_ud'
[]
[mass_out]
variable = rho
type = PCNSFVHLLCSpecifiedPressureMassBC
boundary = right
pressure = 'exact_p'
[]
[momentum_out]
variable = rho_ud
type = PCNSFVHLLCSpecifiedPressureMomentumBC
boundary = right
pressure = 'exact_p'
momentum_component = 'x'
[]
[energy_out]
variable = rho_et
type = PCNSFVHLLCSpecifiedPressureFluidEnergyBC
boundary = right
pressure = 'exact_p'
[]
[]
[Materials]
[var_mat]
type = PorousConservedVarMaterial
rho = rho
superficial_rhou = rho_ud
rho_et = rho_et
porosity = porosity
[]
[porosity]
type = GenericConstantMaterial
prop_names = 'porosity'
prop_values = '${eps}'
[]
[]
[Functions]
[exact_rho]
type = ParsedFunction
expression = '3.48788261470924*cos(x)'
[]
[forcing_rho]
type = ParsedFunction
expression = '-3.83667087618017*eps*sin(1.1*x)'
symbol_names = 'eps'
symbol_values = '${eps}'
[]
[exact_rho_ud]
type = ParsedFunction
expression = '3.48788261470924*eps*cos(1.1*x)'
symbol_names = 'eps'
symbol_values = '${eps}'
[]
[forcing_rho_ud]
type = ParsedFunction
expression = 'eps*(-(10.6975765229419*cos(1.2*x)/cos(x) - 0.697576522941849*cos(1.1*x)^2/cos(x)^2)*sin(x) + (10.6975765229419*sin(x)*cos(1.2*x)/cos(x)^2 - 1.3951530458837*sin(x)*cos(1.1*x)^2/cos(x)^3 + 1.53466835047207*sin(1.1*x)*cos(1.1*x)/cos(x)^2 - 12.8370918275302*sin(1.2*x)/cos(x))*cos(x)) + 3.48788261470924*eps*sin(x)*cos(1.1*x)^2/cos(x)^2 - 7.67334175236034*eps*sin(1.1*x)*cos(1.1*x)/cos(x)'
symbol_names = 'eps'
symbol_values = '${eps}'
[]
[exact_rho_et]
type = ParsedFunction
expression = '26.7439413073546*cos(1.2*x)'
[]
[forcing_rho_et]
type = ParsedFunction
expression = '1.0*eps*(3.48788261470924*(3.06706896551724*cos(1.2*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.2*x))*sin(x)*cos(1.1*x)/cos(x)^2 - 1.1*eps*(3.48788261470924*(3.06706896551724*cos(1.2*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.2*x))*sin(1.1*x)/cos(x) + 1.0*eps*(-(10.6975765229419*cos(1.2*x)/cos(x) - 0.697576522941849*cos(1.1*x)^2/cos(x)^2)*sin(x) + (10.6975765229419*sin(x)*cos(1.2*x)/cos(x)^2 - 1.3951530458837*sin(x)*cos(1.1*x)^2/cos(x)^3 + 1.53466835047207*sin(1.1*x)*cos(1.1*x)/cos(x)^2 - 12.8370918275302*sin(1.2*x)/cos(x))*cos(x) - 32.0927295688256*sin(1.2*x))*cos(1.1*x)/cos(x)'
symbol_names = 'eps'
symbol_values = '${eps}'
[]
[exact_T]
type = ParsedFunction
expression = '0.0106975765229418*cos(1.2*x)/cos(x) - 0.000697576522941848*cos(1.1*x)^2/cos(x)^2'
symbol_names = 'eps'
symbol_values = '${eps}'
[]
[exact_p]
type = ParsedFunction
expression = '3.48788261470924*(3.06706896551724*cos(1.2*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x)'
symbol_names = 'eps'
symbol_values = '${eps}'
[]
[]
[Executioner]
solve_type = NEWTON
type = Steady
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_max_its = 50
line_search = none
nl_rel_tol = 1e-12
nl_abs_tol = 1e-12
[]
[Outputs]
exodus = true
csv = true
[]
[Debug]
show_var_residual_norms = true
[]
[Postprocessors]
[h]
type = AverageElementSize
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2rho]
type = ElementL2Error
variable = rho
function = exact_rho
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2rho_ud]
variable = rho_ud
function = exact_rho_ud
type = ElementL2Error
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2rho_et]
variable = rho_et
function = exact_rho_et
type = ElementL2Error
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[]
(modules/thermal_hydraulics/test/tests/components/inlet_stagnation_enthalpy_1phase/phy.h_rhou_3eqn.i)
[GlobalParams]
gravity_vector = '0 0 0'
initial_p = 101325
initial_T = 300
initial_vel = 0
scaling_factor_1phase = '1.e2 1. 1.e-3'
closures = simple_closures
[]
[FluidProperties]
[eos]
type = IdealGasFluidProperties
gamma = 1.41
molar_mass = 28.9662e-3
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[pipe]
type = FlowChannel1Phase
fp = eos
# geometry
position = '0 0 0'
orientation = '1 0 0'
A = 1e-4
D_h = 1.1283791671e-02
f = 0.0
length = 1
n_elems = 100
[]
[inlet]
type = InletStagnationEnthalpyMomentum1Phase
input = 'pipe:in'
H = 296748.357480000
rhou = 41.0009888754850
[]
[outlet]
type = Outlet1Phase
input = 'pipe:out'
p = 101325
[]
[]
[Preconditioning]
[SMP_PJFNK]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'bdf2'
dt = 1.e-2
abort_on_solve_fail = true
solve_type = 'PJFNK'
nl_rel_tol = 1e-14
nl_abs_tol = 5e-8
nl_max_its = 30
l_tol = 1e-3
l_max_its = 100
start_time = 0.0
end_time = 0.2
[]
(modules/fluid_properties/test/tests/fp_interrogator/2ph.p.i)
[FluidPropertiesInterrogator]
fp = fp
p = 1e5
[]
[FluidProperties]
[./fp_liquid]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02900055737704918
mu = 1.823e-05
k = 0.02568
[../]
[./fp_vapor]
type = IdealGasFluidProperties
gamma = 1.1
molar_mass = 0.027714866
mu = 1.7e-05
k = 0.05
[../]
[./fp]
type = TestTwoPhaseFluidProperties
fp_liquid = fp_liquid
fp_vapor = fp_vapor
[../]
[]
(modules/porous_flow/test/tests/newton_cooling/nc08.i)
# Newton cooling from a bar. 1-phase ideal fluid and heat, steady
[Mesh]
type = GeneratedMesh
dim = 2
nx = 100
ny = 1
xmin = 0
xmax = 100
ymin = 0
ymax = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pressure temp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureVG
m = 0.8
alpha = 1e-5
[]
[]
[Variables]
[pressure]
[]
[temp]
[]
[]
[ICs]
# have to start these reasonably close to their steady-state values
[pressure]
type = FunctionIC
variable = pressure
function = '200-0.5*x'
[]
[temperature]
type = FunctionIC
variable = temp
function = 180+0.1*x
[]
[]
[Kernels]
[flux]
type = PorousFlowAdvectiveFlux
fluid_component = 0
gravity = '0 0 0'
variable = pressure
[]
[heat_advection]
type = PorousFlowHeatAdvection
gravity = '0 0 0'
variable = temp
[]
[]
[FluidProperties]
[idealgas]
type = IdealGasFluidProperties
molar_mass = 1.4
gamma = 1.2
mu = 1.2
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = temp
[]
[ppss]
type = PorousFlow1PhaseP
porepressure = pressure
capillary_pressure = pc
[]
[massfrac]
type = PorousFlowMassFraction
[]
[dens0]
type = PorousFlowSingleComponentFluid
fp = idealgas
phase = 0
[]
[permeability]
type = PorousFlowPermeabilityConst
permeability = '1.1 0 0 0 1.1 0 0 0 1.1'
[]
[relperm]
type = PorousFlowRelativePermeabilityCorey # irrelevant in this fully-saturated situation
n = 2
phase = 0
[]
[]
[BCs]
[leftp]
type = DirichletBC
variable = pressure
boundary = left
value = 200
[]
[leftt]
type = DirichletBC
variable = temp
boundary = left
value = 180
[]
[newtonp]
type = PorousFlowPiecewiseLinearSink
variable = pressure
boundary = right
pt_vals = '-200 0 200'
multipliers = '-200 0 200'
use_mobility = true
use_relperm = true
fluid_phase = 0
flux_function = 0.005 # 1/2/L
[]
[newtont]
type = PorousFlowPiecewiseLinearSink
variable = temp
boundary = right
pt_vals = '-200 0 200'
multipliers = '-200 0 200'
use_mobility = true
use_relperm = true
use_enthalpy = true
fluid_phase = 0
flux_function = 0.005 # 1/2/L
[]
[]
[VectorPostprocessors]
[porepressure]
type = LineValueSampler
variable = pressure
start_point = '0 0.5 0'
end_point = '100 0.5 0'
sort_by = x
num_points = 11
execute_on = timestep_end
[]
[temperature]
type = LineValueSampler
variable = temp
start_point = '0 0.5 0'
end_point = '100 0.5 0'
sort_by = x
num_points = 11
execute_on = timestep_end
[]
[]
[Preconditioning]
[andy]
type = SMP
full = true
[]
[]
[Executioner]
type = Steady
solve_type = Newton
nl_rel_tol = 1E-10
nl_abs_tol = 1E-15
[]
[Outputs]
file_base = nc08
execute_on = timestep_end
[along_line]
type = CSV
execute_vector_postprocessors_on = timestep_end
[]
[]
(modules/navier_stokes/test/tests/finite_volume/cns/scalar_advection/mass-frac-advection.i)
rho_initial=1.29
p_initial=1.01e5
T=273.15
gamma=1.4
e_initial=${fparse p_initial / (gamma - 1) / rho_initial}
et_initial=${e_initial}
rho_et_initial=${fparse rho_initial * et_initial}
v_in=1
[GlobalParams]
fp = fp
# retain behavior at time of test creation
two_term_boundary_expansion = false
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 2
xmin = 0
xmax = 1
nx = 2
ymin = 0
ymax = 10
ny = 20
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Variables]
[rho]
type = MooseVariableFVReal
initial_condition = ${rho_initial}
[]
[rho_u]
type = MooseVariableFVReal
initial_condition = 1e-15
[]
[rho_v]
type = MooseVariableFVReal
initial_condition = 1e-15
[]
[rho_et]
type = MooseVariableFVReal
initial_condition = ${rho_et_initial}
scaling = 1e-5
[]
[mass_frac]
type = MooseVariableFVReal
initial_condition = 1e-15
[]
[]
[AuxVariables]
[U_x]
type = MooseVariableFVReal
[]
[U_y]
type = MooseVariableFVReal
[]
[pressure]
type = MooseVariableFVReal
[]
[temperature]
type = MooseVariableFVReal
[]
[courant]
type = MooseVariableFVReal
[]
[]
[AuxKernels]
[U_x]
type = ADMaterialRealAux
variable = U_x
property = vel_x
execute_on = 'timestep_end'
[]
[U_y]
type = ADMaterialRealAux
variable = U_y
property = vel_y
execute_on = 'timestep_end'
[]
[pressure]
type = ADMaterialRealAux
variable = pressure
property = pressure
execute_on = 'timestep_end'
[]
[temperature]
type = ADMaterialRealAux
variable = temperature
property = T_fluid
execute_on = 'timestep_end'
[]
[courant]
type = Courant
variable = courant
u = U_x
v = U_y
[]
[]
[FVKernels]
[mass_time]
type = FVPorosityTimeDerivative
variable = rho
[]
[mass_advection]
type = PCNSFVKT
variable = rho
eqn = "mass"
[]
[momentum_time_x]
type = FVTimeKernel
variable = rho_u
[]
[momentum_advection_and_pressure_x]
type = PCNSFVKT
variable = rho_u
eqn = "momentum"
momentum_component = 'x'
[]
[momentum_time_y]
type = FVTimeKernel
variable = rho_v
[]
[momentum_advection_and_pressure_y]
type = PCNSFVKT
variable = rho_v
eqn = "momentum"
momentum_component = 'y'
[]
[energy_time]
type = FVPorosityTimeDerivative
variable = rho_et
[]
[energy_advection]
type = PCNSFVKT
variable = rho_et
eqn = "energy"
[]
[mass_frac_time]
type = PCNSFVDensityTimeDerivative
variable = mass_frac
rho = rho
[]
[mass_frac_advection]
type = PCNSFVKT
variable = mass_frac
eqn = "scalar"
[]
[]
[Functions]
[ud_in]
type = ParsedVectorFunction
expression_x = '0'
expression_y = '${v_in}'
[]
[]
[FVBCs]
[rho_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = rho
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'mass'
[]
[rho_u_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = rho_u
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'momentum'
momentum_component = 'x'
[]
[rho_v_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = rho_v
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'momentum'
momentum_component = 'y'
[]
[rho_et_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = rho_et
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'energy'
[]
[mass_frac_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = mass_frac
superficial_velocity = 'ud_in'
T_fluid = ${T}
scalar = 1
eqn = 'scalar'
[]
[rho_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = rho
pressure = ${p_initial}
eqn = 'mass'
[]
[rho_u_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = rho_u
pressure = ${p_initial}
eqn = 'momentum'
momentum_component = 'x'
[]
[rho_v_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = rho_v
pressure = ${p_initial}
eqn = 'momentum'
momentum_component = 'y'
[]
[rho_et_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = rho_et
pressure = ${p_initial}
eqn = 'energy'
[]
[mass_frac_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = mass_frac
pressure = ${p_initial}
eqn = 'scalar'
[]
[momentum_x_walls]
type = PCNSFVImplicitMomentumPressureBC
variable = rho_u
boundary = 'left right'
momentum_component = 'x'
[]
[momentum_y_walls]
type = PCNSFVImplicitMomentumPressureBC
variable = rho_v
boundary = 'left right'
momentum_component = 'y'
[]
[]
[Materials]
[var_mat]
type = PorousConservedVarMaterial
rho = rho
rho_et = rho_et
superficial_rhou = rho_u
superficial_rhov = rho_v
fp = fp
porosity = porosity
[]
[porosity]
type = GenericConstantMaterial
prop_names = 'porosity'
prop_values = '1'
[]
[]
[Executioner]
type = Transient
[TimeIntegrator]
type = ActuallyExplicitEuler
[]
steady_state_detection = true
steady_state_tolerance = 1e-12
abort_on_solve_fail = true
dt = 5e-4
num_steps = 25
[]
[Outputs]
[out]
type = Exodus
execute_on = 'initial timestep_end'
[]
[dof]
type = DOFMap
execute_on = 'initial'
[]
[]
[Debug]
show_var_residual_norms = true
[]
(modules/navier_stokes/test/tests/finite_element/cns/step/step.i)
# Navier-Stokes (or Euler) flow of an ideal gas over a step.
#
# Note: this problem is not currently a regression test for the
# Navier-Stokes module since it is in some sense ill-posed. As
# discussed in [0], the sharp corner of the step (both forward and
# backward-facing) introduces a singularity in the first derivative of
# the velocity and pressure fields, and therefore produces large
# numerical errors in the neighborhood of these points. Physically,
# this numerical error can be interpreted as causing an artificial
# "boundary layer" to form just above the step, as well as a spurious
# production of entropy even though the flow remains subsonic.
# Nevertheless, the forward-facing step problem in particular remains
# a challenging and well-document test problem for flow solvers, and
# this input file is included to help facilitate its development and
# employment by users of the module.
#
# [0]: Woodward and Colella, "The numerical simulation of
# two-dimenstional fluid flow with strong shocks," Journal of
# Computational Physics 54(1), pp. 115-173, 1984
[Mesh]
type = FileMesh
file = step.e
dim = 2
# uniform_refine = 3
[]
[FluidProperties]
[ideal_gas]
type = IdealGasFluidProperties
gamma = 1.4
[]
[]
[Modules]
[CompressibleNavierStokes]
# steady-state or transient
equation_type = transient
# fluid
fluid_properties = ideal_gas
# boundary conditions
stagnation_boundary = left
stagnation_pressure = 120192.995549849 # Pa, Mach=0.5 at 1 atm
stagnation_temperature = 315 # K, Mach=0.5 at 1 atm
stagnation_flow_direction = '1 0'
no_penetration_boundary = 'top bottom step_top step_left step_right'
static_pressure_boundary = 'right'
static_pressure = 101325 # Pa
# variable types, scalings and initial conditions
family = LAGRANGE
order = FIRST
total_energy_scaling = 9.869232667160121e-6
initial_pressure = 101325.
initial_temperature = 300.
initial_velocity = '173.594354746921 0 0' # Mach 0.5: = 0.5*sqrt(gamma*R*T)
[]
[]
[Materials]
[fluid]
type = Air
block = 1
rho = rho
rhou = rhou
rhov = rhov
rhoE = rhoE
vel_x = vel_x
vel_y = vel_y
temperature = temperature
enthalpy = enthalpy
# This value is not used in the Euler equations, but it *is* used
# by the stabilization parameter computation, which it decreases
# the amount of artificial viscosity added, so it's best to use a
# realistic value.
dynamic_viscosity = 0.0
fluid_properties = ideal_gas
[]
[]
[Preconditioning]
[SMP_PJFNK]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
dt = 5.e-5
dtmin = 1.e-5
start_time = 0.0
num_steps = 10000
nl_rel_tol = 1e-5
nl_abs_tol = 1e-9
# nl_abs_step_tol = 1e-15
nl_max_its = 5
l_tol = 1e-4 # Relative linear tolerance for each Krylov solve
l_max_its = 100 # Number of linear iterations for each Krylov solve
# Specify the order as FIRST, otherwise you will get warnings in DEBUG mode...
[Quadrature]
type = TRAP
order = FIRST
[]
[]
[Outputs]
file_base = step_out
time_step_interval = 1
exodus = true
[]
(modules/thermal_hydraulics/test/tests/components/simple_turbine_1phase/phy.conservation.i)
[GlobalParams]
initial_p = 1e6
initial_T = 517
initial_vel = 4.3
initial_vel_x = 4.3
initial_vel_y = 0
initial_vel_z = 0
fp = fp
closures = simple_closures
f = 0
rdg_slope_reconstruction = minmod
gravity_vector = '0 0 0'
scaling_factor_1phase = '1 1 1e-5'
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.01
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[inlet]
type = InletMassFlowRateTemperature1Phase
input = 'pipe1:in'
m_dot = 10
T = 517
[]
[pipe1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 1
n_elems = 10
A = 1
[]
[turbine]
type = SimpleTurbine1Phase
connections = 'pipe1:out pipe2:in'
position = '1 0 0'
volume = 1
A_ref = 1.0
K = 0
on = true
power = 1000
[]
[pipe2]
type = FlowChannel1Phase
position = '1. 0 0'
orientation = '1 0 0'
length = 1
n_elems = 10
A = 1
[]
[outlet]
type = Outlet1Phase
input = 'pipe2:out'
p = 1e6
[]
[]
[Postprocessors]
[mass_in]
type = ADFlowBoundaryFlux1Phase
equation = mass
boundary = inlet
[]
[mass_out]
type = ADFlowBoundaryFlux1Phase
equation = mass
boundary = outlet
[]
[mass_diff]
type = LinearCombinationPostprocessor
pp_coefs = '1 -1'
pp_names = 'mass_in mass_out'
[]
[p_in]
type = SideAverageValue
boundary = pipe1:in
variable = p
[]
[vel_in]
type = SideAverageValue
boundary = pipe1:in
variable = vel_x
[]
[momentum_in]
type = ADFlowBoundaryFlux1Phase
equation = momentum
boundary = inlet
[]
[momentum_out]
type = ADFlowBoundaryFlux1Phase
equation = momentum
boundary = outlet
[]
[dP]
type = ParsedPostprocessor
pp_names = 'p_in W_dot'
expression = 'p_in * (1 - (1-W_dot/(10*2910.06*517))^(1.4/0.4))'
[]
[momentum_diff]
type = LinearCombinationPostprocessor
pp_coefs = '1 -1 -1'
pp_names = 'momentum_in momentum_out dP' # momentum source = -dP * A and A=1
[]
[energy_in]
type = ADFlowBoundaryFlux1Phase
equation = energy
boundary = inlet
[]
[energy_out]
type = ADFlowBoundaryFlux1Phase
equation = energy
boundary = outlet
[]
[W_dot]
type = ElementAverageValue
variable = W_dot
block = 'turbine'
[]
[energy_diff]
type = LinearCombinationPostprocessor
pp_coefs = '1 -1 -1'
pp_names = 'energy_in energy_out W_dot'
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
start_time = 0
end_time = 10
dt = 0.5
abort_on_solve_fail = true
solve_type = 'newton'
petsc_options_iname = '-pc_type'
petsc_options_value = ' lu'
nl_rel_tol = 0
nl_abs_tol = 2e-6
nl_max_its = 10
l_tol = 1e-3
# automatic_scaling = true
# compute_scaling_once = false
# off_diagonals_in_auto_scaling = true
[]
[Outputs]
[csv]
type = CSV
show = 'mass_diff energy_diff momentum_diff'
execute_on = 'final'
[]
[]
(modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/varying-eps-basic-kt-mixed.i)
[GlobalParams]
fp = fp
limiter = 'central_difference'
two_term_boundary_expansion = true
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 1
xmin = .1
xmax = .6
nx = 2
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Problem]
fv_bcs_integrity_check = false
[]
[Variables]
[pressure]
type = MooseVariableFVReal
[]
[sup_mom_x]
type = MooseVariableFVReal
[]
[T_fluid]
type = MooseVariableFVReal
[]
[]
[ICs]
[pressure]
type = FunctionIC
variable = pressure
function = 'exact_p'
[]
[sup_mom_x]
type = FunctionIC
variable = sup_mom_x
function = 'exact_rho_ud'
[]
[T_fluid]
type = FunctionIC
variable = T_fluid
function = 'exact_T'
[]
[]
[FVKernels]
[mass_advection]
type = PCNSFVKT
variable = pressure
eqn = "mass"
[]
[mass_fn]
type = FVBodyForce
variable = pressure
function = 'forcing_rho'
[]
[momentum_x_advection]
type = PCNSFVKT
variable = sup_mom_x
momentum_component = x
eqn = "momentum"
[]
[eps_grad]
type = PNSFVPGradEpsilon
variable = sup_mom_x
momentum_component = 'x'
epsilon_function = 'eps'
[]
[momentum_fn]
type = FVBodyForce
variable = sup_mom_x
function = 'forcing_rho_ud'
[]
[fluid_energy_advection]
type = PCNSFVKT
variable = T_fluid
eqn = "energy"
[]
[energy_fn]
type = FVBodyForce
variable = T_fluid
function = 'forcing_rho_et'
[]
[]
[FVBCs]
[mass_left]
variable = pressure
type = PCNSFVStrongBC
boundary = left
T_fluid = 'exact_T'
superficial_velocity = 'exact_superficial_velocity'
eqn = 'mass'
[]
[momentum_left]
variable = sup_mom_x
type = PCNSFVStrongBC
boundary = left
T_fluid = 'exact_T'
superficial_velocity = 'exact_superficial_velocity'
eqn = 'momentum'
momentum_component = 'x'
[]
[energy_left]
variable = T_fluid
type = PCNSFVStrongBC
boundary = left
T_fluid = 'exact_T'
superficial_velocity = 'exact_superficial_velocity'
eqn = 'energy'
[]
[mass_right]
variable = pressure
type = PCNSFVStrongBC
boundary = right
eqn = 'mass'
pressure = 'exact_p'
[]
[momentum_right]
variable = sup_mom_x
type = PCNSFVStrongBC
boundary = right
eqn = 'momentum'
momentum_component = 'x'
pressure = 'exact_p'
[]
[energy_right]
variable = T_fluid
type = PCNSFVStrongBC
boundary = right
eqn = 'energy'
pressure = 'exact_p'
[]
# help gradient reconstruction
[pressure_right]
type = FVFunctionDirichletBC
variable = pressure
function = exact_p
boundary = 'right'
[]
[sup_mom_x_left]
type = FVFunctionDirichletBC
variable = sup_mom_x
function = exact_rho_ud
boundary = 'left'
[]
[T_fluid_left]
type = FVFunctionDirichletBC
variable = T_fluid
function = exact_T
boundary = 'left'
[]
[]
[Materials]
[var_mat]
type = PorousMixedVarMaterial
pressure = pressure
superficial_rhou = sup_mom_x
T_fluid = T_fluid
porosity = porosity
[]
[porosity]
type = GenericFunctionMaterial
prop_names = 'porosity'
prop_values = 'eps'
[]
[]
[Functions]
[exact_rho]
type = ParsedFunction
expression = '3.48788261470924*cos(x)'
[]
[forcing_rho]
type = ParsedFunction
expression = '-3.83667087618017*sin(1.1*x)*cos(1.3*x) - 4.53424739912202*sin(1.3*x)*cos(1.1*x)'
[]
[exact_rho_ud]
type = ParsedFunction
expression = '3.48788261470924*cos(1.1*x)*cos(1.3*x)'
[]
[forcing_rho_ud]
type = ParsedFunction
expression = '(-(10.6975765229419*cos(1.5*x)/cos(x) - 0.697576522941849*cos(1.1*x)^2/cos(x)^2)*sin(x) + (10.6975765229419*sin(x)*cos(1.5*x)/cos(x)^2 - 1.3951530458837*sin(x)*cos(1.1*x)^2/cos(x)^3 + 1.53466835047207*sin(1.1*x)*cos(1.1*x)/cos(x)^2 - 16.0463647844128*sin(1.5*x)/cos(x))*cos(x))*cos(1.3*x) + 3.48788261470924*sin(x)*cos(1.1*x)^2*cos(1.3*x)/cos(x)^2 - 7.67334175236034*sin(1.1*x)*cos(1.1*x)*cos(1.3*x)/cos(x) - 4.53424739912202*sin(1.3*x)*cos(1.1*x)^2/cos(x)'
[]
[exact_rho_et]
type = ParsedFunction
expression = '26.7439413073546*cos(1.5*x)'
[]
[forcing_rho_et]
type = ParsedFunction
expression = '1.0*(3.48788261470924*(3.06706896551724*cos(1.5*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.5*x))*sin(x)*cos(1.1*x)*cos(1.3*x)/cos(x)^2 - 1.1*(3.48788261470924*(3.06706896551724*cos(1.5*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.5*x))*sin(1.1*x)*cos(1.3*x)/cos(x) - 1.3*(3.48788261470924*(3.06706896551724*cos(1.5*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.5*x))*sin(1.3*x)*cos(1.1*x)/cos(x) + 1.0*(-(10.6975765229419*cos(1.5*x)/cos(x) - 0.697576522941849*cos(1.1*x)^2/cos(x)^2)*sin(x) + (10.6975765229419*sin(x)*cos(1.5*x)/cos(x)^2 - 1.3951530458837*sin(x)*cos(1.1*x)^2/cos(x)^3 + 1.53466835047207*sin(1.1*x)*cos(1.1*x)/cos(x)^2 - 16.0463647844128*sin(1.5*x)/cos(x))*cos(x) - 40.1159119610319*sin(1.5*x))*cos(1.1*x)*cos(1.3*x)/cos(x)'
[]
[exact_T]
type = ParsedFunction
expression = '0.0106975765229418*cos(1.5*x)/cos(x) - 0.000697576522941848*cos(1.1*x)^2/cos(x)^2'
[]
[exact_eps_p]
type = ParsedFunction
expression = '3.48788261470924*(3.06706896551724*cos(1.5*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x)*cos(1.3*x)'
[]
[exact_p]
type = ParsedFunction
expression = '3.48788261470924*(3.06706896551724*cos(1.5*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x)'
[]
[exact_sup_vel_x]
type = ParsedFunction
expression = '1.0*cos(1.1*x)*cos(1.3*x)/cos(x)'
[]
[eps]
type = ParsedFunction
expression = 'cos(1.3*x)'
[]
[exact_superficial_velocity]
type = ParsedVectorFunction
expression_x = '1.0*cos(1.1*x)*cos(1.3*x)/cos(x)'
[]
[]
[Executioner]
solve_type = NEWTON
type = Transient
num_steps = 1
dtmin = 1
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_max_its = 50
line_search = bt
nl_rel_tol = 1e-12
nl_abs_tol = 1e-12
[]
[Outputs]
exodus = true
csv = true
[]
[Debug]
show_var_residual_norms = true
[]
[Postprocessors]
[h]
type = AverageElementSize
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2pressure]
type = ElementL2Error
variable = pressure
function = exact_p
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2sup_mom_x]
variable = sup_mom_x
function = exact_rho_ud
type = ElementL2Error
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2T_fluid]
variable = T_fluid
function = exact_T
type = ElementL2Error
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[]
(modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/straight-channel-hllc.i)
[GlobalParams]
fp = fp
[]
[Mesh]
[./gen_mesh]
type = CartesianMeshGenerator
dim = 1
dx = '.1 .1 .1 .1 .1 .5 .1 .1 .1 .1 .1'
# dx = '.1 .1 .1 .1 .1 .1 .1 .1 .1 .1 .1 .1 .1 .1 .1'
[../]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Variables]
[rho]
type = MooseVariableFVReal
initial_condition = 1.28969
scaling = 1e3
[]
[rho_u]
type = MooseVariableFVReal
initial_condition = 1.28969
[]
[rho_et]
type = MooseVariableFVReal
initial_condition = 2.525e5
scaling = 1e-2
[]
[]
[FVKernels]
[mass_advection]
type = CNSFVMassHLLC
variable = rho
fp = fp
[]
[momentum_x_advection]
type = CNSFVMomentumHLLC
variable = rho_u
momentum_component = x
fp = fp
[]
[drag]
type = FVReaction
variable = rho_u
rate = 1000
[]
[fluid_energy_advection]
type = CNSFVFluidEnergyHLLC
variable = rho_et
fp = fp
[]
[]
[FVBCs]
[mass_in]
variable = rho
type = CNSFVHLLCSpecifiedMassFluxAndTemperatureMassBC
boundary = left
temperature = 273.15
rhou = 1.28969
[]
[momentum_in]
variable = rho_u
type = CNSFVHLLCSpecifiedMassFluxAndTemperatureMomentumBC
boundary = left
temperature = 273.15
rhou = 1.28969
momentum_component = 'x'
[]
[energy_in]
variable = rho_et
type = CNSFVHLLCSpecifiedMassFluxAndTemperatureFluidEnergyBC
boundary = left
temperature = 273.15
rhou = 1.28969
[]
[mass_out]
variable = rho
type = CNSFVHLLCSpecifiedPressureMassBC
boundary = right
pressure = 1.01e5
[]
[momentum_out]
variable = rho_u
type = CNSFVHLLCSpecifiedPressureMomentumBC
boundary = right
pressure = 1.01e5
momentum_component = 'x'
[]
[energy_out]
variable = rho_et
type = CNSFVHLLCSpecifiedPressureFluidEnergyBC
boundary = right
pressure = 1.01e5
[]
[]
[Materials]
[var_mat]
type = ConservedVarValuesMaterial
rho = rho
rhou = rho_u
rho_et = rho_et
[]
[]
[Executioner]
solve_type = NEWTON
type = Steady
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_max_its = 50
line_search = none
[]
[Outputs]
exodus = true
csv = true
[]
[Debug]
show_var_residual_norms = true
[]
(modules/navier_stokes/test/tests/finite_volume/cns/userobject/HLLC/hllc_uo_2D_tri.i)
rho_left = 1.162633159
E_left = 2.1502913276e+05
v_left = 40
rho_right = 1.116127833
E_right = 1.7919094397e+05
v_right = 50
[Mesh]
[./cartesian]
type = GeneratedMeshGenerator
dim = 2
xmin = 0
xmax = 1
ymin = 0
ymax = 2
nx = 1
ny = 1
elem_type = 'TRI3'
[../]
[]
[FluidProperties]
[./fp]
type = IdealGasFluidProperties
allow_imperfect_jacobians = true
[../]
[]
[Problem]
kernel_coverage_check = false
[]
[Variables]
[./rho]
order = CONSTANT
family = MONOMIAL
[../]
[./rho_v]
order = CONSTANT
family = MONOMIAL
[../]
[./rho_E]
order = CONSTANT
family = MONOMIAL
[../]
[]
[ICs]
[./rho_ic]
type = FunctionIC
variable = rho
function = 'if (y / (2 * x) < 0.5, ${rho_left}, ${rho_right})'
[../]
[./rho_v_ic]
type = FunctionIC
variable = rho_v
function = 'if (y / (2 * x) < 0.5, ${fparse rho_left * v_left}, ${fparse rho_right * v_right})'
[../]
[./rho_E_ic]
type = FunctionIC
variable = rho_E
function = 'if (y / (2 * x) < 0.5, ${fparse E_left * rho_left}, ${fparse E_right * rho_right})'
[../]
[]
[Materials]
[./var_mat]
type = ConservedVarValuesMaterial
rho = rho
rhou = 0
rhov = rho_v
rho_et = rho_E
fp = fp
[../]
[]
[UserObjects]
[./hllc]
type = HLLCUserObject
fp = fp
[../]
[]
[VectorPostprocessors]
[./wave_speeds]
type = WaveSpeedVPP
hllc_uo = hllc
elem_id = 0
side_id = 2
[../]
[]
[Executioner]
type = Steady
[]
[Outputs]
csv = true
[]
(modules/fluid_properties/test/tests/fp_interrogator/vapor_mixture_rho_e.i)
[FluidPropertiesInterrogator]
fp = fp_vapor_mix
rho = 1.1870052372064208
e = 2477165.9033225174
x_ncg = '0.1'
[]
[FluidProperties]
[./fp_nitrogen]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02867055103448276
[../]
[./fp_primary]
type = IdealGasFluidProperties
gamma = 1.3
molar_mass = 0.027714866
T_c = 126.19
rho_c = 313.189812
[../]
[./fp_vapor_mix]
type = IdealRealGasMixtureFluidProperties
fp_primary = fp_primary
fp_secondary = 'fp_nitrogen'
[../]
[]
(modules/navier_stokes/test/tests/finite_element/cns/bump/bump.i)
# Euler flow of an ideal gas over a Gaussian "bump".
#
# The inlet is a stagnation pressure and temperature BC which
# corresponds to subsonic (M=0.5) flow with a static pressure of 1 atm
# and static temperature of 300K. The outlet consists of a
# weakly-imposed static pressure BC of 1 atm. The top and bottom
# walls of the channel weakly impose the "no normal flow" BC. The
# problem is initialized with freestream flow throughout the domain.
# Although this initial condition is less physically realistic, it
# helps the problem reach steady state more quickly.
#
# There is a sequence of uniformly-refined, geometry-fitted meshes
# from Yidong Xia available for solving this classical subsonic test
# problem (see the Mesh block below). A coarse grid is used for the
# actual regression test, but changing one line in the Mesh block is
# sufficient to run this problem with different meshes. An
# entropy-based error estimate is also provided, and can be used to
# demonstrate convergence of the numerical solution (since the true
# solution should produce zero entropy). The error should converge at
# second-order in this norm.
[Mesh]
# Bi-Linear elements
# file = SmoothBump_quad_ref1_Q1.msh # 84 elems, 65 nodes
# file = SmoothBump_quad_ref2_Q1.msh # 192 elems, 225 nodes
# file = SmoothBump_quad_ref3_Q1.msh # 768 elems, 833 nodes
# file = SmoothBump_quad_ref4_Q1.msh # 3072 elems, 3201 nodes
# file = SmoothBump_quad_ref5_Q1.msh # 12288 elems, 12545 nodes
# Bi-Quadratic elements
# file = SmoothBump_quad_ref0_Q2.msh # 32 elems, 65 nodes
# file = SmoothBump_quad_ref1_Q2.msh # 84 elems, 225 nodes
file = SmoothBump_quad_ref2_Q2.msh # 260 elems, 833 nodes
# file = SmoothBump_quad_ref3_Q2.msh # 900 elems, 3201 nodes
# file = SmoothBump_quad_ref4_Q2.msh # 3332 elems, 12545 nodes
# file = SmoothBump_quad_ref5_Q2.msh # 12804 elems, 49665 nodes
[]
[FluidProperties]
[ideal_gas]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02897024320557491
[]
[]
[Modules]
[CompressibleNavierStokes]
# steady-state or transient
equation_type = transient
# fluid
fluid_properties = ideal_gas
# boundary conditions
stagnation_boundary = 1
stagnation_pressure = 120192.995549849 # Pa, Mach=0.5 at 1 atm
stagnation_temperature = 315 # K, Mach=0.5 at 1 atm
stagnation_flow_direction = '1 0'
no_penetration_boundary = '3 4'
static_pressure_boundary = 2
static_pressure = 101325 # Pa
# variable types, scalings and initial conditions
family = LAGRANGE
order = FIRST
total_energy_density_scaling = 9.869232667160121e-6
initial_pressure = 101325.
initial_temperature = 300.
initial_velocity = '173.594354746921 0 0' # Mach 0.5: = 0.5*sqrt(gamma*R*T)
pressure_variable_name = "p"
[]
[]
[Materials]
[fluid]
type = Air
block = 0 # 'MeshInterior'
rho = rho
rhou = rhou
rhov = rhov
rho_et = rho_et
vel_x = vel_x
vel_y = vel_y
temperature = temperature
ht = ht
# This value is not used in the Euler equations, but it *is* used
# by the stabilization parameter computation, which it decreases
# the amount of artificial viscosity added, so it's best to use a
# realistic value.
dynamic_viscosity = 0.0
fluid_properties = ideal_gas
[]
[]
[Postprocessors]
[entropy_error]
type = NSEntropyError
execute_on = 'initial timestep_end'
block = 0
rho_infty = 1.1768292682926829
p_infty = 101325
rho = rho
pressure = p
fluid_properties = ideal_gas
[]
[]
[Preconditioning]
[SMP_PJFNK]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
dt = 5.e-5
dtmin = 1.e-5
start_time = 0.0
num_steps = 10
nl_rel_tol = 1e-9
nl_max_its = 5
l_tol = 1e-4
l_max_its = 100
# We use trapezoidal quadrature. This improves stability by
# mimicking the "group variable" discretization approach.
[Quadrature]
type = TRAP
order = FIRST
[]
[]
[Outputs]
time_step_interval = 1
exodus = true
[]
[AuxVariables]
[rhoe][]
[enthalpy][]
[]
[AuxKernels]
[rhoe]
variable = rhoe
type = ParsedAux
expression = 'rho_et'
coupled_variables = 'rho_et'
execute_on = 'initial timestep_end'
[]
[enthalpy]
variable = enthalpy
type = ParsedAux
expression = 'ht'
coupled_variables = 'ht'
execute_on = 'initial timestep_end'
[]
[]
(modules/thermal_hydraulics/test/tests/components/shaft_connected_compressor_1phase/shaft_motor_compressor.i)
area = 0.2359
dt = 1.e-3
[GlobalParams]
initial_p = 1e5
initial_T = 288
initial_vel = 60
initial_vel_x = 60
initial_vel_y = 0
initial_vel_z = 0
A = ${area}
A_ref = ${area}
f = 100
scaling_factor_1phase = '0.04 0.04 0.04e-5'
closures = simple_closures
fp = fp
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[compressor]
type = ShaftConnectedCompressor1Phase
inlet = 'pipe:out'
outlet = 'pipe:in'
position = '0 0 0'
scaling_factor_rhoEV = 1e-5
volume = ${fparse area*0.45}
inertia_coeff = '1 1 1 1'
inertia_const = 1.61397
speed_cr_I = 1e12
speed_cr_fr = 0
tau_fr_coeff = '0 0 0 0'
tau_fr_const = 0
omega_rated = 200
mdot_rated = 21.74
rho0_rated = 1.1812
c0_rated = 340
speeds = '0.0 0.4 0.5 0.6 0.7 0.8 0.9 1.0 1.1 2'
Rp_functions = 'Rp00 Rp04 Rp05 Rp06 Rp07 Rp08 Rp09 Rp10 Rp11 Rp11'
eff_functions = 'eff00 eff04 eff05 eff06 eff07 eff08 eff09 eff10 eff11 eff11'
[]
[pipe]
type = FlowChannel1Phase
position = '0.1 0 0'
orientation = '1 0 0'
length = 10
n_elems = 20
[]
[motor]
type = ShaftConnectedMotor
inertia = 1e2
torque = 100
[]
[shaft]
type = Shaft
connected_components = 'motor compressor'
initial_speed = 100
[]
[]
[Functions]
[Rp00]
type = PiecewiseLinear
x = '0 0.3736 0.4216'
y = '1 0.9701 0.9619'
[]
[eff00]
type = PiecewiseLinear
x = '0 0.3736 0.4216'
y = '0.001 0.8941 0.6641'
[]
[Rp04]
type = PiecewiseLinear
x = '0.3736 0.3745 0.3753 0.3762 0.3770 0.3919 0.4067 0.4216 0.4826'
y = '1.0789 1.0779 1.0771 1.0759 1.0749 1.0570 1.0388 1.0204 0.9450'
[]
[eff04]
type = PiecewiseLinear
x = '0.3736 0.3745 0.3753 0.3762 0.3770 0.3919 0.4067 0.4216 0.4826'
y = '0.8941 0.8929 0.8925 0.8915 0.8901 0.8601 0.7986 0.6641 0.1115'
[]
[Rp05]
type = PiecewiseLinear
x = '0.3736 0.4026 0.4106 0.4186 0.4266 0.4346 0.4426 0.4506 0.4586 0.4666 0.4746 0.4826 0.5941'
y = '1.2898 1.2442 1.2316 1.2189 1.2066 1.1930 1.1804 1.1677 1.1542 1.1413 1.1279 1.1150 0.9357'
[]
[eff05]
type = PiecewiseLinear
x = '0.3736 0.4026 0.4106 0.4186 0.4266 0.4346 0.4426 0.4506 0.4586 0.4666 0.4746 0.4826 0.5941'
y = '0.9281 0.9263 0.9258 0.9244 0.9226 0.9211 0.9195 0.9162 0.9116 0.9062 0.8995 0.8914 0.7793'
[]
[Rp06]
type = PiecewiseLinear
x = '0.4026 0.4613 0.4723 0.4834 0.4945 0.5055 0.5166 0.5277 0.5387 0.5609 0.5719 0.583 0.5941 0.7124'
y = '1.5533 1.4438 1.4232 1.4011 1.3793 1.3589 1.3354 1.3100 1.2867 1.2376 1.2131 1.1887 1.1636 0.896'
[]
[eff06]
type = PiecewiseLinear
x = '0.4026 0.4613 0.4723 0.4834 0.4945 0.5055 0.5166 0.5277 0.5387 0.5609 0.5719 0.583 0.5941 0.7124'
y = '0.9148 0.9255 0.9275 0.9277 0.9282 0.9295 0.9290 0.9269 0.9242 0.9146 0.9080 0.900 0.8920 0.8061'
[]
[Rp07]
type = PiecewiseLinear
x = '0.4613 0.5447 0.5587 0.5726 0.5866 0.6006 0.6145 0.6285 0.6425 0.6565 0.6704 0.6844 0.6984 0.7124 0.8358'
y = '1.8740 1.6857 1.6541 1.6168 1.5811 1.5430 1.5067 1.4684 1.4292 1.3891 1.3479 1.3061 1.2628 1.2208 0.8498'
[]
[eff07]
type = PiecewiseLinear
x = '0.4613 0.5447 0.5587 0.5726 0.5866 0.6006 0.6145 0.6285 0.6425 0.6565 0.6704 0.6844 0.6984 0.7124 0.8358'
y = '0.9004 0.9232 0.9270 0.9294 0.9298 0.9312 0.9310 0.9290 0.9264 0.9225 0.9191 0.9128 0.9030 0.8904 0.7789'
[]
[Rp08]
type = PiecewiseLinear
x = '0.5447 0.6638 0.6810 0.6982 0.7154 0.7326 0.7498 0.7670 0.7842 0.8014 0.8186 0.8358 0.9702'
y = '2.3005 1.9270 1.8732 1.8195 1.7600 1.7010 1.6357 1.5697 1.5019 1.4327 1.3638 1.2925 0.7347'
[]
[eff08]
type = PiecewiseLinear
x = '0.5447 0.6638 0.6810 0.6982 0.7154 0.7326 0.7498 0.7670 0.7842 0.8014 0.8186 0.8358 0.9702'
y = '0.9102 0.9276 0.9301 0.9313 0.9319 0.9318 0.9293 0.9256 0.9231 0.9153 0.9040 0.8933 0.8098'
[]
[Rp09]
type = PiecewiseLinear
x = '0.6638 0.7762 0.7938 0.8115 0.8291 0.8467 0.8644 0.8820 0.8997 0.9173 0.9349 0.9526 0.9702 1.1107 1.25120'
y = '2.6895 2.2892 2.2263 2.1611 2.0887 2.0061 1.9211 1.8302 1.7409 1.6482 1.5593 1.4612 1.3586 0.5422 -0.2742'
[]
[eff09]
type = PiecewiseLinear
x = '0.6638 0.7762 0.7938 0.8115 0.8291 0.8467 0.8644 0.8820 0.8997 0.9173 0.9349 0.9526 0.9702 1.1107 1.2512'
y = '0.8961 0.9243 0.9288 0.9323 0.9330 0.9325 0.9319 0.9284 0.9254 0.9215 0.9134 0.9051 0.8864 0.7380 0.5896'
[]
[Rp10]
type = PiecewiseLinear
x = '0.7762 0.9255 0.9284 0.9461 0.9546 0.9816 0.9968 1.0170 1.039 1.0525 1.0812 1.0880 1.1056 1.1107 1.2511'
y = '3.3162 2.6391 2.6261 2.5425 2.5000 2.3469 2.2521 2.1211 1.974 1.8806 1.6701 1.6169 1.4710 1.4257 0.1817'
[]
[eff10]
type = PiecewiseLinear
x = '0.7762 0.9255 0.9284 0.9461 0.9546 0.9816 0.9968 1.0170 1.0390 1.0525 1.0812 1.0880 1.1056 1.1107 1.2511'
y = '0.8991 0.9276 0.9281 0.9308 0.9317 0.9329 0.9318 0.9291 0.9252 0.9223 0.9116 0.9072 0.8913 0.8844 0.6937'
[]
[Rp11]
type = PiecewiseLinear
x = '0.9255 1.0749 1.134 1.2511'
y = '3.9586 2.9889 2.605 1.4928'
[]
[eff11]
type = PiecewiseLinear
x = '0.9255 1.0749 1.1340 1.2511'
y = '0.9257 0.9308 0.9328 0.8823'
[]
[S_energy_fcn]
type = ParsedFunction
expression = '-(tau_isen+tau_diss)*omega'
symbol_names = 'tau_isen tau_diss omega'
symbol_values = 'isentropic_torque dissipation_torque shaft:omega'
[]
[energy_conservation_fcn]
type = ParsedFunction
expression = '(E_change - S_energy * dt) / E_tot'
symbol_names = 'E_change S_energy dt E_tot'
symbol_values = 'E_change S_energy ${dt} E_tot'
[]
[]
[Postprocessors]
[isentropic_torque]
type = ElementAverageValue
variable = isentropic_torque
block = 'compressor'
execute_on = 'initial timestep_end'
[]
[dissipation_torque]
type = ElementAverageValue
variable = dissipation_torque
block = 'compressor'
execute_on = 'initial timestep_end'
[]
# mass conservation
[mass_pipes]
type = ElementIntegralVariablePostprocessor
variable = rhoA
block = 'pipe'
execute_on = 'initial timestep_end'
[]
[mass_compressor]
type = ElementAverageValue
variable = rhoV
block = 'compressor'
execute_on = 'initial timestep_end'
[]
[mass_tot]
type = SumPostprocessor
values = 'mass_pipes mass_compressor'
execute_on = 'initial timestep_end'
[]
[mass_conservation]
type = ChangeOverTimePostprocessor
postprocessor = mass_tot
change_with_respect_to_initial = true
compute_relative_change = true
execute_on = 'initial timestep_end'
[]
# energy conservation
[E_pipes]
type = ElementIntegralVariablePostprocessor
variable = rhoEA
block = 'pipe'
execute_on = 'initial timestep_end'
[]
[E_compressor]
type = ElementAverageValue
variable = rhoEV
block = 'compressor'
execute_on = 'initial timestep_end'
[]
[E_tot]
type = LinearCombinationPostprocessor
pp_coefs = '1 1'
pp_names = 'E_pipes E_compressor'
execute_on = 'initial timestep_end'
[]
[S_energy]
type = FunctionValuePostprocessor
function = S_energy_fcn
indirect_dependencies = 'isentropic_torque dissipation_torque'
execute_on = 'initial timestep_end'
[]
[E_change]
type = ChangeOverTimePostprocessor
postprocessor = E_tot
execute_on = 'initial timestep_end'
[]
# This should also execute on initial. This value is
# lagged by one timestep as a workaround to moose issue #13262.
[energy_conservation]
type = FunctionValuePostprocessor
function = energy_conservation_fcn
execute_on = 'timestep_end'
indirect_dependencies = 'E_tot E_change S_energy'
[]
[]
[Preconditioning]
[SMP_PJFNK]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'implicit-euler'
dt = ${dt}
num_steps = 6
solve_type = 'NEWTON'
line_search = 'basic'
petsc_options_iname = '-pc_type'
petsc_options_value = ' lu'
nl_rel_tol = 1e-8
nl_abs_tol = 1e-6
nl_max_its = 15
l_tol = 1e-4
l_max_its = 10
[Quadrature]
type = GAUSS
order = SECOND
[]
[]
[Outputs]
velocity_as_vector = false
[]
(modules/fluid_properties/test/tests/ideal_gas/test.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 2
ny = 2
elem_type = QUAD4
[]
[Functions]
[./f_fn]
type = ParsedFunction
expression = -4
[../]
[./bc_fn]
type = ParsedFunction
expression = 'x*x+y*y'
[../]
[]
[Variables]
[./u]
[../]
[]
[AuxVariables]
[./e]
initial_condition = 6232.5
[../]
[./v]
initial_condition = 0.02493
[../]
[./p]
family = MONOMIAL
order = CONSTANT
[../]
[./T]
family = MONOMIAL
order = CONSTANT
[../]
[./cp]
family = MONOMIAL
order = CONSTANT
[../]
[./cv]
family = MONOMIAL
order = CONSTANT
[../]
[./c]
family = MONOMIAL
order = CONSTANT
[../]
[./mu]
family = MONOMIAL
order = CONSTANT
[../]
[./k]
family = MONOMIAL
order = CONSTANT
[../]
[./g]
family = MONOMIAL
order = CONSTANT
[../]
[]
[AuxKernels]
[./p]
type = MaterialRealAux
variable = p
property = pressure
[../]
[./T]
type = MaterialRealAux
variable = T
property = temperature
[../]
[./cp]
type = MaterialRealAux
variable = cp
property = cp
[../]
[./cv]
type = MaterialRealAux
variable = cv
property = cv
[../]
[./c]
type = MaterialRealAux
variable = c
property = c
[../]
[./mu]
type = MaterialRealAux
variable = mu
property = mu
[../]
[./k]
type = MaterialRealAux
variable = k
property = k
[../]
[./g]
type = MaterialRealAux
variable = g
property = g
[../]
[]
[FluidProperties]
[./ideal_gas]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 1.000536678700361
[../]
[]
[Materials]
[./fp_mat]
type = FluidPropertiesMaterialVE
e = e
v = v
fp = ideal_gas
[../]
[]
[Kernels]
[./diff]
type = Diffusion
variable = u
[../]
[./ffn]
type = BodyForce
variable = u
function = f_fn
[../]
[]
[BCs]
[./all]
type = FunctionDirichletBC
variable = u
boundary = 'left right top bottom'
function = bc_fn
[../]
[]
[Executioner]
type = Steady
solve_type = NEWTON
[]
[Outputs]
exodus = true
[]
(modules/fluid_properties/test/tests/fp_interrogator/2ph.p_T.i)
[FluidPropertiesInterrogator]
fp = fp
p = 1e5
T = 300
[]
[FluidProperties]
[./fp_liquid]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02900055737704918
mu = 1.823e-05
k = 0.02568
[../]
[./fp_vapor]
type = IdealGasFluidProperties
gamma = 1.1
molar_mass = 0.027714866
mu = 1.7e-05
k = 0.05
[../]
[./fp]
type = TestTwoPhaseFluidProperties
fp_liquid = fp_liquid
fp_vapor = fp_vapor
[../]
[]
(modules/fluid_properties/test/tests/ideal_gas/test2.i)
# Test IdealGasFluidPropertiesFluidProperties using pressure and temperature
# Use values for Oxygen at 1 MPa and 350 K from NIST chemistry webook
#
# Input values:
# Cv = 669.8e J/kg/K
# Cp = 938.75 J/kg/K
# M = 31.9988e-3 kg/mol
#
# Expected output:
# density = 10.99591793 kg/m^3
# internal energy = 234.43e3 J/kg
# enthalpy = 328.5625e3 J/kg
# speed of sound = 357.0151605 m/s
[Mesh]
type = GeneratedMesh
dim = 2
nx = 1
ny = 1
[]
[Variables]
[./dummy]
[../]
[]
[AuxVariables]
[./pressure]
family = MONOMIAL
order = CONSTANT
initial_condition = 1e6
[../]
[./temperature]
family = MONOMIAL
order = CONSTANT
initial_condition = 350
[../]
[./density]
family = MONOMIAL
order = CONSTANT
[../]
[./viscosity]
family = MONOMIAL
order = CONSTANT
[../]
[./cp]
family = MONOMIAL
order = CONSTANT
[../]
[./cv]
family = MONOMIAL
order = CONSTANT
[../]
[./internal_energy]
family = MONOMIAL
order = CONSTANT
[../]
[./enthalpy]
family = MONOMIAL
order = CONSTANT
[../]
[./entropy]
family = MONOMIAL
order = CONSTANT
[../]
[./thermal_cond]
family = MONOMIAL
order = CONSTANT
[../]
[./c]
family = MONOMIAL
order = CONSTANT
[../]
[]
[AuxKernels]
[./density]
type = MaterialRealAux
variable = density
property = density
[../]
[./viscosity]
type = MaterialRealAux
variable = viscosity
property = viscosity
[../]
[./cp]
type = MaterialRealAux
variable = cp
property = cp
[../]
[./cv]
type = MaterialRealAux
variable = cv
property = cv
[../]
[./e]
type = MaterialRealAux
variable = internal_energy
property = e
[../]
[./enthalpy]
type = MaterialRealAux
variable = enthalpy
property = h
[../]
[./entropy]
type = MaterialRealAux
variable = entropy
property = s
[../]
[./thermal_cond]
type = MaterialRealAux
variable = thermal_cond
property = k
[../]
[./c]
type = MaterialRealAux
variable = c
property = c
[../]
[]
[FluidProperties]
[./idealgas]
type = IdealGasFluidProperties
gamma = 1.401537772469394
molar_mass = 0.0319988
[../]
[]
[Materials]
[./fp_mat]
type = FluidPropertiesMaterialPT
pressure = pressure
temperature = temperature
fp = idealgas
[../]
[]
[Kernels]
[./diff]
type = Diffusion
variable = dummy
[../]
[]
[Executioner]
type = Steady
solve_type = NEWTON
[]
[Outputs]
exodus = true
[]
(modules/navier_stokes/test/tests/finite_volume/materials/ergun/ergun.i)
# This file simulates flow of fluid in a porous elbow for the purpose of verifying
# correct implementation of the various different solution variable sets. This input
# tests correct implementation of the primitive superficial variable set. Flow enters on the top
# and exits on the right. Because the purpose is only to test the equivalence of
# different equation sets, no solid energy equation is included.
porosity_left = 0.4
porosity_right = 0.6
pebble_diameter = 0.06
mu = 1.81e-5 # This has been increased to avoid refining the mesh
M = 28.97e-3
R = 8.3144598
# inlet mass flowrate, kg/s
mdot = -10.0
# inlet mass flux (superficial)
mflux_in_superficial = ${fparse mdot / (pi * 0.5 * 0.5)}
# inlet mass flux (interstitial)
mflux_in_interstitial = ${fparse mflux_in_superficial / porosity_left}
p_initial = 201325.0
T_initial = 300.0
rho_initial = ${fparse p_initial / T_initial * M / R}
vel_y_initial = ${fparse mflux_in_interstitial / rho_initial}
vel_x_initial = 0.0
superficial_vel_y_initial = ${fparse mflux_in_superficial / rho_initial}
superficial_vel_x_initial = 1e-12
# Computation parameters
velocity_interp_method = 'rc'
advected_interp_method = 'upwind'
# ==============================================================================
# GEOMETRY AND MESH
# ==============================================================================
[Mesh]
[fmg]
type = FileMeshGenerator
file = 'ergun_in.e'
[]
coord_type = RZ
[]
[UserObjects]
[rc]
type = PINSFVRhieChowInterpolator
u = superficial_vel_x
v = superficial_vel_y
pressure = pressure
porosity = porosity
[]
[]
[GlobalParams]
porosity = porosity
pebble_diameter = ${pebble_diameter}
fp = fp
# rho for the kernels. Must match fluid property!
rho = ${rho_initial}
fv = true
velocity_interp_method = ${velocity_interp_method}
advected_interp_method = ${advected_interp_method}
# behavior at time of test creation
two_term_boundary_expansion = false
rhie_chow_user_object = 'rc'
[]
# ==============================================================================
# VARIABLES AND KERNELS
# ==============================================================================
[Variables]
[pressure]
type = INSFVPressureVariable
initial_condition = ${p_initial}
[]
[superficial_vel_x]
type = PINSFVSuperficialVelocityVariable
initial_condition = ${superficial_vel_x_initial}
[]
[superficial_vel_y]
type = PINSFVSuperficialVelocityVariable
initial_condition = ${superficial_vel_y_initial}
[]
[]
[FVKernels]
# Mass Equation.
[mass]
type = PINSFVMassAdvection
variable = 'pressure'
[]
# Momentum x component equation.
[vel_x_time]
type = PINSFVMomentumTimeDerivative
variable = 'superficial_vel_x'
momentum_component = 'x'
[]
[vel_x_advection]
type = PINSFVMomentumAdvection
variable = 'superficial_vel_x'
momentum_component = 'x'
[]
[vel_x_viscosity]
type = PINSFVMomentumDiffusion
variable = 'superficial_vel_x'
momentum_component = 'x'
mu = 'mu'
[]
[u_pressure]
type = PINSFVMomentumPressure
variable = 'superficial_vel_x'
pressure = pressure
momentum_component = 'x'
[]
[u_friction]
type = PINSFVMomentumFriction
variable = 'superficial_vel_x'
Darcy_name = 'Darcy_coefficient'
Forchheimer_name = 'Forchheimer_coefficient'
momentum_component = 'x'
speed = speed
mu = 'mu'
[]
# Momentum y component equation.
[vel_y_time]
type = PINSFVMomentumTimeDerivative
variable = 'superficial_vel_y'
momentum_component = 'y'
[]
[vel_y_advection]
type = PINSFVMomentumAdvection
variable = 'superficial_vel_y'
momentum_component = 'y'
[]
[vel_y_viscosity]
type = PINSFVMomentumDiffusion
variable = 'superficial_vel_y'
momentum_component = 'y'
mu = 'mu'
[]
[v_pressure]
type = PINSFVMomentumPressure
variable = 'superficial_vel_y'
pressure = pressure
momentum_component = 'y'
[]
[v_friction]
type = PINSFVMomentumFriction
variable = 'superficial_vel_y'
Darcy_name = 'Darcy_coefficient'
Forchheimer_name = 'Forchheimer_coefficient'
momentum_component = 'y'
mu = 'mu'
speed = speed
[]
[gravity]
type = PINSFVMomentumGravity
variable = 'superficial_vel_y'
gravity = '0 -9.81 0'
momentum_component = 'y'
[]
[]
# ==============================================================================
# AUXVARIABLES AND AUXKERNELS
# ==============================================================================
[AuxVariables]
[T_fluid]
initial_condition = ${T_initial}
order = CONSTANT
family = MONOMIAL
[]
[vel_x]
initial_condition = ${fparse vel_x_initial}
order = CONSTANT
family = MONOMIAL
[]
[vel_y]
initial_condition = ${fparse vel_y_initial}
order = CONSTANT
family = MONOMIAL
[]
[porosity_out]
type = MooseVariableFVReal
[]
[]
[AuxKernels]
[vel_x]
type = FunctorAux
variable = vel_x
functor = vel_x_mat
[]
[vel_y]
type = FunctorAux
variable = vel_y
functor = vel_y_mat
[]
[porosity_out]
type = FunctorAux
variable = porosity_out
functor = porosity
[]
[]
# ==============================================================================
# FLUID PROPERTIES, MATERIALS AND USER OBJECTS
# ==============================================================================
[FluidProperties]
[fp]
type = IdealGasFluidProperties
k = 0.0
mu = ${mu}
gamma = 1.4
molar_mass = ${M}
[]
[]
[FunctorMaterials]
[enthalpy]
type = INSFVEnthalpyMaterial
temperature = 'T_fluid'
[]
[speed]
type = PINSFVSpeedFunctorMaterial
superficial_vel_x = 'superficial_vel_x'
superficial_vel_y = 'superficial_vel_y'
porosity = porosity
vel_x = vel_x_mat
vel_y = vel_y_mat
[]
[kappa]
type = FunctorKappaFluid
[]
[const_Fdrags_mat]
type = FunctorErgunDragCoefficients
porosity = porosity
[]
[fluidprops]
type = GeneralFunctorFluidProps
mu_rampdown = mu_func
porosity = porosity
characteristic_length = ${pebble_diameter}
T_fluid = 'T_fluid'
pressure = 'pressure'
speed = 'speed'
[]
[]
d = 0.05
[Functions]
[mu_func]
type = PiecewiseLinear
x = '1 3 5 10 15 20'
y = '1e5 1e4 1e3 1e2 1e1 1'
[]
[real_porosity_function]
type = ParsedFunction
expression = 'if (x < 0.6 - ${d}, ${porosity_left}, if (x > 0.6 + ${d}, ${porosity_right},
(x-(0.6-${d}))/(2*${d})*(${porosity_right}-${porosity_left}) + ${porosity_left}))'
[]
[porosity]
type = ParsedFunction
expression = 'if (x < 0.6 - ${d}, ${porosity_left}, if (x > 0.6 + ${d}, ${porosity_right},
(x-(0.6-${d}))/(2*${d})*(${porosity_right}-${porosity_left}) + ${porosity_left}))'
[]
[]
# ==============================================================================
# BOUNDARY CONDITIONS
# ==============================================================================
[FVBCs]
[outlet_p]
type = INSFVOutletPressureBC
variable = 'pressure'
function = ${p_initial}
boundary = 'right'
[]
## No or Free slip BC
[free-slip-wall-x]
type = INSFVNaturalFreeSlipBC
boundary = 'bottom wall_1 wall_2 left'
variable = superficial_vel_x
momentum_component = 'x'
[]
[free-slip-wall-y]
type = INSFVNaturalFreeSlipBC
boundary = 'bottom wall_1 wall_2 left'
variable = superficial_vel_y
momentum_component = 'y'
[]
## Symmetry
[symmetry-x]
type = PINSFVSymmetryVelocityBC
boundary = 'left'
variable = superficial_vel_x
u = superficial_vel_x
v = superficial_vel_y
mu = 'mu'
momentum_component = 'x'
[]
[symmetry-y]
type = PINSFVSymmetryVelocityBC
boundary = 'left'
variable = superficial_vel_y
u = superficial_vel_x
v = superficial_vel_y
mu = 'mu'
momentum_component = 'y'
[]
[symmetry-p]
type = INSFVSymmetryPressureBC
boundary = 'left'
variable = 'pressure'
[]
## inlet
[inlet_vel_x]
type = INSFVInletVelocityBC
variable = 'superficial_vel_x'
functor = ${superficial_vel_x_initial}
boundary = 'top'
[]
[inlet_vel_y]
type = INSFVInletVelocityBC
variable = 'superficial_vel_y'
functor = ${superficial_vel_y_initial}
boundary = 'top'
[]
[]
# ==============================================================================
# EXECUTION PARAMETERS
# ==============================================================================
[Executioner]
type = Transient
solve_type = 'NEWTON'
petsc_options_iname = '-pc_type -sub_pc_type -sub_pc_factor_shift_type -ksp_gmres_restart'
petsc_options_value = 'asm lu NONZERO 200'
line_search = 'none'
# Problem time parameters
dtmin = 0.01
dtmax = 2000
end_time = 3000
# must be the same as the fluid
# Iterations parameters
l_max_its = 50
l_tol = 1e-8
nl_max_its = 25
# nl_rel_tol = 5e-7
nl_abs_tol = 2e-7
# Automatic scaling
automatic_scaling = true
verbose = true
[TimeStepper]
type = IterationAdaptiveDT
dt = 0.025
cutback_factor = 0.5
growth_factor = 2.0
[]
# Steady state detection.
steady_state_detection = true
steady_state_tolerance = 1e-7
steady_state_start_time = 400
[]
# ==============================================================================
# POSTPROCESSORS DEBUG AND OUTPUTS
# ==============================================================================
[Postprocessors]
[mass_flow_in]
type = VolumetricFlowRate
boundary = 'top'
vel_x = 'superficial_vel_x'
vel_y = 'superficial_vel_y'
advected_quantity = ${rho_initial}
execute_on = 'INITIAL TIMESTEP_END'
[]
[mass_flow_out]
type = VolumetricFlowRate
boundary = 'right'
vel_x = 'superficial_vel_x'
vel_y = 'superficial_vel_y'
advected_quantity = ${rho_initial}
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_in]
type = SideAverageValue
variable = pressure
boundary = 'top'
[]
[dP]
type = LinearCombinationPostprocessor
pp_names = 'p_in'
pp_coefs = '1.0'
b = ${fparse -p_initial}
[]
[]
[Outputs]
exodus = true
print_linear_residuals = false
[]
(modules/porous_flow/test/tests/jacobian/esbc01.i)
# Tests the Jacobian of PorousFlowEnthalpySink when pore pressure is specified
[Mesh]
type = GeneratedMesh
dim = 2
[]
[GlobalParams]
PorousFlowDictator = dictator
at_nodes = true
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp temp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0.1
[]
[]
[Variables]
[pp]
initial_condition = 1
[]
[temp]
initial_condition = 2
[]
[]
[Kernels]
[mass0]
type = TimeDerivative
variable = pp
[]
[heat_conduction]
type = TimeDerivative
variable = temp
[]
[]
[FluidProperties]
[simple_fluid]
type = IdealGasFluidProperties
[]
[]
[Materials]
[ppss]
type = PorousFlow1PhaseFullySaturated
porepressure = pp
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[temperature]
type = PorousFlowTemperature
temperature = temp
[]
[]
[BCs]
[left]
type = PorousFlowEnthalpySink
variable = temp
boundary = left
fluid_phase = 0
T_in = 300
fp = simple_fluid
flux_function = -23
[]
[]
[Preconditioning]
[andy]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 0.1
num_steps = 1
nl_rel_tol = 1E-12
nl_abs_tol = 1E-12
petsc_options_iname = '-snes_test_err'
petsc_options_value = '1e-2'
[]
(modules/navier_stokes/test/tests/finite_volume/cns/implicit_bcs/hllc_sod_shocktube.i)
rho_left = 1
E_left = 2.501505578
u_left = 1e-15
rho_right = 0.125
E_right = 1.999770935
u_right = 1e-15
middle = 0.5
[GlobalParams]
fp = fp
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 2
xmin = 0
xmax = ${fparse 2 * middle}
nx = 5
ymin = 0
ymax = 1
ny = 2
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
allow_imperfect_jacobians = true
[]
[]
[Variables]
[rho]
order = CONSTANT
family = MONOMIAL
fv = true
[]
[rho_u]
order = CONSTANT
family = MONOMIAL
fv = true
[]
[rho_v]
order = CONSTANT
family = MONOMIAL
fv = true
initial_condition = 1e-10
[]
[rho_E]
order = CONSTANT
family = MONOMIAL
fv = true
[]
[]
[FVKernels]
[mass_time]
type = FVTimeKernel
variable = rho
[]
[mass_advection]
type = CNSFVMassHLLC
variable = rho
[]
[momentum_x_time]
type = FVTimeKernel
variable = rho_u
[]
[momentum_x_advection]
type = CNSFVMomentumHLLC
variable = rho_u
momentum_component = x
[]
[momentum_y_time]
type = FVTimeKernel
variable = rho_v
[]
[momentum_y_advection]
type = CNSFVMomentumHLLC
variable = rho_v
momentum_component = y
[]
[fluid_energy_time]
type = FVTimeKernel
variable = rho_E
[]
[fluid_energy_advection]
type = CNSFVFluidEnergyHLLC
variable = rho_E
[]
[]
[FVBCs]
[mass_implicit]
type = CNSFVHLLCMassImplicitBC
variable = rho
fp = fp
boundary = 'left right'
[]
[mom_x_implicit]
type = CNSFVHLLCMomentumImplicitBC
variable = rho_u
momentum_component = x
fp = fp
boundary = 'left right'
[]
[wall]
type = CNSFVMomImplicitPressureBC
variable = rho_v
momentum_component = y
boundary = 'top bottom'
[]
[fluid_energy_implicit]
type = CNSFVHLLCFluidEnergyImplicitBC
variable = rho_E
fp = fp
boundary = 'left right'
[]
[]
[ICs]
[rho_ic]
type = FunctionIC
variable = rho
function = 'if (x < ${middle}, ${rho_left}, ${rho_right})'
[]
[rho_u_ic]
type = FunctionIC
variable = rho_u
function = 'if (x < ${middle}, ${fparse rho_left * u_left}, ${fparse rho_right * u_right})'
[]
[rho_E_ic]
type = FunctionIC
variable = rho_E
function = 'if (x < ${middle}, ${fparse E_left * rho_left}, ${fparse E_right * rho_right})'
[]
[]
[Materials]
[var_mat]
type = ConservedVarValuesMaterial
rho = rho
rhou = rho_u
rhov = rho_v
rho_et = rho_E
fp = fp
[]
[]
[Executioner]
type = Transient
[TimeIntegrator]
type = ExplicitSSPRungeKutta
order = 2
[]
l_tol = 1e-8
# run to t = 0.15
start_time = 0.0
dt = 1e-1
end_time = 10
abort_on_solve_fail = true
[]
[Outputs]
exodus = true
[]
(modules/thermal_hydraulics/test/tests/components/flow_channel_1phase/steady.i)
# Tests that a flow channel can run with Steady executioner.
#
# Note that this solve may fail to converge based on initial guess. For example,
# having a guess with velocity set to zero will fail to converge.
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[inlet]
type = InletMassFlowRateTemperature1Phase
input = 'pipe:in'
m_dot = 2
T = 500
[]
[pipe]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
gravity_vector = '0 0 0'
length = 1.0
n_elems = 50
A = 1.0
initial_T = 300
initial_p = 1e5
initial_vel = 1
f = 10.0
closures = simple_closures
fp = fp
scaling_factor_1phase = '1 1 1e-5'
[]
[outlet]
type = Outlet1Phase
input = 'pipe:out'
p = 2e5
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Steady
solve_type = NEWTON
nl_rel_tol = 1e-7
nl_abs_tol = 1e-7
nl_max_its = 15
l_tol = 1e-3
l_max_its = 10
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
[Quadrature]
type = GAUSS
order = SECOND
[]
[]
[Outputs]
exodus = true
[]
(modules/thermal_hydraulics/tutorials/single_phase_flow/01_flow_channel.i)
T_in = 300. # K
m_dot_in = 1e-2 # kg/s
press = 10e5 # Pa
[GlobalParams]
initial_p = ${press}
initial_vel = 0.0001
initial_T = ${T_in}
gravity_vector = '0 0 0'
rdg_slope_reconstruction = minmod
scaling_factor_1phase = '1 1e-2 1e-4'
closures = thm_closures
fp = he
[]
[FluidProperties]
[he]
type = IdealGasFluidProperties
molar_mass = 4e-3
gamma = 1.67
k = 0.2556
mu = 3.22639e-5
[]
[]
[Closures]
[thm_closures]
type = Closures1PhaseTHM
[]
[]
[Components]
[inlet]
type = InletMassFlowRateTemperature1Phase
input = 'core_chan:in'
m_dot = ${m_dot_in}
T = ${T_in}
[]
[core_chan]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '0 0 1'
length = 1
n_elems = 25
A = 7.2548e-3
D_h = 7.0636e-2
[]
[outlet]
type = Outlet1Phase
input = 'core_chan:out'
p = ${press}
[]
[]
[Postprocessors]
[core_p_in]
type = SideAverageValue
boundary = core_chan:in
variable = p
[]
[core_p_out]
type = SideAverageValue
boundary = core_chan:out
variable = p
[]
[core_delta_p]
type = ParsedPostprocessor
pp_names = 'core_p_in core_p_out'
expression = 'core_p_in - core_p_out'
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = NEWTON
line_search = basic
start_time = 0
end_time = 1000
dt = 10
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_rel_tol = 1e-8
nl_abs_tol = 1e-8
nl_max_its = 25
[]
[Outputs]
exodus = true
[console]
type = Console
max_rows = 1
outlier_variable_norms = false
[]
print_linear_residuals = false
[]
(modules/thermal_hydraulics/test/tests/components/simple_turbine_1phase/phy.test.i)
[GlobalParams]
initial_p = 1e6
initial_T = 517
initial_vel = 1.0
initial_vel_x = 1
initial_vel_y = 0
initial_vel_z = 0
fp = fp
closures = simple_closures
f = 0
gravity_vector = '0 0 0'
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.01
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[inlet]
type = InletMassFlowRateTemperature1Phase
input = 'pipe1:in'
m_dot = 10
T = 517
[]
[pipe1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 1
n_elems = 10
A = 1
[]
[turbine]
type = SimpleTurbine1Phase
connections = 'pipe1:out pipe2:in'
position = '1 0 0'
volume = 1
on = true
power = 1000
[]
[pipe2]
type = FlowChannel1Phase
position = '1. 0 0'
orientation = '1 0 0'
length = 1
n_elems = 10
A = 1
[]
[outlet]
type = Outlet1Phase
input = 'pipe2:out'
p = 1e6
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
start_time = 0
dt = 1
num_steps = 10
abort_on_solve_fail = true
solve_type = 'newton'
line_search = 'basic'
petsc_options_iname = '-pc_type'
petsc_options_value = ' lu'
nl_rel_tol = 1e-6
nl_abs_tol = 1e-5
nl_max_its = 5
l_tol = 1e-4
[]
[Outputs]
exodus = true
show = 'p T vel'
velocity_as_vector = false
time_step_interval = 5
[]
(modules/thermal_hydraulics/test/tests/problems/natural_circulation/base.i)
# Natural circulation loop
#
# The setup consists of 4 connected 1-m pipes, forming a square:
#
# top_pipe
# *--------------* (1,1)
# | |
# | <- <- | | g
# heated_pipe | <- <- | cooled_pipe V
# | <- <- |
# | |
# (0,0) *--------------*
# bottom_pipe
#
# Heating and cooling occurs in the range z = (0.2 m, 0.8 m) with uniform heat fluxes.
[GlobalParams]
gravity_vector = '0 0 -9.81'
length = ${length}
n_elems = ${n_elems}
A = ${area}
initial_T = ${T_ambient}
initial_p = ${p_initial}
initial_vel = 0
fp = fp
closures = closures
f = 0
Hw = ${htc}
rdg_slope_reconstruction = full
scaling_factor_1phase = '1 1 1e-5'
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
emit_on_nan = none
[]
[]
[Closures]
[closures]
type = Closures1PhaseSimple
[]
[]
[Functions]
[heating_flux_fn]
type = PiecewiseConstant
axis = z
x = '0 0.2 0.8'
y = '0 ${fparse power / (S_heated)} 0'
[]
[cooling_flux_fn]
type = PiecewiseConstant
axis = z
x = '0 0.2 0.8'
y = '0 ${fparse -power / (S_cooled)} 0'
[]
[]
[Components]
[heated_pipe]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '0 0 1'
[]
[top_pipe]
type = FlowChannel1Phase
position = '0 0 1'
orientation = '1 0 0'
[]
[cooled_pipe]
type = FlowChannel1Phase
position = '1 0 1'
orientation = '0 0 -1'
[]
[bottom_pipe]
type = FlowChannel1Phase
position = '1 0 0'
orientation = '-1 0 0'
[]
[heating]
type = HeatTransferFromHeatFlux1Phase
flow_channel = 'heated_pipe'
q_wall = heating_flux_fn
[]
[cooling]
type = HeatTransferFromHeatFlux1Phase
flow_channel = 'cooled_pipe'
q_wall = cooling_flux_fn
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
start_time = 0
end_time = 50
[TimeStepper]
type = IterationAdaptiveDT
dt = 0.01
optimal_iterations = 6
iteration_window = 0
growth_factor = 1.2
cutback_factor = 0.8
[]
steady_state_detection = true
petsc_options_iname = '-pc_type'
petsc_options_value = ' lu '
nl_rel_tol = 1e-10
nl_abs_tol = 1e-10
nl_max_its = 15
l_tol = 1e-4
l_max_its = 10
[]
[VectorPostprocessors]
[heated_pipe_vpp]
type = ElementValueSampler
block = 'heated_pipe'
variable = ${output_variables}
sort_by = z
execute_on = 'FINAL'
[]
[top_pipe_vpp]
type = ElementValueSampler
block = 'top_pipe'
variable = ${output_variables}
sort_by = x
execute_on = 'FINAL'
[]
[cooled_pipe_vpp]
type = ElementValueSampler
block = 'cooled_pipe'
variable = ${output_variables}
sort_by = z
execute_on = 'FINAL'
[]
[bottom_pipe_vpp]
type = ElementValueSampler
block = 'bottom_pipe'
variable = ${output_variables}
sort_by = x
execute_on = 'FINAL'
[]
[]
[Outputs]
xml = true
velocity_as_vector = false
execute_on = 'FINAL'
[]
(modules/thermal_hydraulics/test/tests/components/shaft_connected_pump_1phase/pump_coastdown.i)
# Pump data used in this test comes from the Semiscale Program, summarized in NUREG/CR-4945
initial_T = 393.15
area = 1e-2
dt = 0.005
[GlobalParams]
initial_p = 1.4E+07
initial_T = ${initial_T}
initial_vel = 0.01
initial_vel_x = 0.01
initial_vel_y = 0
initial_vel_z = 0
A = ${area}
A_ref = ${area}
f = 100
scaling_factor_1phase = '1 1 1e-3'
closures = simple_closures
rdg_slope_reconstruction = minmod
fp = fp
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[pump]
type = ShaftConnectedPump1Phase
inlet = 'pipe:out'
outlet = 'pipe:in'
position = '0 0 0'
scaling_factor_rhoEV = 1e-5
volume = 0.3
inertia_coeff = '1 1 1 1'
inertia_const = 0.5
omega_rated = 314
speed_cr_I = 1e12
speed_cr_fr = 0.001
torque_rated = 47.1825
volumetric_rated = 1
head_rated = 58.52
tau_fr_coeff = '4 0 80 0'
tau_fr_const = 8
head = head_fcn
torque_hydraulic = torque_fcn
density_rated = 124.2046
[]
[pipe]
type = FlowChannel1Phase
position = '0.6096 0 0'
orientation = '1 0 0'
length = 10
n_elems = 20
[]
[shaft]
type = Shaft
connected_components = 'pump'
initial_speed = 1
[]
[]
[Functions]
[head_fcn]
type = PiecewiseLinear
data_file = semiscale_head_data.csv
format = columns
[]
[torque_fcn]
type = PiecewiseLinear
data_file = semiscale_torque_data.csv
format = columns
[]
[]
[Postprocessors]
[vel_avg]
type = ElementAverageValue
variable = vel
block = 'pipe'
execute_on = 'INITIAL TIMESTEP_END'
[]
[hydraulic_torque]
type = ElementAverageValue
variable = hydraulic_torque
block = 'pump'
execute_on = 'initial timestep_end'
[]
[]
[Preconditioning]
[SMP]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'bdf2'
dt = ${dt}
num_steps = 40
solve_type = 'NEWTON'
line_search = 'basic'
nl_rel_tol = 1e-8
nl_abs_tol = 1e-8
nl_max_its = 15
l_tol = 1e-4
l_max_its = 10
[Quadrature]
type = GAUSS
order = SECOND
[]
[]
[Outputs]
velocity_as_vector = false
file_base = 'pump_coastdown'
[csv]
type = CSV
show = 'shaft:omega vel_avg'
[]
[]
(modules/navier_stokes/test/tests/finite_volume/cns/symmetry_test/2D_symmetry.i)
rho_inside = 1
E_inside = 2.501505578
rho_outside = 0.125
E_outside = 1.999770935
radius = 0.1
angle = 45
[GlobalParams]
fp = fp
[]
[Debug]
show_material_props = true
[]
[Mesh]
[file]
type = GeneratedMeshGenerator
dim = 2
xmin = -0.5
xmax = 0.5
nx = 10
ymin = -0.5
ymax = 0.5
ny = 10
[../]
[rotate]
type = TransformGenerator
vector_value = '${angle} 0 0'
transform = ROTATE
input = file
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
allow_imperfect_jacobians = true
[]
[]
[Variables]
[rho]
family = MONOMIAL
order = CONSTANT
fv = true
[../]
[rho_u]
family = MONOMIAL
order = CONSTANT
fv = true
initial_condition = 1e-15
outputs = none
[]
[rho_v]
family = MONOMIAL
order = CONSTANT
fv = true
initial_condition = 1e-15
outputs = none
[]
[rho_E]
family = MONOMIAL
order = CONSTANT
fv = true
[]
[]
[ICs]
[rho_ic]
type = FunctionIC
variable = rho
function = 'if (abs(x) < ${radius} & abs(y) < ${radius}, ${rho_inside}, ${rho_outside})'
[]
[rho_E_ic]
type = FunctionIC
variable = rho_E
function = 'if (abs(x) < ${radius} & abs(y) < ${radius}, ${fparse E_inside * rho_inside}, ${fparse E_outside * rho_outside})'
[]
[]
[FVKernels]
# Mass conservation
[mass_time]
type = FVTimeKernel
variable = rho
[]
[mass_advection]
type = CNSFVMassHLLC
variable = rho
fp = fp
[]
# Momentum x conservation
[momentum_x_time]
type = FVTimeKernel
variable = rho_u
[]
[momentum_x_advection]
type = CNSFVMomentumHLLC
variable = rho_u
momentum_component = x
fp = fp
[]
# Momentum y conservation
[momentum_y_time]
type = FVTimeKernel
variable = rho_v
[]
[./momentum_y_advection]
type = CNSFVMomentumHLLC
variable = rho_v
momentum_component = y
[]
# Fluid energy conservation
[./fluid_energy_time]
type = FVTimeKernel
variable = rho_E
[]
[./fluid_energy_advection]
type = CNSFVFluidEnergyHLLC
variable = rho_E
fp = fp
[]
[]
[FVBCs]
## outflow implicit conditions
[mass_outflow]
type = CNSFVHLLCMassImplicitBC
variable = rho
fp = fp
boundary = 'left right top bottom'
[]
[./momentum_x_outflow]
type = CNSFVHLLCMomentumImplicitBC
variable = rho_u
momentum_component = x
fp = fp
boundary = 'left right top bottom'
[]
[momentum_y_outflow]
type = CNSFVHLLCMomentumImplicitBC
variable = rho_v
momentum_component = y
fp = fp
boundary = 'left right top bottom'
[]
[fluid_energy_outflow]
type = CNSFVHLLCFluidEnergyImplicitBC
variable = rho_E
fp = fp
boundary = 'left right top bottom'
[]
[]
[AuxVariables]
[Ma]
family = MONOMIAL
order = CONSTANT
[]
[p]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[Ma_aux]
type = NSMachAux
variable = Ma
fluid_properties = fp
use_material_properties = true
[]
[p_aux]
type = ADMaterialRealAux
variable = p
property = pressure
[]
[]
[Materials]
[var_mat]
type = ConservedVarValuesMaterial
rho = rho
rhou = rho_u
rhov = rho_v
rho_et = rho_E
[]
[sound_speed]
type = SoundspeedMat
fp = fp
[]
[]
[Postprocessors]
[cfl_dt]
type = ADCFLTimeStepSize
c_names = 'sound_speed'
vel_names = 'speed'
CFL = 0.5
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
[]
[]
[Executioner]
type = Transient
end_time = 0.2
[TimeIntegrator]
type = ExplicitSSPRungeKutta
order = 2
[]
l_tol = 1e-8
[TimeStepper]
type = PostprocessorDT
postprocessor = cfl_dt
[]
[]
(modules/thermal_hydraulics/test/tests/materials/binary_diffusion_coef/binary_diffusion_coef.i)
p = 1e5
T = 300
collision_diam = 0.3e-9
[Mesh]
type = GeneratedMesh
dim = 1
nx = 1
[]
[FluidProperties]
[fp1]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.029
[]
[fp2]
type = IdealGasFluidProperties
gamma = 1.5
molar_mass = 0.04
[]
[mixture_fp]
type = IdealGasMixtureFluidProperties
component_fluid_properties = 'fp1 fp2'
[]
[]
[Materials]
[pT_mat]
type = ADGenericConstantMaterial
prop_names = 'p T'
prop_values = '${p} ${T}'
[]
[test_mat]
type = BinaryDiffusionCoefMaterial
primary_collision_diameter = ${collision_diam}
secondary_collision_diameter = ${collision_diam}
vapor_mixture_fp = mixture_fp
[]
[]
[Postprocessors]
[diffcoef]
type = ADElementAverageMaterialProperty
mat_prop = mass_diffusion_coefficient
execute_on = 'INITIAL'
[]
[]
[Problem]
solve = false
[]
[Executioner]
type = Steady
[]
[Outputs]
csv = true
execute_on = 'INITIAL'
[]
(modules/navier_stokes/test/tests/finite_volume/two_phase/mixture_interface_area_model/turbulent_driven_growth.i)
###############################################################################
# Validation test based on Hibiki and Ishii experiment [1] reported in Figure 5
# [1] Hibiki, T., & Ishii, M. (2000). One-group interfacial area transport of
# bubbly flows in vertical round tubes.
# International Journal of Heat and Mass Transfer, 43(15), 2711-2726.
###############################################################################
mu = 1.0
rho = 1000.0
mu_d = 1.0
rho_d = 1.0
l = ${fparse 50.8/1000.0}
U = 5.031429
dp = 0.005
inlet_phase_2 = 0.442
advected_interp_method = 'upwind'
velocity_interp_method = 'rc'
mass_exchange_coeff = 0.0
inlet_interface_area = ${fparse 6.0*inlet_phase_2/dp}
outlet_pressure = 1e5
[GlobalParams]
rhie_chow_user_object = 'rc'
density_interp_method = 'average'
mu_interp_method = 'average'
[]
[Problem]
identify_variable_groups_in_nl = false
previous_nl_solution_required = true
[]
[UserObjects]
[rc]
type = INSFVRhieChowInterpolator
u = vel_x
v = vel_y
pressure = pressure
[]
[]
[Mesh]
coord_type = 'RZ'
rz_coord_axis = 'X'
[gen]
type = GeneratedMeshGenerator
dim = 2
xmin = 0
xmax = '${fparse l * 60}'
ymin = 0
ymax = '${fparse l / 2}'
nx = 20
ny = 5
[]
uniform_refine = 0
[]
[Variables]
[vel_x]
type = INSFVVelocityVariable
initial_condition = 0
[]
[vel_y]
type = INSFVVelocityVariable
initial_condition = 0
[]
[pressure]
type = INSFVPressureVariable
[]
[phase_2]
type = INSFVScalarFieldVariable
initial_condition = ${inlet_phase_2}
[]
[interface_area]
type = INSFVScalarFieldVariable
initial_condition = ${inlet_interface_area}
[]
[]
[FVKernels]
[mass]
type = INSFVMassAdvection
variable = pressure
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = ${rho}
[]
[u_advection]
type = INSFVMomentumAdvection
variable = vel_x
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = 'rho_mixture'
momentum_component = 'x'
[]
[u_drift]
type = WCNSFV2PMomentumDriftFlux
variable = vel_x
rho_d = ${rho_d}
fd = 'rho_mixture_var'
u_slip = 'vel_slip_x'
v_slip = 'vel_slip_y'
momentum_component = 'x'
[]
[u_viscosity]
type = INSFVMomentumDiffusion
variable = vel_x
mu = 'mu_mixture'
limit_interpolation = true
momentum_component = 'x'
[]
[u_pressure]
type = INSFVMomentumPressure
variable = vel_x
momentum_component = 'x'
pressure = pressure
[]
[v_advection]
type = INSFVMomentumAdvection
variable = vel_y
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = 'rho_mixture'
momentum_component = 'y'
[]
[v_drift]
type = WCNSFV2PMomentumDriftFlux
variable = vel_y
rho_d = ${rho_d}
fd = 'rho_mixture_var'
u_slip = 'vel_slip_x'
v_slip = 'vel_slip_y'
momentum_component = 'y'
[]
[v_viscosity]
type = INSFVMomentumDiffusion
variable = vel_y
mu = 'mu_mixture'
limit_interpolation = true
momentum_component = 'y'
[]
[v_pressure]
type = INSFVMomentumPressure
variable = vel_y
momentum_component = 'y'
pressure = pressure
[]
[phase_2_advection]
type = INSFVScalarFieldAdvection
variable = phase_2
u_slip = 'vel_x'
v_slip = 'vel_y'
velocity_interp_method = ${velocity_interp_method}
advected_interp_method = 'upwind'
[]
[phase_2_diffusion]
type = FVDiffusion
variable = phase_2
coeff = 1.0
[]
[phase_2_src]
type = NSFVMixturePhaseInterface
variable = phase_2
phase_coupled = phase_1
alpha = ${mass_exchange_coeff}
[]
[interface_area_advection]
type = INSFVScalarFieldAdvection
variable = interface_area
velocity_interp_method = ${velocity_interp_method}
advected_interp_method = 'upwind'
[]
[interface_area_diffusion]
type = FVDiffusion
variable = interface_area
coeff = 0.1
[]
[interface_area_source_sink]
type = WCNSFV2PInterfaceAreaSourceSink
variable = interface_area
u = 'vel_x'
v = 'vel_y'
L = ${fparse l/2}
rho = 'rho_mixture'
rho_d = 'rho'
pressure = 'pressure'
k_c = '${fparse mass_exchange_coeff}'
fd = 'phase_2'
sigma = 1e-3
[]
[]
[FVBCs]
[inlet-u]
type = INSFVInletVelocityBC
boundary = 'left'
variable = vel_x
functor = '${U}'
[]
[inlet-v]
type = INSFVInletVelocityBC
boundary = 'left'
variable = vel_y
functor = '0'
[]
[walls-u]
type = INSFVNoSlipWallBC
boundary = 'top'
variable = vel_x
function = 0
[]
[walls-v]
type = INSFVNoSlipWallBC
boundary = 'top'
variable = vel_y
function = 0
[]
[outlet_p]
type = INSFVOutletPressureBC
boundary = 'right'
variable = pressure
function = '${outlet_pressure}'
[]
[inlet_phase_2]
type = FVDirichletBC
boundary = 'left'
variable = phase_2
value = ${inlet_phase_2}
[]
[inlet_interface_area]
type = FVDirichletBC
boundary = 'left'
variable = interface_area
value = ${inlet_interface_area}
[]
[symmetry-u]
type = PINSFVSymmetryVelocityBC
boundary = 'bottom'
variable = vel_x
u = vel_x
v = vel_y
mu = 'mu_mixture'
momentum_component = 'x'
[]
[symmetry-v]
type = PINSFVSymmetryVelocityBC
boundary = 'bottom'
variable = vel_y
u = vel_x
v = vel_y
mu = 'mu_mixture'
momentum_component = 'y'
[]
[symmetry-p]
type = INSFVSymmetryPressureBC
boundary = 'bottom'
variable = pressure
[]
[symmetry-phase-2]
type = INSFVSymmetryScalarBC
boundary = 'bottom'
variable = phase_2
[]
[symmetry-interface-area]
type = INSFVSymmetryScalarBC
boundary = 'bottom'
variable = interface_area
[]
[]
[AuxVariables]
[drag_coefficient]
type = MooseVariableFVReal
[]
[rho_mixture_var]
type = MooseVariableFVReal
[]
[mu_mixture_var]
type = MooseVariableFVReal
[]
[]
[AuxKernels]
[populate_cd]
type = FunctorAux
variable = drag_coefficient
functor = 'Darcy_coefficient'
[]
[populate_rho_mixture_var]
type = FunctorAux
variable = rho_mixture_var
functor = 'rho_mixture'
[]
[populate_mu_mixture_var]
type = FunctorAux
variable = mu_mixture_var
functor = 'mu_mixture'
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[FunctorMaterials]
[bubble_properties]
type = GeneralFunctorFluidProps
fp = 'fp'
pressure = 'pressure'
T_fluid = 300.0
speed = 1.0
characteristic_length = 1.0
porosity = 1.0
output_properties = 'rho'
outputs = 'out'
[]
[populate_u_slip]
type = WCNSFV2PSlipVelocityFunctorMaterial
slip_velocity_name = 'vel_slip_x'
momentum_component = 'x'
u = 'vel_x'
v = 'vel_y'
rho = ${rho}
mu = 'mu_mixture'
rho_d = ${rho_d}
particle_diameter = ${dp}
linear_coef_name = 'Darcy_coefficient'
[]
[populate_v_slip]
type = WCNSFV2PSlipVelocityFunctorMaterial
slip_velocity_name = 'vel_slip_y'
momentum_component = 'y'
u = 'vel_x'
v = 'vel_y'
rho = ${rho}
mu = 'mu_mixture'
rho_d = ${rho_d}
particle_diameter = ${dp}
linear_coef_name = 'Darcy_coefficient'
[]
[compute_phase_1]
type = ADParsedFunctorMaterial
property_name = phase_1
functor_names = 'phase_2'
expression = '1 - phase_2'
[]
[CD]
type = NSFVDispersePhaseDragFunctorMaterial
rho = 'rho_mixture'
mu = mu_mixture
u = 'vel_x'
v = 'vel_y'
particle_diameter = ${dp}
[]
[mixing_material]
type = NSFVMixtureFunctorMaterial
phase_2_names = '${rho} ${mu}'
phase_1_names = 'rho ${mu_d}'
prop_names = 'rho_mixture mu_mixture'
phase_1_fraction = 'phase_2'
[]
[]
[Executioner]
type = Steady
solve_type = 'NEWTON'
nl_rel_tol = 1e-10
line_search = 'none'
[]
[Debug]
show_var_residual_norms = true
[]
[Preconditioning]
[SMP]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_shift_type'
petsc_options_value = 'lu NONZERO'
[]
[]
[Outputs]
[out]
type = Exodus
[]
[]
[Postprocessors]
[Re]
type = ParsedPostprocessor
expression = '${rho} * ${l} * ${U}'
pp_names = ''
[]
[rho_outlet]
type = SideAverageValue
boundary = 'right'
variable = 'rho_mixture_var'
[]
[]
(modules/navier_stokes/test/tests/finite_volume/cns/stagnation_inlet/supersonic_nozzle_hllc.i)
stagnation_pressure = 1
stagnation_temperature = 1
[GlobalParams]
fp = fp
[]
[Debug]
show_material_props = true
[]
[Mesh]
[file]
type = FileMeshGenerator
file = supersonic_nozzle.e
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Variables]
[rho]
family = MONOMIAL
order = CONSTANT
fv = true
initial_condition = 0.0034
[]
[rho_u]
family = MONOMIAL
order = CONSTANT
fv = true
initial_condition = 1e-4
outputs = none
[]
[rho_v]
family = MONOMIAL
order = CONSTANT
fv = true
outputs = none
[]
[rho_E]
family = MONOMIAL
order = CONSTANT
fv = true
initial_condition = 2.5
[]
[]
[FVKernels]
# Mass conservation
[mass_time]
type = FVTimeKernel
variable = rho
[]
[mass_advection]
type = CNSFVMassHLLC
variable = rho
[]
# Momentum x conservation
[momentum_x_time]
type = FVTimeKernel
variable = rho_u
[]
[momentum_x_advection]
type = CNSFVMomentumHLLC
variable = rho_u
momentum_component = x
[]
# Momentum y conservation
[momentum_y_time]
type = FVTimeKernel
variable = rho_v
[]
[momentum_y_advection]
type = CNSFVMomentumHLLC
variable = rho_v
momentum_component = y
[]
# Fluid energy conservation
[fluid_energy_time]
type = FVTimeKernel
variable = rho_E
[]
[fluid_energy_advection]
type = CNSFVFluidEnergyHLLC
variable = rho_E
[]
[]
[FVBCs]
## inflow stagnation boundaries
[mass_stagnation_inflow]
type = CNSFVHLLCMassStagnationInletBC
variable = rho
stagnation_pressure = ${stagnation_pressure}
stagnation_temperature = ${stagnation_temperature}
boundary = left
[]
[momentum_x_stagnation_inflow]
type = CNSFVHLLCMomentumStagnationInletBC
variable = rho_u
momentum_component = x
stagnation_pressure = ${stagnation_pressure}
stagnation_temperature = ${stagnation_temperature}
boundary = left
[]
[momentum_y_stagnation_inflow]
type = CNSFVHLLCMomentumStagnationInletBC
variable = rho_v
momentum_component = y
stagnation_pressure = ${stagnation_pressure}
stagnation_temperature = ${stagnation_temperature}
boundary = left
[../]
[fluid_energy_stagnation_inflow]
type = CNSFVHLLCFluidEnergyStagnationInletBC
variable = rho_E
stagnation_pressure = ${stagnation_pressure}
stagnation_temperature = ${stagnation_temperature}
boundary = left
[]
## outflow implicit conditions
[mass_outflow]
type = CNSFVHLLCMassImplicitBC
variable = rho
boundary = right
[]
[momentum_x_outflow]
type = CNSFVHLLCMomentumImplicitBC
variable = rho_u
momentum_component = x
boundary = right
[]
[momentum_y_outflow]
type = CNSFVHLLCMomentumImplicitBC
variable = rho_v
momentum_component = y
boundary = right
[]
[fluid_energy_outflow]
type = CNSFVHLLCFluidEnergyImplicitBC
variable = rho_E
boundary = right
[]
# wall conditions
[momentum_x_pressure_wall]
type = CNSFVMomImplicitPressureBC
variable = rho_u
momentum_component = x
boundary = wall
[]
[momentum_y_pressure_wall]
type = CNSFVMomImplicitPressureBC
variable = rho_v
momentum_component = y
boundary = wall
[]
[]
[AuxVariables]
[Ma]
family = MONOMIAL
order = CONSTANT
[]
[Ma_layered]
family = MONOMIAL
order = CONSTANT
[]
[]
[UserObjects]
[layered_Ma_UO]
type = LayeredAverage
variable = Ma
num_layers = 100
direction = x
[]
[]
[AuxKernels]
[Ma_aux]
type = NSMachAux
variable = Ma
fluid_properties = fp
use_material_properties = true
[]
[Ma_layered_aux]
type = SpatialUserObjectAux
variable = Ma_layered
user_object = layered_Ma_UO
[]
[]
[Materials]
[var_mat]
type = ConservedVarValuesMaterial
rho = rho
rhou = rho_u
rhov = rho_v
rho_et = rho_E
[]
[fluid_props]
type = GeneralFluidProps
porosity = 1
characteristic_length = 1
[]
[sound_speed]
type = SoundspeedMat
fp = fp
[]
[]
[Postprocessors]
[cfl_dt]
type = ADCFLTimeStepSize
c_names = 'sound_speed'
vel_names = 'speed'
CFL = 0.5
[]
[outflow_Ma]
type = SideAverageValue
variable = Ma
boundary = right
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
[]
[]
[Executioner]
type = Transient
end_time = 0.1
[TimeIntegrator]
type = ExplicitSSPRungeKutta
order = 2
[]
l_tol = 1e-8
[TimeStepper]
type = PostprocessorDT
postprocessor = cfl_dt
[]
[]
[VectorPostprocessors]
[Ma_layered]
type = LineValueSampler
variable = Ma_layered
start_point = '0 0 0'
end_point = '10 0 0'
num_points = 100
sort_by = x
[]
[]
[Outputs]
exodus = true
[]
(modules/thermal_hydraulics/test/tests/components/deprecated/gate_valve.i)
[GlobalParams]
gravity_vector = '0 0 0'
closures = simple_closures
fp = fp
f = 0.0
initial_T = 300
initial_p = 1e5
initial_vel = 0
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02897
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[inlet]
type = InletMassFlowRateTemperature1Phase
input = 'pipe1:in'
m_dot = 1
T = 300
[]
[pipe1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = 2
A = 0.1
[]
[valve]
type = GateValve
connections = 'pipe1:out pipe2:in'
open_area_fraction = 1
[]
[pipe2]
type = FlowChannel1Phase
position = '0.5 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = 2
A = 0.1
[]
[outlet]
type = Outlet1Phase
input = 'pipe2:out'
p = 1e5
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
solve_type = NEWTON
nl_rel_tol = 1e-8
nl_abs_tol = 1e-8
nl_max_its = 20
l_tol = 1e-4
start_time = 0.0
end_time = 1.0
dt = 0.01
abort_on_solve_fail = true
[]
(modules/fluid_properties/test/tests/fp_interrogator/1ph.rho_p.i)
[FluidPropertiesInterrogator]
fp = fp
rho = 1
p = 1e5
[]
[FluidProperties]
[./fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02900055737704918
mu = 1.823e-05
k = 0.02568
[../]
[]
(modules/thermal_hydraulics/test/tests/components/heat_transfer_from_external_app_1phase/phy.q_wall_transfer_3eqn.child.i)
# This is a part of phy.q_wall_transfer_3eqn test. See the master file for details.
[GlobalParams]
initial_p = 1.e5
initial_vel = 0.
initial_T = 300.
closures = simple_closures
[]
[FluidProperties]
[eos]
type = IdealGasFluidProperties
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[pipe1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 1
n_elems = 10
A = 9.6858407346e-01
D_h = 6.1661977237e+00
f = 0.01
fp = eos
[]
[hxconn]
type = HeatTransferFromExternalAppHeatFlux1Phase
flow_channel = pipe1
Hw = 1e3
[]
[inlet]
type = SolidWall1Phase
input = 'pipe1:in'
[]
[outlet]
type = SolidWall1Phase
input = 'pipe1:out'
[]
[]
[Preconditioning]
[SMP_PJFNK]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'bdf2'
dt = 0.5
dtmin = 1e-7
abort_on_solve_fail = true
solve_type = 'PJFNK'
line_search = 'basic'
nl_rel_tol = 1e-8
nl_abs_tol = 1e-6
nl_max_its = 20
l_tol = 1e-3
l_max_its = 300
start_time = 0.0
end_time = 5
[Quadrature]
type = GAUSS
order = SECOND
[]
[]
[Outputs]
exodus = true
show = 'q_wall'
[]
(modules/thermal_hydraulics/test/tests/problems/sod_shock_tube/sod_shock_tube.i)
# This test problem is the classic Sod shock tube test problem,
# which is a Riemann problem with the following parameters:
# * domain = (0,1)
# * gravity = 0
# * EoS: Ideal gas EoS with gamma = 1.4, R = 0.71428571428571428571
# * interface: x = 0.5
# * typical end time: 0.2
# Left initial values:
# * rho = 1
# * vel = 0
# * p = 1
# Right initial values:
# * rho = 0.125
# * vel = 0
# * p = 0.1
#
# The output can be viewed by opening Paraview with the state file `plot.pvsm`:
# paraview --state=plot.pvsm
# This will plot the numerical solution against the analytical solution
[Functions]
[p_ic_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.5 1.0'
y = '1.0 0.1'
[]
[T_ic_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.5 1.0'
y = '1.4 1.12'
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 11.64024372
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[pipe]
type = FlowChannel1Phase
fp = fp
# geometry
position = '0 0 0'
orientation = '1 0 0'
length = 1.0
n_elems = 100
A = 1.0
gravity_vector = '0 0 0'
# IC
initial_T = T_ic_fn
initial_p = p_ic_fn
initial_vel = 0
f = 0
closures = simple_closures
rdg_slope_reconstruction = minmod
[]
[left_boundary]
type = FreeBoundary1Phase
input = 'pipe:in'
[]
[right_boundary]
type = FreeBoundary1Phase
input = 'pipe:out'
[]
[]
[Executioner]
type = Transient
[TimeIntegrator]
type = ExplicitSSPRungeKutta
[]
solve_type = LINEAR
l_tol = 1e-4
nl_rel_tol = 1e-20
nl_abs_tol = 1e-8
nl_max_its = 60
# run to t = 0.2
start_time = 0.0
dt = 1e-3
num_steps = 200
abort_on_solve_fail = true
[]
[Outputs]
file_base = 'sod_shock_tube'
velocity_as_vector = false
execute_on = 'initial timestep_end'
[out]
type = Exodus
show = 'rho p vel'
[]
[]
(modules/thermal_hydraulics/test/tests/problems/mms/mms_1phase.i)
# Method of manufactured solutions (MMS) problem for 1-phase flow model.
#
# The python script mms_derivation.py derives the MMS sources used in this
# input file.
#
# To perform a convergence study, run this input file with different values of
# 'refinement_level', starting with 0. Manually create a CSV file (call it the
# "convergence CSV file") to store the error vs. mesh size data. It should have
# the columns specified in the plot script plot_convergence_1phase.py. Copy the
# CSV output from each run into the convergence CSV file. After all of the runs,
# run the plot script using python.
refinement_level = 0 # 0 is initial
n_elems_coarse = 10
n_elems = ${fparse int(n_elems_coarse * 2^refinement_level)}
dt = 1e-6
t_end = ${fparse dt * 10}
area = 1.0
gamma = 2.0
M = 0.05
A = 1
B = 1
C = 1
aA = ${fparse area}
R_univ = 8.3144598
R = ${fparse R_univ / M}
cp = ${fparse gamma * R / (gamma - 1.0)}
cv = ${fparse cp / gamma}
[GlobalParams]
gravity_vector = '0 0 0'
closures = simple_closures
[]
[Functions]
# solutions
[rho_fn]
type = ParsedFunction
expression = 'A * (sin(B*x + C*t) + 2)'
symbol_names = 'A B C'
symbol_values = '${A} ${B} ${C}'
[]
[vel_fn]
type = ParsedFunction
expression = 'A * t * sin(pi * x)'
symbol_names = 'A'
symbol_values = '${A}'
[]
[p_fn]
type = ParsedFunction
expression = 'A * (cos(B*x + C*t) + 2)'
symbol_names = 'A B C'
symbol_values = '${A} ${B} ${C}'
[]
[T_fn]
type = ParsedFunction
expression = '(cos(B*x + C*t) + 2)/(cv*(gamma - 1)*(sin(B*x + C*t) + 2))'
symbol_names = 'B C gamma cv'
symbol_values = '${B} ${C} ${gamma} ${cv}'
[]
# MMS sources
[rho_src_fn]
type = ParsedFunction
expression = 'A^2*B*t*sin(pi*x)*cos(B*x + C*t) + pi*A^2*t*(sin(B*x + C*t) + 2)*cos(pi*x) + A*C*cos(B*x + C*t)'
symbol_names = 'A B C'
symbol_values = '${A} ${B} ${C}'
[]
[rhou_src_fn]
type = ParsedFunction
expression = 'A^3*B*t^2*sin(pi*x)^2*cos(B*x + C*t) + 2*pi*A^3*t^2*(sin(B*x + C*t) + 2)*sin(pi*x)*cos(pi*x) + A^2*C*t*sin(pi*x)*cos(B*x + C*t) + A^2*(sin(B*x + C*t) + 2)*sin(pi*x) - A*B*sin(B*x + C*t)'
symbol_names = 'A B C'
symbol_values = '${A} ${B} ${C}'
[]
[rhoE_src_fn]
type = ParsedFunction
expression = 'A*C*(A^2*t^2*sin(pi*x)^2/2 + (cos(B*x + C*t) + 2)/((gamma - 1)*(sin(B*x + C*t) + 2)))*cos(B*x + C*t) + pi*A*t*(A*(A^2*t^2*sin(pi*x)^2/2 + (cos(B*x + C*t) + 2)/((gamma - 1)*(sin(B*x + C*t) + 2)))*(sin(B*x + C*t) + 2) + A*(cos(B*x + C*t) + 2))*cos(pi*x) + A*t*(A*B*(A^2*t^2*sin(pi*x)^2/2 + (cos(B*x + C*t) + 2)/((gamma - 1)*(sin(B*x + C*t) + 2)))*cos(B*x + C*t) - A*B*sin(B*x + C*t) + A*(sin(B*x + C*t) + 2)*(pi*A^2*t^2*sin(pi*x)*cos(pi*x) - B*sin(B*x + C*t)/((gamma - 1)*(sin(B*x + C*t) + 2)) - B*(cos(B*x + C*t) + 2)*cos(B*x + C*t)/((gamma - 1)*(sin(B*x + C*t) + 2)^2)))*sin(pi*x) + A*(sin(B*x + C*t) + 2)*(A^2*t*sin(pi*x)^2 - C*sin(B*x + C*t)/((gamma - 1)*(sin(B*x + C*t) + 2)) - C*(cos(B*x + C*t) + 2)*cos(B*x + C*t)/((gamma - 1)*(sin(B*x + C*t) + 2)^2))'
symbol_names = 'A B C gamma'
symbol_values = '${A} ${B} ${C} ${gamma}'
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = ${gamma}
molar_mass = ${M}
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[pipe]
type = FlowChannel1Phase
fp = fp
# geometry
position = '0 0 0'
orientation = '1 0 0'
length = 1.0
n_elems = ${n_elems}
A = ${area}
# IC
initial_p = p_fn
initial_T = T_fn
initial_vel = 0
f = 0
[]
[left_boundary]
type = InletFunction1Phase
input = 'pipe:in'
p = p_fn
rho = rho_fn
vel = vel_fn
[]
[right_boundary]
type = InletFunction1Phase
input = 'pipe:out'
p = p_fn
rho = rho_fn
vel = vel_fn
[]
[]
[Kernels]
[rho_src]
type = BodyForce
variable = rhoA
function = rho_src_fn
value = ${aA}
[]
[rhou_src]
type = BodyForce
variable = rhouA
function = rhou_src_fn
value = ${aA}
[]
[rhoE_src]
type = BodyForce
variable = rhoEA
function = rhoE_src_fn
value = ${aA}
[]
[]
[Postprocessors]
[rho_err]
type = ElementL1Error
variable = rho
function = rho_fn
execute_on = 'INITIAL TIMESTEP_END'
[]
[vel_err]
type = ElementL1Error
variable = vel
function = vel_fn
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_err]
type = ElementL1Error
variable = p
function = p_fn
execute_on = 'INITIAL TIMESTEP_END'
[]
[]
[Executioner]
type = Transient
[TimeIntegrator]
type = ExplicitSSPRungeKutta
order = 3
[]
start_time = 0
dt = ${dt}
end_time = ${t_end}
abort_on_solve_fail = true
[Quadrature]
type = GAUSS
order = FIRST
[]
[]
[Outputs]
csv = true
execute_on = 'FINAL'
velocity_as_vector = false
[]
(modules/thermal_hydraulics/tutorials/single_phase_flow/06_custom_closures.i)
T_in = 300. # K
m_dot_in = 1e-2 # kg/s
press = 10e5 # Pa
# core parameters
core_length = 1. # m
core_n_elems = 25
core_dia = '${units 2. cm -> m}'
core_pitch = '${units 8.7 cm -> m}'
A_core = '${fparse core_pitch^2 - 0.25 *pi * core_dia^2}'
P_wet_core = '${fparse 4*core_pitch + pi * core_dia}'
Dh_core = '${fparse 4 * A_core / P_wet_core}'
# pipe parameters
pipe_dia = '${units 10. cm -> m}'
A_pipe = '${fparse 0.25 * pi * pipe_dia^2}'
tot_power = 2000 # W
# heat exchanger parameters
hx_dia_inner = '${units 12. cm -> m}'
hx_wall_thickness = '${units 5. mm -> m}'
hx_dia_outer = '${units 50. cm -> m}'
hx_radius_wall = '${fparse hx_dia_inner / 2. + hx_wall_thickness}'
hx_length = 1.5 # m
hx_n_elems = 25
m_dot_sec_in = 1. # kg/s
[GlobalParams]
initial_p = ${press}
initial_vel = 0.0001
initial_T = ${T_in}
initial_vel_x = 0
initial_vel_y = 0
initial_vel_z = 0
gravity_vector = '0 0 0'
rdg_slope_reconstruction = minmod
scaling_factor_1phase = '1 1e-2 1e-4'
scaling_factor_rhoV = 1
scaling_factor_rhouV = 1e-2
scaling_factor_rhovV = 1e-2
scaling_factor_rhowV = 1e-2
scaling_factor_rhoEV = 1e-4
closures = thm_closures
fp = he
[]
[Functions]
[m_dot_sec_fn]
type = PiecewiseLinear
xy_data = '
0 0
10 ${m_dot_sec_in}'
[]
[]
[FluidProperties]
[he]
type = IdealGasFluidProperties
molar_mass = 4e-3
gamma = 1.67
k = 0.2556
mu = 3.22639e-5
[]
[water]
type = StiffenedGasFluidProperties
gamma = 2.35
cv = 1816.0
q = -1.167e6
p_inf = 1.0e9
q_prime = 0
[]
[]
[Closures]
[thm_closures]
type = Closures1PhaseTHM
[]
[]
[Materials]
[Re_mat]
type = ADReynoldsNumberMaterial
Re = Re
rho = rho
vel = vel
D_h = D_h
mu = mu
block = hx/pri
[]
[f_mat]
type = ADParsedMaterial
property_name = f_D
constant_names = 'a b c'
constant_expressions = '1 0.1 -0.5'
material_property_names = 'Re'
expression = 'a + b * Re^c'
block = hx/pri
[]
[Pr_mat]
type = ADPrandtlNumberMaterial
Pr = Pr
cp = cp
mu = mu
k = k
block = hx/pri
[]
[Nu_mat]
type = ADParsedMaterial
property_name = 'Nu'
constant_names = 'a b c'
constant_expressions = '0.03 0.9 0.5'
material_property_names = 'Re Pr'
expression = 'a * Re ^b * Pr^c'
block = hx/pri
[]
[Hw_mat]
type = ADConvectiveHeatTransferCoefficientMaterial
D_h = D_h
k = k
Nu = Nu
Hw = Hw
block = hx/pri
[]
[]
[SolidProperties]
[steel]
type = ThermalFunctionSolidProperties
rho = 8050
k = 45
cp = 466
[]
[]
[Components]
[total_power]
type = TotalPower
power = ${tot_power}
[]
[up_pipe_1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '0 0 1'
length = 0.5
n_elems = 15
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct1]
type = JunctionParallelChannels1Phase
position = '0 0 0.5'
connections = 'up_pipe_1:out core_chan:in'
volume = 1e-5
[]
[core_chan]
type = FlowChannel1Phase
position = '0 0 0.5'
orientation = '0 0 1'
length = ${core_length}
n_elems = ${core_n_elems}
roughness = .0001
A = ${A_core}
D_h = ${Dh_core}
[]
[core_hs]
type = HeatStructureCylindrical
position = '0 0 0.5'
orientation = '0 0 1'
length = ${core_length}
n_elems = ${core_n_elems}
names = 'block'
widths = '${fparse core_dia / 2.}'
solid_properties = 'steel'
solid_properties_T_ref = '300'
n_part_elems = 3
[]
[core_heating]
type = HeatSourceFromTotalPower
hs = core_hs
regions = block
power = total_power
[]
[core_ht]
type = HeatTransferFromHeatStructure1Phase
flow_channel = core_chan
hs = core_hs
hs_side = outer
P_hf = '${fparse pi * core_dia}'
[]
[jct2]
type = JunctionParallelChannels1Phase
position = '0 0 1.5'
connections = 'core_chan:out up_pipe_2:in'
volume = 1e-5
[]
[up_pipe_2]
type = FlowChannel1Phase
position = '0 0 1.5'
orientation = '0 0 1'
length = 0.5
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct3]
type = JunctionOneToOne1Phase
connections = 'up_pipe_2:out top_pipe_1:in'
[]
[top_pipe_1]
type = FlowChannel1Phase
position = '0 0 2'
orientation = '1 0 0'
length = 0.5
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[top_pipe_2]
type = FlowChannel1Phase
position = '0.5 0 2'
orientation = '1 0 0'
length = 0.5
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct4]
type = VolumeJunction1Phase
position = '0.5 0 2'
volume = 1e-5
connections = 'top_pipe_1:out top_pipe_2:in press_pipe:in'
[]
[press_pipe]
type = FlowChannel1Phase
position = '0.5 0 2'
orientation = '0 1 0'
length = 0.2
n_elems = 5
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[pressurizer]
type = InletStagnationPressureTemperature1Phase
p0 = ${press}
T0 = ${T_in}
input = press_pipe:out
[]
[jct5]
type = JunctionOneToOne1Phase
connections = 'top_pipe_2:out down_pipe_1:in'
[]
[down_pipe_1]
type = FlowChannel1Phase
position = '1 0 2'
orientation = '0 0 -1'
length = 0.25
A = ${A_pipe}
n_elems = 5
[]
[jct6]
type = JunctionParallelChannels1Phase
position = '1 0 1.75'
connections = 'down_pipe_1:out hx/pri:in'
volume = 1e-5
[]
[hx]
[pri]
type = FlowChannel1Phase
position = '1 0 1.75'
orientation = '0 0 -1'
length = ${hx_length}
n_elems = ${hx_n_elems}
roughness = 1e-5
A = '${fparse pi * hx_dia_inner * hx_dia_inner / 4.}'
D_h = ${hx_dia_inner}
closures = ''
[]
[ht_pri]
type = HeatTransferFromHeatStructure1Phase
hs = hx/wall
hs_side = inner
flow_channel = hx/pri
P_hf = '${fparse pi * hx_dia_inner}'
[]
[wall]
type = HeatStructureCylindrical
position = '1 0 1.75'
orientation = '0 0 -1'
length = ${hx_length}
n_elems = ${hx_n_elems}
widths = '${hx_wall_thickness}'
n_part_elems = '3'
solid_properties = 'steel'
solid_properties_T_ref = '300'
names = '0'
inner_radius = '${fparse hx_dia_inner / 2.}'
[]
[ht_sec]
type = HeatTransferFromHeatStructure1Phase
hs = hx/wall
hs_side = outer
flow_channel = hx/sec
P_hf = '${fparse 2 * pi * hx_radius_wall}'
[]
[sec]
type = FlowChannel1Phase
position = '${fparse 1 + hx_wall_thickness} 0 0.25'
orientation = '0 0 1'
length = ${hx_length}
n_elems = ${hx_n_elems}
A = '${fparse pi * (hx_dia_outer * hx_dia_outer / 4. - hx_radius_wall * hx_radius_wall)}'
D_h = '${fparse hx_dia_outer - (2 * hx_radius_wall)}'
fp = water
initial_T = 300
[]
[]
[jct7]
type = JunctionParallelChannels1Phase
position = '1 0 0.5'
connections = 'hx/pri:out down_pipe_2:in'
volume = 1e-5
[]
[down_pipe_2]
type = FlowChannel1Phase
position = '1 0 0.25'
orientation = '0 0 -1'
length = 0.25
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct8]
type = JunctionOneToOne1Phase
connections = 'down_pipe_2:out bottom_1:in'
[]
[bottom_1]
type = FlowChannel1Phase
position = '1 0 0'
orientation = '-1 0 0'
length = 0.5
n_elems = 5
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[pump]
type = Pump1Phase
position = '0.5 0 0'
connections = 'bottom_1:out bottom_2:in'
volume = 1e-4
A_ref = ${A_pipe}
head = 0
[]
[bottom_2]
type = FlowChannel1Phase
position = '0.5 0 0'
orientation = '-1 0 0'
length = 0.5
n_elems = 5
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct9]
type = JunctionOneToOne1Phase
connections = 'bottom_2:out up_pipe_1:in'
[]
[inlet_sec]
type = InletMassFlowRateTemperature1Phase
input = 'hx/sec:in'
m_dot = 0
T = 300
[]
[outlet_sec]
type = Outlet1Phase
input = 'hx/sec:out'
p = 1e5
[]
[]
[ControlLogic]
[set_point]
type = GetFunctionValueControl
function = ${m_dot_in}
[]
[pid]
type = PIDControl
initial_value = 0.0
set_point = set_point:value
input = m_dot_pump
K_p = 1.
K_i = 4.
K_d = 0
[]
[set_pump_head]
type = SetComponentRealValueControl
component = pump
parameter = head
value = pid:output
[]
[m_dot_sec_inlet_ctrl]
type = GetFunctionValueControl
function = m_dot_sec_fn
[]
[set_m_dot_sec_ctrl]
type = SetComponentRealValueControl
component = inlet_sec
parameter = m_dot
value = m_dot_sec_inlet_ctrl:value
[]
[]
[Postprocessors]
[power_to_coolant]
type = ADHeatRateConvection1Phase
block = core_chan
P_hf = '${fparse pi *core_dia}'
[]
[m_dot_pump]
type = ADFlowJunctionFlux1Phase
boundary = core_chan:in
connection_index = 1
equation = mass
junction = jct7
[]
[core_T_out]
type = SideAverageValue
boundary = core_chan:out
variable = T
[]
[core_p_in]
type = SideAverageValue
boundary = core_chan:in
variable = p
[]
[core_p_out]
type = SideAverageValue
boundary = core_chan:out
variable = p
[]
[core_delta_p]
type = ParsedPostprocessor
pp_names = 'core_p_in core_p_out'
expression = 'core_p_in - core_p_out'
[]
[hx_pri_T_out]
type = SideAverageValue
boundary = hx/pri:out
variable = T
[]
[hx_sec_T_in]
type = SideAverageValue
boundary = inlet_sec
variable = T
[]
[hx_sec_T_out]
type = SideAverageValue
boundary = outlet_sec
variable = T
[]
[m_dot_sec]
type = ADFlowBoundaryFlux1Phase
boundary = inlet_sec
equation = mass
[]
[Hw_hx_pri]
type = ADElementAverageMaterialProperty
mat_prop = Hw
block = hx/pri
[]
[fD_hx_pri]
type = ADElementAverageMaterialProperty
mat_prop = f_D
block = hx/pri
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
start_time = 0
[TimeStepper]
type = IterationAdaptiveDT
dt = 1
[]
dtmax = 5
end_time = 500
line_search = basic
solve_type = NEWTON
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_rel_tol = 1e-8
nl_abs_tol = 1e-8
nl_max_its = 25
[]
[Outputs]
exodus = true
[console]
type = Console
max_rows = 1
outlier_variable_norms = false
[]
print_linear_residuals = false
[]
(modules/thermal_hydraulics/test/tests/materials/fluid_properties_gas_mix_material/fluid_properties_gas_mix_material.i)
mass_fraction = 0.4
vel = 10
area = 0.2
# computed at p = 1e5 Pa, T = 300 K:
rho = 1.30632939267729
e_value = 1.789042384551724e+05
E = ${fparse e_value + 0.5 * vel * vel}
rhoA = ${fparse rho * area}
xirhoA = ${fparse mass_fraction * rhoA}
rhouA = ${fparse rhoA * vel}
rhoEA = ${fparse rhoA * E}
[Mesh]
type = GeneratedMesh
dim = 1
nx = 1
[]
[FluidProperties]
[fp1]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.029
[]
[fp2]
type = IdealGasFluidProperties
gamma = 1.5
molar_mass = 0.04
[]
[mixture_fp]
type = IdealGasMixtureFluidProperties
component_fluid_properties = 'fp1 fp2'
[]
[]
[Materials]
[fp_mat]
type = FluidPropertiesGasMixMaterial
xirhoA = xirhoA
rhoA = rhoA
rhouA = rhouA
rhoEA = rhoEA
area = A
fluid_properties = mixture_fp
[]
[]
[AuxVariables]
[A]
initial_condition = ${area}
[]
[xirhoA]
initial_condition = ${xirhoA}
[]
[rhoA]
initial_condition = ${rhoA}
[]
[rhouA]
initial_condition = ${rhouA}
[]
[rhoEA]
initial_condition = ${rhoEA}
[]
[mass_fraction]
family = MONOMIAL
order = CONSTANT
[]
[rho]
family = MONOMIAL
order = CONSTANT
[]
[v]
family = MONOMIAL
order = CONSTANT
[]
[vel]
family = MONOMIAL
order = CONSTANT
[]
[e]
family = MONOMIAL
order = CONSTANT
[]
[p]
family = MONOMIAL
order = CONSTANT
[]
[T]
family = MONOMIAL
order = CONSTANT
[]
[h]
family = MONOMIAL
order = CONSTANT
[]
[H]
family = MONOMIAL
order = CONSTANT
[]
[c]
family = MONOMIAL
order = CONSTANT
[]
[cp]
family = MONOMIAL
order = CONSTANT
[]
[cv]
family = MONOMIAL
order = CONSTANT
[]
[k]
family = MONOMIAL
order = CONSTANT
[]
[mu]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[mass_fraction_aux]
type = ADMaterialRealAux
variable = mass_fraction
property = mass_fraction
execute_on = 'INITIAL'
[]
[rho_aux]
type = ADMaterialRealAux
variable = rho
property = rho
execute_on = 'INITIAL'
[]
[v_aux]
type = ADMaterialRealAux
variable = v
property = v
execute_on = 'INITIAL'
[]
[vel_aux]
type = ADMaterialRealAux
variable = vel
property = vel
execute_on = 'INITIAL'
[]
[e_aux]
type = ADMaterialRealAux
variable = e
property = e
execute_on = 'INITIAL'
[]
[p_aux]
type = ADMaterialRealAux
variable = p
property = p
execute_on = 'INITIAL'
[]
[T_aux]
type = ADMaterialRealAux
variable = T
property = T
execute_on = 'INITIAL'
[]
[h_aux]
type = ADMaterialRealAux
variable = h
property = h
execute_on = 'INITIAL'
[]
[H_aux]
type = ADMaterialRealAux
variable = H
property = H
execute_on = 'INITIAL'
[]
[c_aux]
type = ADMaterialRealAux
variable = c
property = c
execute_on = 'INITIAL'
[]
[cp_aux]
type = ADMaterialRealAux
variable = cp
property = cp
execute_on = 'INITIAL'
[]
[cv_aux]
type = ADMaterialRealAux
variable = cv
property = cv
execute_on = 'INITIAL'
[]
[k_aux]
type = ADMaterialRealAux
variable = k
property = k
execute_on = 'INITIAL'
[]
[mu_aux]
type = ADMaterialRealAux
variable = mu
property = mu
execute_on = 'INITIAL'
[]
[]
[Postprocessors]
[mass_fraction]
type = ElementAverageValue
variable = mass_fraction
execute_on = 'INITIAL'
[]
[rho]
type = ElementAverageValue
variable = rho
execute_on = 'INITIAL'
[]
[v]
type = ElementAverageValue
variable = v
execute_on = 'INITIAL'
[]
[vel]
type = ElementAverageValue
variable = vel
execute_on = 'INITIAL'
[]
[e]
type = ElementAverageValue
variable = e
execute_on = 'INITIAL'
[]
[p]
type = ElementAverageValue
variable = p
execute_on = 'INITIAL'
[]
[T]
type = ElementAverageValue
variable = T
execute_on = 'INITIAL'
[]
[h]
type = ElementAverageValue
variable = h
execute_on = 'INITIAL'
[]
[H]
type = ElementAverageValue
variable = H
execute_on = 'INITIAL'
[]
[c]
type = ElementAverageValue
variable = c
execute_on = 'INITIAL'
[]
[cp]
type = ElementAverageValue
variable = cp
execute_on = 'INITIAL'
[]
[cv]
type = ElementAverageValue
variable = cv
execute_on = 'INITIAL'
[]
[k]
type = ElementAverageValue
variable = k
execute_on = 'INITIAL'
[]
[mu]
type = ElementAverageValue
variable = mu
execute_on = 'INITIAL'
[]
[]
[Problem]
solve = false
[]
[Executioner]
type = Steady
[]
[Outputs]
csv = true
execute_on = 'INITIAL'
[]
(modules/thermal_hydraulics/test/tests/components/deprecated/solid_wall.i)
[GlobalParams]
gravity_vector = '0 0 0'
closures = simple_closures
fp = fp
f = 0.0
initial_T = 300
initial_p = 1e5
initial_vel = 0
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02897
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[in]
type = SolidWall
input = 'pipe:in'
[]
[pipe]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = 2
A = 0.1
[]
[out]
type = SolidWall
input = 'pipe:out'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
solve_type = NEWTON
nl_rel_tol = 1e-8
nl_abs_tol = 1e-8
nl_max_its = 20
l_tol = 1e-4
start_time = 0.0
end_time = 1.0
dt = 0.01
abort_on_solve_fail = true
[]
(modules/fluid_properties/test/tests/fp_interrogator/2ph_ncg_p_T.i)
[FluidPropertiesInterrogator]
fp = fp_2phase_ncg
p = 1e5
T = 372.7559289
[]
[FluidProperties]
[fp_nitrogen]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02867055103448276
[]
[fp_2phase_ncg]
type = TestTwoPhaseNCGFluidProperties
fp_ncgs = 'fp_nitrogen'
[]
[]
(modules/porous_flow/test/tests/fluids/ideal_gas.i)
# Example of using the IdealGasFluidProperties userobject to provide fluid
# properties for an ideal gas. Use values for hydrogen (H2) at 1 MPa and 50 C.
#
# Input values:
# M = 2.01588e-3 kg/mol
# gamma = 1.4
# viscosity = 9.4393e-6 Pa.s
#
# Expected output:
# density = 750.2854 kg/m^3
# internal energy = 3.33 MJ/kg
# enthalpy = 4.66 MJ/kg
[Mesh]
type = GeneratedMesh
dim = 1
nx = 1
[]
[GlobalParams]
PorousFlowDictator = dictator
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[]
[Variables]
[pp]
initial_condition = 1e6
[]
[]
[Kernels]
[dummy]
type = Diffusion
variable = pp
[]
[]
[AuxVariables]
[temp]
initial_condition = 50.0
[]
[]
[FluidProperties]
[idealgas]
type = IdealGasFluidProperties
molar_mass = 2.01588e-3
gamma = 1.4
mu = 9.4393e-6
[]
[]
[Materials]
[temperature]
type = PorousFlowTemperature
temperature = temp
[]
[ppss]
type = PorousFlow1PhaseFullySaturated
porepressure = pp
[]
[idealgass]
type = PorousFlowSingleComponentFluid
temperature_unit = Celsius
fp = idealgas
phase = 0
[]
[]
[Executioner]
type = Steady
solve_type = Newton
[]
[Postprocessors]
[pressure]
type = ElementIntegralVariablePostprocessor
variable = pp
[]
[temperature]
type = ElementIntegralVariablePostprocessor
variable = temp
[]
[density]
type = ElementIntegralMaterialProperty
mat_prop = 'PorousFlow_fluid_phase_density_qp0'
[]
[viscosity]
type = ElementIntegralMaterialProperty
mat_prop = 'PorousFlow_viscosity_qp0'
[]
[internal_energy]
type = ElementIntegralMaterialProperty
mat_prop = 'PorousFlow_fluid_phase_internal_energy_qp0'
[]
[enthalpy]
type = ElementIntegralMaterialProperty
mat_prop = 'PorousFlow_fluid_phase_enthalpy_qp0'
[]
[]
[Outputs]
execute_on = 'timestep_end'
file_base = ideal_gas
csv = true
[]
(modules/fluid_properties/test/tests/two_phase_fluid_properties_independent/test.i)
# Tests the TwoPhaseFluidPropertiesIndependent class, which takes the names
# of 2 single-phase fluid properties independently. This test uses a dummy
# aux to make sure that the single-phase fluid properties can be recovered
# from the 2-phase fluid properties. A modification to this test checks that
# an error results if one tries to call a 2-phase fluid properties interface
# using this class, which is designed to ensure that the 2 phases are independent.
[Mesh]
type = GeneratedMesh
dim = 1
nx = 1
# Required for NodalVariableValue on distributed mesh
allow_renumbering = false
[]
[Problem]
solve = false
[]
[AuxVariables]
[./p]
initial_condition = 1e5
[../]
[./T]
initial_condition = 300
[../]
[./rho_avg]
[../]
[]
[FluidProperties]
# rho1 = 1.149425287 kg/m^3
[./fp1]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02867055103448276
[../]
# rho2 = 0.6666666667 kg/m^3
[./fp2]
type = IdealGasFluidProperties
gamma = 1.2
molar_mass = 0.0166289196
[../]
[./fp_2phase]
type = TwoPhaseFluidPropertiesIndependent
fp_liquid = fp1
fp_vapor = fp2
[../]
[]
[AuxKernels]
# correct value (0.5*(rho1 + rho2)) should be: 0.90804597685 kg/m^3
[./rho_avg_aux]
type = TwoPhaseAverageDensityAux
variable = rho_avg
p = p
T = T
fp_2phase = fp_2phase
execute_on = 'initial'
[../]
[]
[Postprocessors]
[./rho_avg_value]
type = NodalVariableValue
variable = rho_avg
nodeid = 0
[../]
[]
[Executioner]
type = Steady
[]
[Outputs]
execute_on = 'timestep_end'
csv = true
[]
(modules/navier_stokes/test/tests/finite_volume/two_phase/mixture_interface_area_model/pressure_driven_growth.i)
###############################################################################
# Validation test based on Hibiki and Ishii experiment [1] reported in Figure 3
# [1] Hibiki, T., & Ishii, M. (2000). One-group interfacial area transport of bubbly flows in vertical round tubes.
# International Journal of Heat and Mass Transfer, 43(15), 2711-2726.
###############################################################################
mu = 1.0
rho = 1000.0
mu_d = 1.0
rho_d = 1.0
l = ${fparse 50.8/1000.0}
U = 0.491230114
dp = 0.001
inlet_phase_2 = 0.049
advected_interp_method = 'upwind'
velocity_interp_method = 'rc'
mass_exchange_coeff = 0.0
inlet_interface_area = ${fparse 6.0*inlet_phase_2/dp}
outlet_pressure = 1e5
[GlobalParams]
rhie_chow_user_object = 'rc'
density_interp_method = 'average'
mu_interp_method = 'average'
[]
[Problem]
identify_variable_groups_in_nl = false
previous_nl_solution_required = true
[]
[UserObjects]
[rc]
type = INSFVRhieChowInterpolator
u = vel_x
v = vel_y
pressure = pressure
[]
[]
[Mesh]
coord_type = 'RZ'
rz_coord_axis = 'X'
[gen]
type = GeneratedMeshGenerator
dim = 2
xmin = 0
xmax = '${fparse l * 60}'
ymin = 0
ymax = '${fparse l / 2}'
nx = 20
ny = 5
[]
uniform_refine = 0
[]
[Variables]
[vel_x]
type = INSFVVelocityVariable
initial_condition = 0
[]
[vel_y]
type = INSFVVelocityVariable
initial_condition = 0
[]
[pressure]
type = INSFVPressureVariable
[]
[phase_2]
type = INSFVScalarFieldVariable
initial_condition = ${inlet_phase_2}
[]
[interface_area]
type = INSFVScalarFieldVariable
initial_condition = ${inlet_interface_area}
[]
[]
[FVKernels]
[mass]
type = INSFVMassAdvection
variable = pressure
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = ${rho}
[]
[u_advection]
type = INSFVMomentumAdvection
variable = vel_x
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = 'rho_mixture'
momentum_component = 'x'
[]
[u_drift]
type = WCNSFV2PMomentumDriftFlux
variable = vel_x
rho_d = ${rho_d}
fd = 'rho_mixture_var'
u_slip = 'vel_slip_x'
v_slip = 'vel_slip_y'
momentum_component = 'x'
[]
[u_viscosity]
type = INSFVMomentumDiffusion
variable = vel_x
mu = 'mu_mixture'
limit_interpolation = true
momentum_component = 'x'
[]
[u_pressure]
type = INSFVMomentumPressure
variable = vel_x
momentum_component = 'x'
pressure = pressure
[]
[v_advection]
type = INSFVMomentumAdvection
variable = vel_y
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = 'rho_mixture'
momentum_component = 'y'
[]
[v_drift]
type = WCNSFV2PMomentumDriftFlux
variable = vel_y
rho_d = ${rho_d}
fd = 'rho_mixture_var'
u_slip = 'vel_slip_x'
v_slip = 'vel_slip_y'
momentum_component = 'y'
[]
[v_viscosity]
type = INSFVMomentumDiffusion
variable = vel_y
mu = 'mu_mixture'
limit_interpolation = true
momentum_component = 'y'
[]
[v_pressure]
type = INSFVMomentumPressure
variable = vel_y
momentum_component = 'y'
pressure = pressure
[]
[phase_2_advection]
type = INSFVScalarFieldAdvection
variable = phase_2
u_slip = 'vel_x'
v_slip = 'vel_y'
velocity_interp_method = ${velocity_interp_method}
advected_interp_method = 'upwind'
[]
[phase_2_diffusion]
type = FVDiffusion
variable = phase_2
coeff = 1.0
[]
[phase_2_src]
type = NSFVMixturePhaseInterface
variable = phase_2
phase_coupled = phase_1
alpha = ${mass_exchange_coeff}
[]
[interface_area_advection]
type = INSFVScalarFieldAdvection
variable = interface_area
velocity_interp_method = ${velocity_interp_method}
advected_interp_method = 'upwind'
[]
[interface_area_diffusion]
type = FVDiffusion
variable = interface_area
coeff = 0.1
[]
[interface_area_source_sink]
type = WCNSFV2PInterfaceAreaSourceSink
variable = interface_area
u = 'vel_x'
v = 'vel_y'
L = ${fparse l/2}
rho = 'rho_mixture'
rho_d = 'rho'
pressure = 'pressure'
k_c = '${fparse mass_exchange_coeff}'
fd = 'phase_2'
sigma = 1e-3
cutoff_fraction = 0.0
[]
[]
[FVBCs]
[inlet-u]
type = INSFVInletVelocityBC
boundary = 'left'
variable = vel_x
functor = '${U}'
[]
[inlet-v]
type = INSFVInletVelocityBC
boundary = 'left'
variable = vel_y
functor = '0'
[]
[walls-u]
type = INSFVNoSlipWallBC
boundary = 'top'
variable = vel_x
function = 0
[]
[walls-v]
type = INSFVNoSlipWallBC
boundary = 'top'
variable = vel_y
function = 0
[]
[outlet_p]
type = INSFVOutletPressureBC
boundary = 'right'
variable = pressure
function = '${outlet_pressure}'
[]
[inlet_phase_2]
type = FVDirichletBC
boundary = 'left'
variable = phase_2
value = ${inlet_phase_2}
[]
[inlet_interface_area]
type = FVDirichletBC
boundary = 'left'
variable = interface_area
value = ${inlet_interface_area}
[]
[symmetry-u]
type = PINSFVSymmetryVelocityBC
boundary = 'bottom'
variable = vel_x
u = vel_x
v = vel_y
mu = 'mu_mixture'
momentum_component = 'x'
[]
[symmetry-v]
type = PINSFVSymmetryVelocityBC
boundary = 'bottom'
variable = vel_y
u = vel_x
v = vel_y
mu = 'mu_mixture'
momentum_component = 'y'
[]
[symmetry-p]
type = INSFVSymmetryPressureBC
boundary = 'bottom'
variable = pressure
[]
[symmetry-phase-2]
type = INSFVSymmetryScalarBC
boundary = 'bottom'
variable = phase_2
[]
[symmetry-interface-area]
type = INSFVSymmetryScalarBC
boundary = 'bottom'
variable = interface_area
[]
[]
[AuxVariables]
[drag_coefficient]
type = MooseVariableFVReal
[]
[rho_mixture_var]
type = MooseVariableFVReal
[]
[mu_mixture_var]
type = MooseVariableFVReal
[]
[]
[AuxKernels]
[populate_cd]
type = FunctorAux
variable = drag_coefficient
functor = 'Darcy_coefficient'
[]
[populate_rho_mixture_var]
type = FunctorAux
variable = rho_mixture_var
functor = 'rho_mixture'
[]
[populate_mu_mixture_var]
type = FunctorAux
variable = mu_mixture_var
functor = 'mu_mixture'
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[FunctorMaterials]
[bubble_properties]
type = GeneralFunctorFluidProps
fp = 'fp'
pressure = 'pressure'
T_fluid = 300.0
speed = 1.0
characteristic_length = 1.0
porosity = 1.0
output_properties = 'rho'
outputs = 'out'
[]
[populate_u_slip]
type = WCNSFV2PSlipVelocityFunctorMaterial
slip_velocity_name = 'vel_slip_x'
momentum_component = 'x'
u = 'vel_x'
v = 'vel_y'
rho = ${rho}
mu = 'mu_mixture'
rho_d = ${rho_d}
particle_diameter = ${dp}
linear_coef_name = 'Darcy_coefficient'
[]
[populate_v_slip]
type = WCNSFV2PSlipVelocityFunctorMaterial
slip_velocity_name = 'vel_slip_y'
momentum_component = 'y'
u = 'vel_x'
v = 'vel_y'
rho = ${rho}
mu = 'mu_mixture'
rho_d = ${rho_d}
particle_diameter = ${dp}
linear_coef_name = 'Darcy_coefficient'
[]
[compute_phase_1]
type = ADParsedFunctorMaterial
property_name = phase_1
functor_names = 'phase_2'
expression = '1 - phase_2'
[]
[CD]
type = NSFVDispersePhaseDragFunctorMaterial
rho = 'rho_mixture'
mu = mu_mixture
u = 'vel_x'
v = 'vel_y'
particle_diameter = ${dp}
[]
[mixing_material]
type = NSFVMixtureFunctorMaterial
phase_2_names = '${rho} ${mu}'
phase_1_names = 'rho ${mu_d}'
prop_names = 'rho_mixture mu_mixture'
phase_1_fraction = 'phase_2'
[]
[]
[Executioner]
type = Steady
solve_type = 'NEWTON'
nl_rel_tol = 1e-10
line_search = 'none'
[]
[Debug]
show_var_residual_norms = true
[]
[Preconditioning]
[SMP]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_shift_type'
petsc_options_value = 'lu NONZERO'
[]
[]
[Outputs]
[out]
type = Exodus
[]
[]
[Postprocessors]
[Re]
type = ParsedPostprocessor
expression = '${rho} * ${l} * ${U}'
pp_names = ''
[]
[rho_outlet]
type = SideAverageValue
boundary = 'right'
variable = 'rho_mixture_var'
[]
[]
(modules/thermal_hydraulics/test/tests/ics/flow_model_gas_mix_ic/flow_model_gas_mix_ic.i)
mass_fraction = 0.4
pressure = 1e5
temperature = 300
velocity = 10
area = 0.2
[GlobalParams]
fluid_properties = mixture_fp
mass_fraction = mass_frac_fn
pressure = pressure_fn
temperature = temperature_fn
velocity = velocity_fn
area = A
[]
[Mesh]
type = GeneratedMesh
dim = 1
nx = 5
[]
[FluidProperties]
[fp1]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.029
[]
[fp2]
type = IdealGasFluidProperties
gamma = 1.5
molar_mass = 0.04
[]
[mixture_fp]
type = IdealGasMixtureFluidProperties
component_fluid_properties = 'fp1 fp2'
[]
[]
[Functions]
[mass_frac_fn]
type = ConstantFunction
value = ${mass_fraction}
[]
[pressure_fn]
type = ConstantFunction
value = ${pressure}
[]
[temperature_fn]
type = ConstantFunction
value = ${temperature}
[]
[velocity_fn]
type = ConstantFunction
value = ${velocity}
[]
[]
[AuxVariables]
[A]
initial_condition = ${area}
[]
[rho]
[]
[rhoEA]
[]
[]
[ICs]
[rho_ic]
type = FlowModelGasMixIC
variable = rho
quantity = rho
[]
[rhoEA_ic]
type = FlowModelGasMixIC
variable = rhoEA
quantity = rhoEA
[]
[]
[Postprocessors]
[rho]
type = AverageNodalVariableValue
variable = rho
execute_on = 'INITIAL'
[]
[rhoEA]
type = AverageNodalVariableValue
variable = rhoEA
execute_on = 'INITIAL'
[]
[]
[Problem]
solve = false
[]
[Executioner]
type = Steady
[]
[Outputs]
csv = true
execute_on = 'INITIAL'
[]
(modules/thermal_hydraulics/test/tests/components/heat_transfer_from_specified_temperature_1phase/err.no_phf.i)
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[SolidProperties]
[mat]
type = ThermalFunctionSolidProperties
k = 1
cp = 2
rho = 3
[]
[]
[Components]
[fch1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '0 1 0'
length = 1
n_elems = 2
A = 1
closures = simple_closures
fp = fp
f = 0.01
initial_p = 1e5
initial_T = 300
initial_vel = 0
[]
[hs]
type = HeatStructureCylindrical
position = '0 0 0'
orientation = '1 0 0'
length = 1
n_elems = 2
names = 'blk'
widths = '0.1'
n_part_elems = '1'
solid_properties = 'mat'
solid_properties_T_ref = '300'
initial_T = 300
[]
[hx]
type = HeatTransferFromHeatStructure1Phase
hs = hs
hs_side = START
flow_channel = fch1
Hw = 0
[]
[inlet]
type = InletMassFlowRateTemperature1Phase
input = 'fch1:in'
m_dot = 1
T = 300
[]
[outlet]
type = Outlet1Phase
input = 'fch1:out'
p = 1e5
[]
[]
[Preconditioning]
[SMP_PJFNK]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'bdf2'
start_time = 0
dt = 0.1
num_steps = 1
[]
(modules/thermal_hydraulics/test/tests/misc/coupling_mD_flow/thm_non_overlapping.i)
T_in = 523.0
mdot = 10
pout = 7e6
[GlobalParams]
initial_p = ${pout}
initial_vel = 1
initial_T = ${T_in}
gravity_vector = '0 0 0'
closures = simple_closures
n_elems = 5
scaling_factor_1phase = '1 1e-2 1e-5'
f = 1
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.66
molar_mass = 0.004
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[inlet_bc]
type = InletMassFlowRateTemperature1Phase
input = 'inlet:in'
m_dot = ${mdot}
T = ${T_in}
[]
[inlet]
type = FlowChannel1Phase
fp = fp
position = '0 0 11'
orientation = '0 0 -1'
length = 1
A = 1
[]
[inlet_plenum]
type = VolumeJunction1Phase
position = '0 0 10'
initial_vel_x = 0
initial_vel_y = 0
initial_vel_z = 1
connections = 'inlet:out bypass:in core_top:in'
volume = 1
[]
[bypass]
type = FlowChannel1Phase
fp = fp
position = '2 0 10'
orientation = '0 0 -1'
length = 10
A = 0.01
[]
[core_top]
type = FlowChannel1Phase
fp = fp
position = '0 0 10'
orientation = '0 0 -1'
length = 0.1
A = 9
[]
[core_top_bc]
type = Outlet1Phase
p = ${pout}
input = 'core_top:out'
[]
[core_bottom_bc]
type = InletMassFlowRateTemperature1Phase
input = 'core_bottom:in'
m_dot = ${mdot}
T = ${T_in}
[]
[core_bottom]
type = FlowChannel1Phase
fp = fp
position = '0 0 0.1'
orientation = '0 0 -1'
length = 0.1
A = 9
[]
[outlet_plenum]
type = VolumeJunction1Phase
position = '0 0 0'
initial_vel_x = 1
initial_vel_y = 0
initial_vel_z = 1
connections = 'bypass:out core_bottom:out outlet:in'
volume = 1
[]
[outlet]
type = FlowChannel1Phase
fp = fp
position = '0 0 0'
orientation = '0 0 -1'
length = 1
A = 1
[]
[outlet_bc]
type = Outlet1Phase
p = ${pout}
input = 'outlet:out'
[]
[]
[ControlLogic]
[set_core_inlet_pressure]
type = SetComponentRealValueControl
component = core_top_bc
parameter = p
value = core_inlet_pressure
[]
[set_core_outlet_mdot]
type = SetComponentRealValueControl
component = core_bottom_bc
parameter = m_dot
value = core_outlet_mdot
[]
[set_core_outlet_temperature]
type = SetComponentRealValueControl
component = core_bottom_bc
parameter = T
value = core_outlet_temperature
[]
[]
[Postprocessors]
[core_inlet_pressure]
type = Receiver
default = ${pout}
[]
[core_outlet_mdot]
type = Receiver
default = ${mdot}
[]
[core_outlet_temperature]
type = Receiver
default = ${T_in}
[]
[core_outlet_pressure]
type = SideAverageValue
variable = p
boundary = 'core_bottom:in'
execute_on = 'INITIAL LINEAR TIMESTEP_END'
[]
[core_inlet_mdot]
type = SideAverageValue
variable = rhouA
boundary = 'core_top:out'
execute_on = 'INITIAL LINEAR TIMESTEP_END'
[]
[core_inlet_temperature]
type = SideAverageValue
variable = T
boundary = 'core_top:out'
execute_on = 'INITIAL LINEAR TIMESTEP_END'
[]
[bypass_inlet_pressure]
type = SideAverageValue
variable = p
boundary = 'bypass:in'
[]
[bypass_outlet_pressure]
type = SideAverageValue
variable = p
boundary = 'bypass:out'
[]
[bypass_pressure_drop]
type = DifferencePostprocessor
value1 = bypass_inlet_pressure
value2 = bypass_outlet_pressure
[]
[bypass_mdot]
type = SideAverageValue
variable = rhouA
boundary = 'bypass:out'
execute_on = 'INITIAL LINEAR TIMESTEP_END'
[]
[inlet_mdot]
type = SideAverageValue
variable = rhouA
boundary = 'inlet:in'
execute_on = 'INITIAL LINEAR TIMESTEP_END'
[]
[outlet_mdot]
type = SideAverageValue
variable = rhouA
boundary = 'outlet:out'
execute_on = 'INITIAL LINEAR TIMESTEP_END'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
timestep_tolerance = 1e-6
start_time = 0
end_time = 100
dt = 0.01
line_search = l2
nl_rel_tol = 1e-6
nl_abs_tol = 1e-4
nl_max_its = 25
l_tol = 1e-3
l_max_its = 20
petsc_options = '-snes_converged_reason'
petsc_options_iname = '-pc_type'
petsc_options_value = ' lu '
[]
[Outputs]
exodus = true
[]
(modules/thermal_hydraulics/test/tests/postprocessors/heat_rate_convection_1phase/heat_rate_convection_1phase.i)
# Gold value should be the following:
# htc * (T_wall - T) * P_hf * L
T_wall = 350
T = 300
htc = 50
P_hf = 0.3
L = 2.0
[GlobalParams]
gravity_vector = '0 0 0'
closures = simple_closures
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[left_wall]
type = SolidWall1Phase
input = 'pipe:in'
[]
[pipe]
type = FlowChannel1Phase
fp = fp
position = '0 0 0'
orientation = '1 0 0'
length = ${L}
n_elems = 10
A = 1
f = 0.
initial_p = 1e6
initial_T = ${T}
initial_vel = 0
[]
[right_wall]
type = SolidWall1Phase
input = 'pipe:out'
[]
[heat_flux]
type = HeatTransferFromSpecifiedTemperature1Phase
flow_channel = pipe
Hw = ${htc}
T_wall = ${T_wall}
P_hf = ${P_hf}
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
start_time = 0.0
dt = 0.01
num_steps = 0
abort_on_solve_fail = true
solve_type = 'PJFNK'
line_search = 'basic'
nl_rel_tol = 1e-6
nl_abs_tol = 1e-6
nl_max_its = 10
l_tol = 1e-3
l_max_its = 10
[]
[Postprocessors]
[heat_rate]
type = ADHeatRateConvection1Phase
P_hf = P_hf
execute_on = 'INITIAL'
[]
[]
[Outputs]
csv = true
[]
(modules/thermal_hydraulics/test/tests/components/heat_transfer_from_heat_structure_1phase/err.1phase.i)
[GlobalParams]
initial_p = 1e5
initial_vel = 0
initial_T = 300
closures = simple_closures
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[SolidProperties]
[fuel-mat]
type = ThermalFunctionSolidProperties
k = 2.5
cp = 300.
rho = 1.032e4
[]
[]
[Components]
[pipe]
type = FlowChannel1Phase
position = '0 0.1 0'
orientation = '0 0 1'
length = 4
n_elems = 2
A = 8.78882e-5
D_h = 0.01179
f = 0.01
fp = fp
[]
[hs]
type = HeatStructureCylindrical
position = '0 0 0'
orientation = '0 0 1'
length = 4
n_elems = 2
names = 'fuel'
widths = '0.1'
n_part_elems = '1'
solid_properties = 'fuel-mat'
solid_properties_T_ref = '300'
initial_T = 300
[]
[hx]
type = HeatTransferFromHeatStructure1Phase
hs = hs
hs_side = outer
flow_channel = pipe
P_hf = 0.029832559676
[]
[inlet]
type = InletStagnationPressureTemperature1Phase
input = 'pipe:in'
p0 = 1e5
T0 = 300
[]
[outlet]
type = Outlet1Phase
input = 'pipe:out'
p = 1e5
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
dt = 1.e-5
solve_type = 'NEWTON'
num_steps = 1
abort_on_solve_fail = true
[]
(modules/thermal_hydraulics/test/tests/problems/pressure_drop/pressure_drop_with_junction.i)
nelem = 50
friction_factor = 1e4
area = 0.176752
mfr_final = 1.0
p_out = 7e6
T_in = 300
ramp_time = 5.0
[GlobalParams]
gravity_vector = '0 0 0'
initial_T = ${T_in}
initial_p = ${p_out}
initial_vel = 0
closures = closures
rdg_slope_reconstruction = full
scaling_factor_1phase = '1 1 1e-5'
[]
[FluidProperties]
[h2]
type = IdealGasFluidProperties
gamma = 1.3066
molar_mass = 2.016e-3
k = 0.437
mu = 3e-5
[]
[]
[Closures]
[closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[bc_inlet]
type = InletMassFlowRateTemperature1Phase
input = 'ch_1:in'
m_dot = 0 # This value is controlled by 'mfr_ctrl'
T = ${T_in}
[]
[ch_1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = ${nelem}
A = ${area}
f = ${friction_factor}
fp = h2
[]
[junction]
type = JunctionOneToOne1Phase
connections = 'ch_1:out ch_2:in'
[]
[ch_2]
type = FlowChannel1Phase
position = '0.5 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = ${nelem}
A = ${area}
f = ${friction_factor}
fp = h2
[]
[bc_outlet]
type = Outlet1Phase
input = 'ch_2:out'
p = ${p_out}
[]
[]
[Functions]
[mfr_fn]
type = PiecewiseLinear
x = '0 ${ramp_time}'
y = '0 ${mfr_final}'
[]
[]
[ControlLogic]
[mfr_cntrl]
type = TimeFunctionComponentControl
component = bc_inlet
parameter = m_dot
function = mfr_fn
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[VectorPostprocessors]
[pressure_vpp]
type = ADSampler1DReal
block = 'ch_1 ch_2'
property = 'p'
sort_by = x
execute_on = 'FINAL'
[]
[]
[Executioner]
type = Transient
scheme = bdf2
start_time = 0
end_time = 50
dt = 1
steady_state_detection = true
steady_state_start_time = ${ramp_time}
petsc_options_iname = '-pc_type'
petsc_options_value = ' lu '
nl_rel_tol = 1e-6
nl_abs_tol = 1e-6
nl_max_its = 15
l_tol = 1e-4
l_max_its = 10
[]
[Outputs]
[csv]
type = CSV
create_final_symlink = true
execute_on = 'FINAL'
[]
[]
(modules/thermal_hydraulics/tutorials/single_phase_flow/02_core.i)
T_in = 300. # K
m_dot_in = 1e-2 # kg/s
press = 10e5 # Pa
# core parameters
core_length = 1. # m
core_n_elems = 25
core_dia = '${units 2. cm -> m}'
core_pitch = '${units 8.7 cm -> m}'
A_core = '${fparse core_pitch^2 - 0.25 *pi * core_dia^2}'
P_wet_core = '${fparse 4*core_pitch + pi * core_dia}'
Dh_core = '${fparse 4 * A_core / P_wet_core}'
tot_power = 2000 # W
[GlobalParams]
initial_p = ${press}
initial_vel = 0.0001
initial_T = ${T_in}
gravity_vector = '0 0 0'
rdg_slope_reconstruction = minmod
scaling_factor_1phase = '1 1e-2 1e-4'
closures = thm_closures
fp = he
[]
[FluidProperties]
[he]
type = IdealGasFluidProperties
molar_mass = 4e-3
gamma = 1.67
k = 0.2556
mu = 3.22639e-5
[]
[]
[Closures]
[thm_closures]
type = Closures1PhaseTHM
[]
[]
[SolidProperties]
[steel]
type = ThermalFunctionSolidProperties
rho = 8050
k = 45
cp = 466
[]
[]
[Components]
[total_power]
type = TotalPower
power = ${tot_power}
[]
[inlet]
type = InletMassFlowRateTemperature1Phase
input = 'core_chan:in'
m_dot = ${m_dot_in}
T = ${T_in}
[]
[core_chan]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '0 0 1'
length = ${core_length}
n_elems = ${core_n_elems}
roughness = .0001
A = '${A_core}'
D_h = ${Dh_core}
[]
[core_hs]
type = HeatStructureCylindrical
position = '0 0 0'
orientation = '0 0 1'
length = ${core_length}
n_elems = ${core_n_elems}
names = 'block'
widths = '${fparse core_dia / 2.}'
solid_properties = 'steel'
solid_properties_T_ref = '300'
n_part_elems = 3
[]
[core_heating]
type = HeatSourceFromTotalPower
hs = core_hs
regions = block
power = total_power
[]
[core_ht]
type = HeatTransferFromHeatStructure1Phase
flow_channel = core_chan
hs = core_hs
hs_side = outer
P_hf = '${fparse pi * core_dia}'
[]
[outlet]
type = Outlet1Phase
input = 'core_chan:out'
p = ${press}
[]
[]
[Postprocessors]
[power_to_coolant]
type = ADHeatRateConvection1Phase
block = core_chan
P_hf = '${fparse pi *core_dia}'
[]
[core_T_out]
type = SideAverageValue
boundary = core_chan:out
variable = T
[]
[core_p_in]
type = SideAverageValue
boundary = core_chan:in
variable = p
[]
[core_p_out]
type = SideAverageValue
boundary = core_chan:out
variable = p
[]
[core_delta_p]
type = ParsedPostprocessor
pp_names = 'core_p_in core_p_out'
expression = 'core_p_in - core_p_out'
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
start_time = 0
[TimeStepper]
type = IterationAdaptiveDT
dt = 10
[]
end_time = 5000
line_search = basic
solve_type = NEWTON
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_rel_tol = 1e-8
nl_abs_tol = 1e-8
nl_max_its = 25
[]
[Outputs]
exodus = true
[console]
type = Console
max_rows = 1
outlier_variable_norms = false
[]
print_linear_residuals = false
[]
(modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/regular-straight-channel.i)
[GlobalParams]
fp = fp
[]
[Mesh]
[./gen_mesh]
type = GeneratedMeshGenerator
dim = 1
xmax = 1.5
nx = 15
[../]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Variables]
[rho]
type = MooseVariableFVReal
initial_condition = 1.28969
scaling = 1e3
[]
[rho_u]
type = MooseVariableFVReal
initial_condition = 1.28969
[]
[rho_et]
type = MooseVariableFVReal
initial_condition = 2.525e5
scaling = 1e-2
[]
[]
[FVKernels]
[mass_advection]
type = CNSFVMassHLLC
variable = rho
fp = fp
[]
[momentum_x_advection]
type = CNSFVMomentumHLLC
variable = rho_u
momentum_component = x
fp = fp
[]
[drag]
type = FVReaction
variable = rho_u
rate = 1000
[]
[fluid_energy_advection]
type = CNSFVFluidEnergyHLLC
variable = rho_et
fp = fp
[]
[]
[FVBCs]
[mass_in]
variable = rho
type = CNSFVHLLCSpecifiedMassFluxAndTemperatureMassBC
boundary = left
temperature = 273.15
rhou = 1.28969
[]
[momentum_in]
variable = rho_u
type = CNSFVHLLCSpecifiedMassFluxAndTemperatureMomentumBC
boundary = left
temperature = 273.15
rhou = 1.28969
momentum_component = 'x'
[]
[energy_in]
variable = rho_et
type = CNSFVHLLCSpecifiedMassFluxAndTemperatureFluidEnergyBC
boundary = left
temperature = 273.15
rhou = 1.28969
[]
[mass_out]
variable = rho
type = CNSFVHLLCSpecifiedPressureMassBC
boundary = right
pressure = 1.01e5
[]
[momentum_out]
variable = rho_u
type = CNSFVHLLCSpecifiedPressureMomentumBC
boundary = right
pressure = 1.01e5
momentum_component = 'x'
[]
[energy_out]
variable = rho_et
type = CNSFVHLLCSpecifiedPressureFluidEnergyBC
boundary = right
pressure = 1.01e5
[]
[]
[Materials]
[var_mat]
type = ConservedVarValuesMaterial
rho = rho
rhou = rho_u
rho_et = rho_et
[]
[]
[Executioner]
solve_type = NEWTON
type = Steady
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_max_its = 50
line_search = none
[]
[Outputs]
exodus = true
csv = true
[]
[Debug]
show_var_residual_norms = true
[]
(modules/fluid_properties/test/tests/fluid_properties/ideal_gas_mixture/ideal_gas_mixture.i)
[Mesh]
type = GeneratedMesh
dim = 1
nx = 1
[]
[FluidProperties]
[fp1]
type = IdealGasFluidProperties
[]
[fp2]
type = StiffenedGasFluidProperties
gamma = 1.4
cv = 1000
p_inf = 0
q = 0
[]
[fpmix]
type = IdealGasMixtureFluidProperties
component_fluid_properties = 'fp1 fp2'
[]
[]
[Problem]
solve = false
[]
[Executioner]
type = Steady
[]
(modules/navier_stokes/test/tests/finite_volume/cns/straight_channel_porosity_step/rotated-2d-bkt-function-porosity.i)
p_initial=1.01e5
T=273.15
# u refers to the superficial velocity
u_in=1
user_limiter='upwind'
friction_coeff=10
[GlobalParams]
fp = fp
two_term_boundary_expansion = true
limiter = ${user_limiter}
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 2
xmin = 0
xmax = 1
nx = 3
ymin = 0
ymax = 18
ny = 90
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Problem]
fv_bcs_integrity_check = false
[]
[Variables]
[pressure]
type = MooseVariableFVReal
initial_condition = ${p_initial}
[]
[sup_vel_x]
type = MooseVariableFVReal
initial_condition = 1e-15
scaling = 1e-2
[]
[sup_vel_y]
type = MooseVariableFVReal
initial_condition = 1e-15
scaling = 1e-2
[]
[T_fluid]
type = MooseVariableFVReal
initial_condition = ${T}
scaling = 1e-5
[]
[]
[AuxVariables]
[vel_y]
type = MooseVariableFVReal
[]
[sup_mom_y]
type = MooseVariableFVReal
[]
[rho]
type = MooseVariableFVReal
[]
[eps]
type = MooseVariableFVReal
[]
[]
[AuxKernels]
[vel_y]
type = ADMaterialRealAux
variable = vel_y
property = vel_y
execute_on = 'timestep_end'
[]
[sup_mom_y]
type = ADMaterialRealAux
variable = sup_mom_y
property = superficial_rhov
execute_on = 'timestep_end'
[]
[rho]
type = ADMaterialRealAux
variable = rho
property = rho
execute_on = 'timestep_end'
[]
[eps]
type = MaterialRealAux
variable = eps
property = porosity
execute_on = 'timestep_end'
[]
[]
[FVKernels]
[mass_time]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rho_dt'
variable = pressure
[]
[mass_advection]
type = PCNSFVKT
variable = pressure
eqn = "mass"
[]
[momentum_time]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rhou_dt'
variable = sup_vel_x
[]
[momentum_advection]
type = PCNSFVKT
variable = sup_vel_x
eqn = "momentum"
momentum_component = 'x'
[]
[eps_grad]
type = PNSFVPGradEpsilon
variable = sup_vel_x
momentum_component = 'x'
epsilon_function = 'eps'
[]
[drag]
type = PCNSFVMomentumFriction
variable = sup_vel_x
momentum_component = 'x'
Darcy_name = 'cl'
momentum_name = superficial_rhou
[]
[momentum_time_y]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rhov_dt'
variable = sup_vel_y
[]
[momentum_advection_y]
type = PCNSFVKT
variable = sup_vel_y
eqn = "momentum"
momentum_component = 'y'
[]
[eps_grad_y]
type = PNSFVPGradEpsilon
variable = sup_vel_y
momentum_component = 'y'
epsilon_function = 'eps'
[]
[drag_y]
type = PCNSFVMomentumFriction
variable = sup_vel_y
momentum_component = 'y'
Darcy_name = 'cl'
momentum_name = superficial_rhov
[]
[energy_time]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rho_et_dt'
variable = T_fluid
[]
[energy_advection]
type = PCNSFVKT
variable = T_fluid
eqn = "energy"
[]
[]
[FVBCs]
[rho_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = pressure
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'mass'
[]
[rhou_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = sup_vel_x
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'momentum'
momentum_component = 'x'
[]
[rhov_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = sup_vel_y
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'momentum'
momentum_component = 'y'
[]
[rho_et_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = T_fluid
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'energy'
[]
[rho_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = pressure
pressure = ${p_initial}
eqn = 'mass'
[]
[rhou_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = sup_vel_x
pressure = ${p_initial}
eqn = 'momentum'
momentum_component = 'x'
[]
[rhov_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = sup_vel_y
pressure = ${p_initial}
eqn = 'momentum'
momentum_component = 'y'
[]
[rho_et_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = T_fluid
pressure = ${p_initial}
eqn = 'energy'
[]
[wall_pressure_x]
type = PCNSFVImplicitMomentumPressureBC
momentum_component = 'x'
boundary = 'left right'
variable = sup_vel_x
[]
[wall_pressure_y]
type = PCNSFVImplicitMomentumPressureBC
momentum_component = 'y'
boundary = 'left right'
variable = sup_vel_y
[]
# Use these to help create more accurate cell centered gradients for cells adjacent to boundaries
[T_bottom]
type = FVDirichletBC
variable = T_fluid
value = ${T}
boundary = 'bottom'
[]
[sup_vel_x_bottom_and_walls]
type = FVDirichletBC
variable = sup_vel_x
value = 0
boundary = 'bottom left right'
[]
[sup_vel_y_walls]
type = FVDirichletBC
variable = sup_vel_y
value = 0
boundary = 'left right'
[]
[sup_vel_y_bottom]
type = FVDirichletBC
variable = sup_vel_y
value = ${u_in}
boundary = 'bottom'
[]
[p_top]
type = FVDirichletBC
variable = pressure
value = ${p_initial}
boundary = 'top'
[]
[]
[Functions]
[ud_in]
type = ParsedVectorFunction
expression_x = '0'
expression_y = '${u_in}'
[]
[eps]
type = ParsedFunction
expression = 'if(y < 2.8, 1,
if(y < 3.2, 1 - .5 / .4 * (y - 2.8),
if(y < 6.8, .5,
if(y < 7.2, .5 - .25 / .4 * (y - 6.8),
if(y < 10.8, .25,
if(y < 11.2, .25 + .25 / .4 * (y - 10.8),
if(y < 14.8, .5,
if(y < 15.2, .5 + .5 / .4 * (y - 14.8),
1))))))))'
[]
[]
[Materials]
[var_mat]
type = PorousPrimitiveVarMaterial
pressure = pressure
T_fluid = T_fluid
superficial_vel_x = sup_vel_x
superficial_vel_y = sup_vel_y
fp = fp
porosity = porosity
[]
[porosity]
type = GenericFunctionMaterial
prop_names = 'porosity'
prop_values = 'eps'
[]
[ad_generic]
type = ADGenericConstantVectorMaterial
prop_names = 'cl'
prop_values = '${friction_coeff} ${friction_coeff} ${friction_coeff}'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
solve_type = NEWTON
line_search = 'bt'
type = Transient
nl_max_its = 20
[TimeStepper]
type = IterationAdaptiveDT
dt = 5e-5
optimal_iterations = 6
growth_factor = 1.2
[]
num_steps = 10000
end_time = 500
nl_abs_tol = 1e-7
petsc_options_iname = '-pc_type -pc_factor_mat_solver_type'
petsc_options_value = 'lu mumps'
[]
[Outputs]
[out]
type = Exodus
execute_on = 'final'
[]
checkpoint = true
[]
[Debug]
show_var_residual_norms = true
[]
(modules/navier_stokes/test/tests/finite_volume/two_phase/mixture_interface_area_model/pressure_driven_growth_transient.i)
###############################################################################
# Validation test based on Hibiki and Ishii experiment [1] reported in Figure 3
# [1] Hibiki, T., & Ishii, M. (2000). One-group interfacial area transport of bubbly flows in vertical round tubes.
# International Journal of Heat and Mass Transfer, 43(15), 2711-2726.
###############################################################################
mu = 1.0
rho = 1000.0
mu_d = 1.0
rho_d = 1.0
l = ${fparse 50.8/1000.0}
U = 0.491230114
dp = 0.001
inlet_phase_2 = 0.049
advected_interp_method = 'upwind'
velocity_interp_method = 'rc'
mass_exchange_coeff = 0.0
inlet_interface_area = ${fparse 6.0*inlet_phase_2/dp}
outlet_pressure = 1e6
[GlobalParams]
rhie_chow_user_object = 'rc'
density_interp_method = 'average'
mu_interp_method = 'average'
[]
[Problem]
identify_variable_groups_in_nl = false
[]
[UserObjects]
[rc]
type = INSFVRhieChowInterpolator
u = vel_x
v = vel_y
pressure = pressure
[]
[]
[Mesh]
coord_type = 'RZ'
rz_coord_axis = 'X'
[gen]
type = GeneratedMeshGenerator
dim = 2
xmin = 0
xmax = '${fparse l * 60}'
ymin = 0
ymax = '${fparse l / 2}'
nx = 20
ny = 5
[]
uniform_refine = 0
[]
[Variables]
[vel_x]
type = INSFVVelocityVariable
initial_condition = 0
[]
[vel_y]
type = INSFVVelocityVariable
initial_condition = 0
[]
[pressure]
type = INSFVPressureVariable
[]
[phase_2]
type = INSFVScalarFieldVariable
initial_condition = ${inlet_phase_2}
[]
[interface_area]
type = INSFVScalarFieldVariable
initial_condition = ${inlet_interface_area}
[]
[]
[FVKernels]
[mass]
type = INSFVMassAdvection
variable = pressure
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = ${rho}
[]
[u_time]
type = INSFVMomentumTimeDerivative
variable = vel_x
rho = 'rho_mixture'
momentum_component = 'x'
[]
[u_advection]
type = INSFVMomentumAdvection
variable = vel_x
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = 'rho_mixture'
momentum_component = 'x'
[]
[u_drift]
type = WCNSFV2PMomentumDriftFlux
variable = vel_x
rho_d = ${rho_d}
fd = 'rho_mixture_var'
u_slip = 'vel_slip_x'
v_slip = 'vel_slip_y'
momentum_component = 'x'
[]
[u_viscosity]
type = INSFVMomentumDiffusion
variable = vel_x
mu = 'mu_mixture'
limit_interpolation = true
momentum_component = 'x'
[]
[u_pressure]
type = INSFVMomentumPressure
variable = vel_x
momentum_component = 'x'
pressure = pressure
[]
[v_time]
type = INSFVMomentumTimeDerivative
variable = vel_y
rho = 'rho_mixture'
momentum_component = 'y'
[]
[v_advection]
type = INSFVMomentumAdvection
variable = vel_y
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = 'rho_mixture'
momentum_component = 'y'
[]
[v_drift]
type = WCNSFV2PMomentumDriftFlux
variable = vel_y
rho_d = ${rho_d}
fd = 'rho_mixture_var'
u_slip = 'vel_slip_x'
v_slip = 'vel_slip_y'
momentum_component = 'y'
[]
[v_viscosity]
type = INSFVMomentumDiffusion
variable = vel_y
mu = 'mu_mixture'
limit_interpolation = true
momentum_component = 'y'
[]
[v_pressure]
type = INSFVMomentumPressure
variable = vel_y
momentum_component = 'y'
pressure = pressure
[]
[phase_2_time]
type = FVFunctorTimeKernel
variable = phase_2
functor = phase_2
[]
[phase_2_advection]
type = INSFVScalarFieldAdvection
variable = phase_2
u_slip = 'vel_x'
v_slip = 'vel_y'
velocity_interp_method = ${velocity_interp_method}
advected_interp_method = 'upwind'
[]
[phase_2_diffusion]
type = FVDiffusion
variable = phase_2
coeff = 1.0
[]
[phase_2_src]
type = NSFVMixturePhaseInterface
variable = phase_2
phase_coupled = phase_1
alpha = ${mass_exchange_coeff}
[]
[interface_area_time]
type = FVFunctorTimeKernel
variable = interface_area
functor = interface_area
[]
[interface_area_advection]
type = INSFVScalarFieldAdvection
variable = interface_area
velocity_interp_method = ${velocity_interp_method}
advected_interp_method = 'upwind'
[]
[interface_area_diffusion]
type = FVDiffusion
variable = interface_area
coeff = 0.1
[]
[interface_area_source_sink]
type = WCNSFV2PInterfaceAreaSourceSink
variable = interface_area
u = 'vel_x'
v = 'vel_y'
L = ${fparse l/2}
rho = 'rho_mixture'
rho_d = 'rho'
pressure = 'pressure'
k_c = '${fparse mass_exchange_coeff}'
fd = 'phase_2'
sigma = 1e-3
cutoff_fraction = 0.0
[]
[]
[FVBCs]
[inlet-u]
type = INSFVInletVelocityBC
boundary = 'left'
variable = vel_x
functor = '${U}'
[]
[inlet-v]
type = INSFVInletVelocityBC
boundary = 'left'
variable = vel_y
functor = '0'
[]
[walls-u]
type = INSFVNoSlipWallBC
boundary = 'top'
variable = vel_x
function = 0
[]
[walls-v]
type = INSFVNoSlipWallBC
boundary = 'top'
variable = vel_y
function = 0
[]
[outlet_p]
type = INSFVOutletPressureBC
boundary = 'right'
variable = pressure
function = '${outlet_pressure}'
[]
[inlet_phase_2]
type = FVDirichletBC
boundary = 'left'
variable = phase_2
value = ${inlet_phase_2}
[]
[inlet_interface_area]
type = FVDirichletBC
boundary = 'left'
variable = interface_area
value = ${inlet_interface_area}
[]
[symmetry-u]
type = PINSFVSymmetryVelocityBC
boundary = 'bottom'
variable = vel_x
u = vel_x
v = vel_y
mu = 'mu_mixture'
momentum_component = 'x'
[]
[symmetry-v]
type = PINSFVSymmetryVelocityBC
boundary = 'bottom'
variable = vel_y
u = vel_x
v = vel_y
mu = 'mu_mixture'
momentum_component = 'y'
[]
[symmetry-p]
type = INSFVSymmetryPressureBC
boundary = 'bottom'
variable = pressure
[]
[symmetry-phase-2]
type = INSFVSymmetryScalarBC
boundary = 'bottom'
variable = phase_2
[]
[symmetry-interface-area]
type = INSFVSymmetryScalarBC
boundary = 'bottom'
variable = interface_area
[]
[]
[AuxVariables]
[drag_coefficient]
type = MooseVariableFVReal
[]
[rho_mixture_var]
type = MooseVariableFVReal
[]
[mu_mixture_var]
type = MooseVariableFVReal
[]
[]
[AuxKernels]
[populate_cd]
type = FunctorAux
variable = drag_coefficient
functor = 'Darcy_coefficient'
[]
[populate_rho_mixture_var]
type = FunctorAux
variable = rho_mixture_var
functor = 'rho_mixture'
[]
[populate_mu_mixture_var]
type = FunctorAux
variable = mu_mixture_var
functor = 'mu_mixture'
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[FunctorMaterials]
[bubble_properties]
type = GeneralFunctorFluidProps
fp = 'fp'
pressure = 'pressure'
T_fluid = 300.0
speed = 1.0
characteristic_length = 1.0
porosity = 1.0
output_properties = 'rho'
outputs = 'out'
[]
[populate_u_slip]
type = WCNSFV2PSlipVelocityFunctorMaterial
slip_velocity_name = 'vel_slip_x'
momentum_component = 'x'
u = 'vel_x'
v = 'vel_y'
rho = ${rho}
mu = 'mu_mixture'
rho_d = ${rho_d}
particle_diameter = ${dp}
linear_coef_name = 'Darcy_coefficient'
[]
[populate_v_slip]
type = WCNSFV2PSlipVelocityFunctorMaterial
slip_velocity_name = 'vel_slip_y'
momentum_component = 'y'
u = 'vel_x'
v = 'vel_y'
rho = ${rho}
mu = 'mu_mixture'
rho_d = ${rho_d}
particle_diameter = ${dp}
linear_coef_name = 'Darcy_coefficient'
[]
[compute_phase_1]
type = ADParsedFunctorMaterial
property_name = phase_1
functor_names = 'phase_2'
expression = '1 - phase_2'
[]
[CD]
type = NSFVDispersePhaseDragFunctorMaterial
rho = 'rho_mixture'
mu = mu_mixture
u = 'vel_x'
v = 'vel_y'
particle_diameter = ${dp}
[]
[mixing_material]
type = NSFVMixtureFunctorMaterial
phase_2_names = '${rho} ${mu}'
phase_1_names = 'rho ${mu_d}'
prop_names = 'rho_mixture mu_mixture'
phase_1_fraction = 'phase_2'
[]
[]
[Executioner]
type = Transient
solve_type = 'NEWTON'
nl_abs_tol = 1e-7
dt = 0.1
end_time = 1.0
nl_max_its = 10
line_search = 'none'
[]
[Debug]
show_var_residual_norms = true
[]
[Preconditioning]
[SMP]
type = SMP
full = true
petsc_options_iname = '-pc_type -pc_factor_shift_type'
petsc_options_value = 'lu NONZERO'
[]
[]
[Outputs]
[out]
type = Exodus
[]
[]
[Postprocessors]
[Re]
type = ParsedPostprocessor
expression = '${rho} * ${l} * ${U}'
pp_names = ''
[]
[rho_outlet]
type = SideAverageValue
boundary = 'right'
variable = 'rho_mixture_var'
[]
[]
(modules/thermal_hydraulics/test/tests/components/heat_transfer_from_heat_structure_1phase/jac.1phase.i)
[GlobalParams]
initial_p = 1.e5
initial_vel = 2
initial_T = 300
scaling_factor_1phase = '1 1 1'
scaling_factor_temperature = '1'
closures = simple_closures
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[SolidProperties]
[fuel-mat]
type = ThermalFunctionSolidProperties
k = 2.5
cp = 300.
rho = 1.032e4
[]
[]
[Components]
[pipe]
type = FlowChannel1Phase
position = '0 0.1 0'
orientation = '0 0 1'
length = 2
n_elems = 1
A = 8.78882e-5
D_h = 0.01179
f = 0.01
fp = fp
[]
[hs]
type = HeatStructureCylindrical
position = '0 0 0'
orientation = '0 0 1'
length = 2
n_elems = 1
names = 'fuel'
widths = '0.1'
n_part_elems = '1'
solid_properties = 'fuel-mat'
solid_properties_T_ref = '300'
initial_T = 300
[]
[hx]
type = HeatTransferFromHeatStructure1Phase
hs = hs
hs_side = outer
flow_channel = pipe
Hw = 100
P_hf = 0.029832559676
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
start_time = 0
dt = 1
num_steps = 1
abort_on_solve_fail = true
solve_type = 'NEWTON'
petsc_options_iname = '-snes_test_err'
petsc_options_value = ' 1e-11'
[]
(modules/navier_stokes/test/tests/ics/test.i)
p_initial=1.01e5
T=273.15
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 2
xmin = 0
xmax = 1
ymin = 1
ymax = 2
nx = 4
ny = 4
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Problem]
kernel_coverage_check = false
solve = false
skip_nl_system_check = true
[]
[AuxVariables]
[pressure]
type = MooseVariableFVReal
[]
[vel_x]
type = MooseVariableFVReal
[]
[vel_y]
type = MooseVariableFVReal
[]
[vel_z]
type = MooseVariableFVReal
[]
[temperature]
type = MooseVariableFVReal
[]
[ht]
type = MooseVariableFVReal
[]
[e]
type = MooseVariableFVReal
[]
[Mach]
type = MooseVariableFVReal
[]
[rho]
type = MooseVariableFVReal
[]
[rhou]
type = MooseVariableFVReal
[]
[rhov]
type = MooseVariableFVReal
[]
[rhow]
type = MooseVariableFVReal
[]
[rho_et]
type = MooseVariableFVReal
[]
[specific_volume]
type = MooseVariableFVReal
[]
[pressure_2]
[]
[vel_x_2]
[]
[vel_y_2]
[]
[vel_z_2]
[]
[temperature_2]
[]
[ht_2]
[]
[e_2]
[]
[Mach_2]
[]
[rho_2]
[]
[rhou_2]
[]
[rhov_2]
[]
[rhow_2]
[]
[rho_et_2]
[]
[specific_volume_2]
[]
[]
[GlobalParams]
fluid_properties = 'fp'
initial_pressure = ${p_initial}
initial_temperature = ${T}
initial_velocity = '1 0.2 18'
[]
[ICs]
[p]
type = NSInitialCondition
variable = 'pressure'
[]
[vel_x]
type = NSInitialCondition
variable = 'vel_x'
[]
[vel_y]
type = NSInitialCondition
variable = 'vel_y'
[]
[vel_z]
type = NSInitialCondition
variable = 'vel_z'
[]
[temperature]
type = NSInitialCondition
variable = 'temperature'
[]
[ht]
type = NSInitialCondition
variable = 'ht'
[]
[e]
type = NSInitialCondition
variable = 'e'
[]
[Mach]
type = NSInitialCondition
variable = 'Mach'
[]
[rho]
type = NSInitialCondition
fluid_properties = 'fp'
initial_pressure = ${p_initial}
initial_temperature = ${T}
initial_velocity = '1 0.2 18'
variable = 'rho'
[]
[rhou]
type = NSInitialCondition
variable = 'rhou'
[]
[rhov]
type = NSInitialCondition
variable = 'rhov'
[]
[rhow]
type = NSInitialCondition
variable = 'rhow'
[]
[rho_et]
type = NSInitialCondition
variable = 'rho_et'
[]
[specific_volume]
type = NSInitialCondition
variable = 'specific_volume'
[]
[p_2]
type = NSInitialCondition
variable = 'pressure_2'
variable_type = 'pressure'
[]
[vel_x_2]
type = NSInitialCondition
variable = 'vel_x_2'
variable_type = 'vel_x'
[]
[vel_y_2]
type = NSInitialCondition
variable = 'vel_y_2'
variable_type = 'vel_y'
[]
[vel_z_2]
type = NSInitialCondition
variable = 'vel_z_2'
variable_type = 'vel_z'
[]
[temperature_2]
type = NSInitialCondition
variable = 'temperature_2'
variable_type = 'temperature'
[]
[ht_2]
type = NSInitialCondition
variable = 'ht_2'
variable_type = 'ht'
[]
[e_2]
type = NSInitialCondition
variable = 'e_2'
variable_type = 'e'
[]
[Mach_2]
type = NSInitialCondition
variable = 'Mach_2'
variable_type = 'Mach'
[]
[rho_2]
type = NSInitialCondition
variable = 'rho_2'
variable_type = 'rho'
[]
[rhou_2]
type = NSInitialCondition
variable = 'rhou_2'
variable_type = 'rhou'
[]
[rhov_2]
type = NSInitialCondition
variable = 'rhov_2'
variable_type = 'rhov'
[]
[rhow_2]
type = NSInitialCondition
variable = 'rhow_2'
variable_type = 'rhow'
[]
[rho_et_2]
type = NSInitialCondition
variable = 'rho_et_2'
variable_type = 'rho_et'
[]
[specific_volume_2]
type = NSInitialCondition
variable = 'specific_volume_2'
variable_type = 'specific_volume'
[]
[]
[Executioner]
type = Steady
[]
[Outputs]
exodus = true
[]
(modules/thermal_hydraulics/test/tests/problems/lax_shock_tube/lax_shock_tube.i)
# This test problem is the Lax shock tube test problem,
# which is a Riemann problem with the following parameters:
# * domain = (0,1)
# * gravity = 0
# * EoS: Ideal gas EoS with gamma = 1.4, R = 0.71428571428571428571
# * interface: x = 0.5
# * typical end time: 0.15
# Left initial values:
# * rho = 0.445
# * vel = 0.692
# * p = 3.52874226
# Right initial values:
# * rho = 0.5
# * vel = 0
# * p = 0.571
[GlobalParams]
gravity_vector = '0 0 0'
rdg_slope_reconstruction = minmod
closures = simple_closures
[]
[Functions]
[p_ic_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.5 1.0'
y = '3.52874226 0.571'
[]
[T_ic_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.5 1.0'
y = '11.1016610426966 1.5988'
[]
[vel_ic_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.5 1.0'
y = '0.692 0.0'
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 11.64024372
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[pipe]
type = FlowChannel1Phase
fp = fp
# geometry
position = '0 0 0'
orientation = '1 0 0'
length = 1.0
n_elems = 100
A = 1.0
# IC
initial_T = T_ic_fn
initial_p = p_ic_fn
initial_vel = vel_ic_fn
f = 0
[]
[left_boundary]
type = FreeBoundary1Phase
input = 'pipe:in'
[]
[right_boundary]
type = FreeBoundary1Phase
input = 'pipe:out'
[]
[]
[Executioner]
type = Transient
[TimeIntegrator]
type = ExplicitSSPRungeKutta
# add order via 'cli_args' in 'tests'
[]
solve_type = LINEAR
l_tol = 1e-4
nl_rel_tol = 1e-8
nl_abs_tol = 1e-8
nl_max_its = 60
# run to t = 0.15
start_time = 0.0
dt = 1e-3
num_steps = 150
abort_on_solve_fail = true
[]
[Outputs]
file_base = 'lax_shock_tube'
velocity_as_vector = false
execute_on = 'initial timestep_end'
[out]
type = Exodus
show = 'rho p vel'
[]
[]
(modules/thermal_hydraulics/test/tests/postprocessors/flow_junction_flux_1phase/flow_junction_flux_1phase.i)
# This input file tests mass conservation at steady-state by looking at the
# net mass flux into the domain.
T_in = 523.0
m_dot = 100
p_out = 7e6
[GlobalParams]
initial_p = ${p_out}
initial_vel = 1
initial_T = ${T_in}
gravity_vector = '0 0 0'
closures = simple_closures
n_elems = 3
f = 0
scaling_factor_1phase = '1 1 1e-5'
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[inlet_bc]
type = InletMassFlowRateTemperature1Phase
input = 'inlet:in'
m_dot = ${m_dot}
T = ${T_in}
[]
[inlet]
type = FlowChannel1Phase
fp = fp
position = '0 0 11'
orientation = '0 0 -1'
length = 1
A = 3
[]
[inlet_plenum]
type = VolumeJunction1Phase
position = '0 0 10'
initial_vel_x = 0
initial_vel_y = 0
initial_vel_z = 1
connections = 'inlet:out channel1:in channel2:in'
volume = 1
scaling_factor_rhoEV = '1e-5'
[]
[channel1]
type = FlowChannel1Phase
fp = fp
position = '0 0 10'
orientation = '0 0 -1'
length = 10
A = 4
D_h = 1
[]
[K_bypass]
type = FormLossFromFunction1Phase
K_prime = 500
flow_channel = channel1
[]
[channel2]
type = FlowChannel1Phase
fp = fp
position = '0 0 10'
orientation = '0 0 -1'
length = 10
A = 1
D_h = 1
[]
[outlet_plenum]
type = VolumeJunction1Phase
position = '0 0 0'
initial_vel_x = 1
initial_vel_y = 0
initial_vel_z = 1
connections = 'channel1:out channel2:out outlet:in'
volume = 1
scaling_factor_rhoEV = '1e-5'
[]
[outlet]
type = FlowChannel1Phase
fp = fp
position = '0 0 0'
orientation = '0 0 -1'
length = 1
A = 1
[]
[outlet_bc]
type = Outlet1Phase
p = ${p_out}
input = 'outlet:out'
[]
[]
[Postprocessors]
[inlet_in_m_dot]
type = ADFlowBoundaryFlux1Phase
boundary = 'inlet_bc'
equation = mass
[]
[inlet_out_m_dot]
type = ADFlowJunctionFlux1Phase
boundary = 'inlet:out'
connection_index = 0
junction = inlet_plenum
equation = mass
[]
[channel1_in_m_dot]
type = ADFlowJunctionFlux1Phase
boundary = 'channel1:in'
connection_index = 1
junction = inlet_plenum
equation = mass
[]
[channel1_out_m_dot]
type = ADFlowJunctionFlux1Phase
boundary = 'channel1:out'
connection_index = 0
junction = outlet_plenum
equation = mass
[]
[channel2_in_m_dot]
type = ADFlowJunctionFlux1Phase
boundary = 'channel2:in'
connection_index = 2
junction = inlet_plenum
equation = mass
[]
[channel2_out_m_dot]
type = ADFlowJunctionFlux1Phase
boundary = 'channel2:out'
connection_index = 1
junction = outlet_plenum
equation = mass
[]
[outlet_in_m_dot]
type = ADFlowJunctionFlux1Phase
boundary = 'outlet:in'
connection_index = 2
junction = outlet_plenum
equation = mass
[]
[outlet_out_m_dot]
type = ADFlowBoundaryFlux1Phase
boundary = 'outlet_bc'
equation = mass
[]
[net_mass_flow_rate_domain]
type = LinearCombinationPostprocessor
pp_names = 'inlet_in_m_dot outlet_out_m_dot'
pp_coefs = '1 -1'
[]
[net_mass_flow_rate_volume_junction]
type = LinearCombinationPostprocessor
pp_names = 'inlet_out_m_dot channel1_in_m_dot channel2_in_m_dot'
pp_coefs = '1 -1 -1'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
start_time = 0
end_time = 10000
[TimeStepper]
type = IterationAdaptiveDT
dt = 0.01
optimal_iterations = 8
iteration_window = 2
[]
timestep_tolerance = 1e-6
abort_on_solve_fail = true
line_search = none
nl_rel_tol = 1e-8
nl_abs_tol = 2e-8
nl_max_its = 25
l_tol = 1e-3
l_max_its = 5
petsc_options = '-snes_converged_reason'
petsc_options_iname = '-pc_type'
petsc_options_value = ' lu '
[]
[Outputs]
[out]
type = CSV
execute_on = 'FINAL'
show = 'net_mass_flow_rate_domain net_mass_flow_rate_volume_junction'
[]
[]
(modules/thermal_hydraulics/test/tests/components/deprecated/junction_one_to_one.i)
[GlobalParams]
gravity_vector = '0 0 0'
closures = simple_closures
fp = fp
f = 0.0
initial_T = 300
initial_p = 1e5
initial_vel = 0
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02897
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[inlet]
type = InletMassFlowRateTemperature1Phase
input = 'pipe1:in'
m_dot = 1
T = 300
[]
[pipe1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = 2
A = 0.1
[]
[valve]
type = JunctionOneToOne
connections = 'pipe1:out pipe2:in'
[]
[pipe2]
type = FlowChannel1Phase
position = '0.5 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = 2
A = 0.1
[]
[outlet]
type = Outlet1Phase
input = 'pipe2:out'
p = 1e5
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
solve_type = NEWTON
nl_rel_tol = 1e-8
nl_abs_tol = 1e-8
nl_max_its = 20
l_tol = 1e-4
start_time = 0.0
end_time = 1.0
dt = 0.01
abort_on_solve_fail = true
[]
(modules/thermal_hydraulics/test/tests/components/supersonic_inlet/err.i)
[GlobalParams]
gravity_vector = '0 0 0'
closures = simple_closures
fp = fp
f = 0.0
initial_T = 300
initial_p = 1e5
initial_vel = 0
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02897
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[in]
type = SupersonicInlet
input = 'pipe:in'
vel = 500
T = 300
p = 1e5
[]
[pipe]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = 2
A = 0.1
[]
[out]
type = Outlet1Phase
input = 'pipe:out'
p = 1e5
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
solve_type = NEWTON
nl_rel_tol = 1e-8
nl_abs_tol = 1e-8
nl_max_its = 20
l_tol = 1e-4
start_time = 0.0
end_time = 1.0
dt = 0.01
abort_on_solve_fail = true
[]
(modules/thermal_hydraulics/test/tests/problems/woodward_colella_blast_wave/woodward_colella_blast_wave.i)
# Woodward-Colella blast wave problem
[GlobalParams]
gravity_vector = '0 0 0'
closures = simple_closures
[]
[Functions]
[p_ic_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.1 0.9 1.0'
y = '1000 0.01 100'
[]
[T_ic_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.1 0.9 1.0'
y = '1400 0.014 140'
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 11.64024372
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[pipe]
type = FlowChannel1Phase
fp = fp
# geometry
position = '0 0 0'
orientation = '1 0 0'
length = 1.0
n_elems = 500
A = 1.0
# IC
initial_T = T_ic_fn
initial_p = p_ic_fn
initial_vel = 0
f = 0
[]
[left_wall]
type = SolidWall1Phase
input = 'pipe:in'
[]
[right_wall]
type = SolidWall1Phase
input = 'pipe:out'
[]
[]
[Executioner]
type = Transient
[TimeIntegrator]
type = ExplicitSSPRungeKutta
order = 2
[]
solve_type = LINEAR
l_tol = 1e-4
nl_rel_tol = 1e-20
nl_abs_tol = 1e-8
nl_max_its = 60
# run to t = 0.038
start_time = 0.0
dt = 1e-5
num_steps = 3800
abort_on_solve_fail = true
[]
[Outputs]
file_base = 'woodward_colella_blast_wave'
velocity_as_vector = false
execute_on = 'initial timestep_end'
[out]
type = Exodus
show = 'p T vel'
[]
[]
(modules/thermal_hydraulics/test/tests/closures/wall_temperature_1phase/base.i)
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Closures]
[wall_temp_closures]
type = WallTemperature1PhaseClosures
[]
[]
[Components]
[pipe]
type = FlowChannel1Phase
gravity_vector = '0 0 0'
position = '0 0 0'
orientation = '1 0 0'
A = 1e-4
length = 1
n_elems = 10
initial_vel = 0
initial_p = 1e5
initial_T = 300
fp = fp
closures = wall_temp_closures
[]
[inlet]
type = SolidWall1Phase
input = 'pipe:in'
[]
[outlet]
type = SolidWall1Phase
input = 'pipe:out'
[]
[ht]
type = HeatTransferFromSpecifiedTemperature1Phase
flow_channel = pipe
T_wall = 500
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Postprocessors]
[T_wall]
type = ADElementAverageMaterialProperty
mat_prop = T_wall
execute_on = 'INITIAL'
[]
[]
[Executioner]
type = Transient
scheme = 'bdf2'
start_time = 0
num_steps = 0
dt = 1e-6
solve_type = NEWTON
nl_rel_tol = 1e-8
nl_abs_tol = 1e-8
nl_max_its = 5
l_tol = 1e-3
l_max_its = 10
[]
[Outputs]
csv = true
execute_on = 'INITIAL'
[]
(modules/thermal_hydraulics/test/tests/components/deprecated/free_boundary.i)
[GlobalParams]
gravity_vector = '0 0 0'
closures = simple_closures
fp = fp
f = 0.0
initial_T = 300
initial_p = 1e5
initial_vel = 0
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02897
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[in]
type = FreeBoundary
input = 'pipe:in'
[]
[pipe]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = 2
A = 0.1
[]
[out]
type = FreeBoundary
input = 'pipe:out'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
solve_type = NEWTON
nl_rel_tol = 1e-8
nl_abs_tol = 1e-8
nl_max_its = 20
l_tol = 1e-4
start_time = 0.0
end_time = 1.0
dt = 0.01
abort_on_solve_fail = true
[]
(modules/navier_stokes/test/tests/finite_volume/wcns/natural_convection/natural_circulation_pipe.i)
# natural convection through a pipe
# Reference solution in "reference_pipe_natural_convection.py"
# Reference mdot: 0.0792 kg/s
# this input
# iy mdot
# 10 8.302364e-02
# 20 8.111192e-02
# 40 8.007924e-02
# 80 7.954403e-02
# 160 7.927201e-02
# Convergence to the analytical result is observed
height = 10.0
gravity = 9.81
p0 = 1e5
molar_mass = 29.0e-3
T0 = 328
Ru = 8.3145
Ri = '${fparse Ru / molar_mass}'
density = '${fparse p0 / (Ri * T0)}'
head = '${fparse height * density * gravity}'
k = 25.68e-3
gamma = 1.4
[Mesh]
[mesh]
type = CartesianMeshGenerator
dim = 2
dx = '0.1'
ix = '2'
dy = '${height}'
iy = '5'
[]
[]
[GlobalParams]
rhie_chow_user_object = pins_rhie_chow_interpolator
[]
[FluidProperties]
[air]
type = IdealGasFluidProperties
molar_mass = ${molar_mass}
k = ${k}
gamma = ${gamma}
[]
[]
[Modules]
[NavierStokesFV]
compressibility = 'weakly-compressible'
add_energy_equation = true
gravity = '0 -${gravity} 0'
density = rho
dynamic_viscosity = mu
specific_heat = cp
thermal_conductivity = k
initial_velocity = '0 1e-6 0'
initial_pressure = ${p0}
initial_temperature = ${T0}
inlet_boundaries = 'bottom'
momentum_inlet_types = 'fixed-pressure'
momentum_inlet_functors = '${fparse p0 + head}'
energy_inlet_types = 'fixed-temperature'
energy_inlet_functors = '${T0}'
energy_scaling = 1e-5
wall_boundaries = 'left right'
momentum_wall_types = 'slip slip'
energy_wall_types = 'heatflux heatflux'
energy_wall_functors = '300 300'
outlet_boundaries = 'top'
momentum_outlet_types = 'fixed-pressure'
pressure_functors = '${fparse p0}'
momentum_advection_interpolation = 'upwind'
mass_advection_interpolation = 'upwind'
porous_medium_treatment = true
porosity = porosity
energy_advection_interpolation = 'average'
[]
[]
[FVKernels]
[u_friction]
type = PINSFVMomentumFriction
variable = superficial_vel_x
Darcy_name = linear_friction_coeff
momentum_component = 'x'
standard_friction_formulation = false
rho = rho
[]
[v_friction]
type = PINSFVMomentumFriction
variable = superficial_vel_y
Darcy_name = linear_friction_coeff
momentum_component = 'y'
standard_friction_formulation = false
rho = rho
[]
[]
[Executioner]
type = Transient
solve_type = 'NEWTON'
petsc_options_iname = '-pc_type -sub_pc_factor_shift_type'
petsc_options_value = 'lu NONZERO'
nl_rel_tol = 1e-8
nl_abs_tol = 1e-6
end_time = 1e4
[TimeStepper]
type = IterationAdaptiveDT
dt = 0.1
growth_factor = 2
iteration_window = 2
optimal_iterations = 6
[]
[]
[Functions]
[mu_rampdown_fn]
type = PiecewiseLinear
x = '0 0.5 1 5 10 100 1000 2000'
y = '1000 1000 100 10 1 1 1 0'
[]
[]
[FunctorMaterials]
[fluid_props_to_mat_props]
type = GeneralFunctorFluidProps
fp = air
pressure = pressure
T_fluid = T_fluid
speed = speed
force_define_density = true
neglect_derivatives_of_density_time_derivative = false
mu_rampdown = 'mu_rampdown_fn'
characteristic_length = 1
porosity = porosity
[]
[scalar_props]
type = ADGenericFunctorMaterial
prop_names = 'porosity loss_coeff'
prop_values = '1 1.3'
[]
[linear_friction]
type = ADParsedFunctorMaterial
property_name = 'linear_friction'
expression = 'loss_coeff * rho'
functor_names = 'loss_coeff rho'
[]
[linear_friction_coeff]
type = ADGenericVectorFunctorMaterial
prop_names = 'linear_friction_coeff'
prop_values = 'linear_friction linear_friction linear_friction'
[]
[]
[AuxVariables]
[rho_var]
type = MooseVariableFVReal
[]
[cp_var]
type = MooseVariableFVReal
[]
[rho_cp_T_fluid_var]
type = MooseVariableFVReal
[]
[]
[AuxKernels]
[rho_var_aux]
type = FunctorAux
variable = rho_var
functor = rho
[]
[cp_var_aux]
type = FunctorAux
variable = cp_var
functor = cp
[]
[rho_cp_T_fluid_var_aux]
type = ParsedAux
variable = rho_cp_T_fluid_var
coupled_variables = 'rho_var cp_var T_fluid'
expression = 'rho_var * cp_var * T_fluid'
[]
[]
[Postprocessors]
[inlet_mfr]
type = VolumetricFlowRate
vel_x = superficial_vel_x
vel_y = superficial_vel_y
advected_quantity = rho
boundary = bottom
advected_interp_method = average
[]
[outlet_mfr]
type = VolumetricFlowRate
vel_x = superficial_vel_x
vel_y = superficial_vel_y
advected_quantity = rho
boundary = top
advected_interp_method = average
[]
[inlet_energy]
type = VolumetricFlowRate
vel_x = superficial_vel_x
vel_y = superficial_vel_y
advected_quantity = rho_cp_T_fluid_var
boundary = bottom
advected_interp_method = average
[]
[outlet_energy]
type = VolumetricFlowRate
vel_x = superficial_vel_x
vel_y = superficial_vel_y
advected_quantity = rho_cp_T_fluid_var
boundary = top
advected_interp_method = average
[]
[]
[Debug]
show_var_residual_norms = true
[]
[Outputs]
exodus = true
[]
(modules/navier_stokes/test/tests/finite_volume/ins/boussinesq/wcnsfv.i)
mu = 1
rho = 'rho'
k = 1
cp = 1
alpha = 1
velocity_interp_method = 'rc'
advected_interp_method = 'average'
# rayleigh=1e3
cold_temp=300
hot_temp=310
[GlobalParams]
two_term_boundary_expansion = true
rhie_chow_user_object = 'rc'
[]
[UserObjects]
[rc]
type = INSFVRhieChowInterpolator
u = u
v = v
pressure = pressure
[]
[]
[Mesh]
[gen]
type = GeneratedMeshGenerator
dim = 2
xmin = 0
xmax = 10
ymin = 0
ymax = 10
nx = 64
ny = 64
[]
[]
[Variables]
[u]
type = INSFVVelocityVariable
initial_condition = 1e-15
[]
[v]
type = INSFVVelocityVariable
initial_condition = 1e-15
[]
[pressure]
type = INSFVPressureVariable
initial_condition = 1e5
[]
[T]
type = INSFVEnergyVariable
scaling = 1e-4
initial_condition = ${cold_temp}
[]
[lambda]
family = SCALAR
order = FIRST
[]
[]
[AuxVariables]
[U]
order = CONSTANT
family = MONOMIAL
fv = true
[]
[vel_x]
order = FIRST
family = MONOMIAL
[]
[vel_y]
order = FIRST
family = MONOMIAL
[]
[viz_T]
order = FIRST
family = MONOMIAL
[]
[rho_out]
type = MooseVariableFVReal
[]
[]
[AuxKernels]
[mag]
type = VectorMagnitudeAux
variable = U
x = u
y = v
execute_on = 'initial timestep_end'
[]
[vel_x]
type = ParsedAux
variable = vel_x
expression = 'u'
execute_on = 'initial timestep_end'
coupled_variables = 'u'
[]
[vel_y]
type = ParsedAux
variable = vel_y
expression = 'v'
execute_on = 'initial timestep_end'
coupled_variables = 'v'
[]
[viz_T]
type = ParsedAux
variable = viz_T
expression = 'T'
execute_on = 'initial timestep_end'
coupled_variables = 'T'
[]
[rho_out]
type = FunctorAux
functor = 'rho'
variable = 'rho_out'
execute_on = 'initial timestep_end'
[]
[]
[FVKernels]
[mass]
type = INSFVMassAdvection
variable = pressure
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = ${rho}
[]
[mean_zero_pressure]
type = FVIntegralValueConstraint
variable = pressure
lambda = lambda
phi0 = 1e5
[]
[u_advection]
type = INSFVMomentumAdvection
variable = u
velocity_interp_method = ${velocity_interp_method}
advected_interp_method = ${advected_interp_method}
rho = ${rho}
momentum_component = 'x'
[]
[u_viscosity]
type = INSFVMomentumDiffusion
variable = u
mu = ${mu}
momentum_component = 'x'
[]
[u_pressure]
type = INSFVMomentumPressure
variable = u
momentum_component = 'x'
pressure = pressure
[]
[u_gravity]
type = INSFVMomentumGravity
variable = u
gravity = '0 -1 0'
rho = ${rho}
momentum_component = 'x'
[]
[v_advection]
type = INSFVMomentumAdvection
variable = v
velocity_interp_method = ${velocity_interp_method}
advected_interp_method = ${advected_interp_method}
rho = ${rho}
momentum_component = 'y'
[]
[v_viscosity]
type = INSFVMomentumDiffusion
variable = v
mu = ${mu}
momentum_component = 'y'
[]
[v_pressure]
type = INSFVMomentumPressure
variable = v
momentum_component = 'y'
pressure = pressure
[]
[v_gravity]
type = INSFVMomentumGravity
variable = v
gravity = '0 -1 0'
rho = ${rho}
momentum_component = 'y'
[]
[temp_conduction]
type = FVDiffusion
coeff = 'k'
variable = T
[]
[temp_advection]
type = INSFVEnergyAdvection
variable = T
velocity_interp_method = ${velocity_interp_method}
advected_interp_method = ${advected_interp_method}
[]
[]
[FVBCs]
[no_slip_x]
type = INSFVNoSlipWallBC
variable = u
boundary = 'left right top bottom'
function = 0
[]
[no_slip_y]
type = INSFVNoSlipWallBC
variable = v
boundary = 'left right top bottom'
function = 0
[]
[T_hot]
type = FVDirichletBC
variable = T
boundary = left
value = ${hot_temp}
[]
[T_cold]
type = FVDirichletBC
variable = T
boundary = right
value = ${cold_temp}
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Materials]
[const]
type = ADGenericConstantMaterial
prop_names = 'alpha'
prop_values = '${alpha}'
[]
[]
[FunctorMaterials]
[const_functor]
type = ADGenericFunctorMaterial
prop_names = 'cp k'
prop_values = '${cp} ${k}'
[]
[rho]
type = RhoFromPTFunctorMaterial
fp = fp
temperature = T
pressure = pressure
[]
[ins_fv]
type = INSFVEnthalpyFunctorMaterial
temperature = 'T'
rho = ${rho}
[]
[]
[Functions]
[lid_function]
type = ParsedFunction
expression = '4*x*(1-x)'
[]
[]
[Executioner]
type = Steady
solve_type = 'NEWTON'
petsc_options_iname = '-pc_type -pc_factor_shift_type'
petsc_options_value = 'lu NONZERO'
[]
[Outputs]
exodus = true
[]
(modules/thermal_hydraulics/test/tests/problems/area_constriction/area_constriction_junction.i)
# This test features air flowing through a channel whose cross-sectional area
# shrinks to half its value in the right half. Assuming incompressible flow
# conditions, such as having a low Mach number, the velocity should approximately
# double from inlet to outlet. In this version of the test, the area discontinuity
# is achieved by connecting two flow channels with a junction.
p_outlet = 1e5
[GlobalParams]
gravity_vector = '0 0 0'
initial_T = 300
initial_p = ${p_outlet}
fp = fp
closures = simple_closures
f = 0
scaling_factor_1phase = '1 1 1e-5'
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[inlet]
type = InletDensityVelocity1Phase
input = 'pipe1:in'
rho = 1.16263315948279 # rho @ (p = 1e5 Pa, T = 300 K)
vel = 1
[]
[pipe1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = 50
A = 1
initial_vel = 1
[]
[junction]
type = JunctionOneToOne1Phase
connections = 'pipe1:out pipe2:in'
[]
[pipe2]
type = FlowChannel1Phase
position = '0.5 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = 50
A = 0.5
initial_vel = 2
[]
[outlet]
type = Outlet1Phase
input = 'pipe2:out'
p = ${p_outlet}
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'bdf2'
end_time = 10
[TimeStepper]
type = IterationAdaptiveDT
dt = 0.001
optimal_iterations = 5
iteration_window = 1
growth_factor = 1.2
[]
steady_state_detection = true
solve_type = PJFNK
nl_rel_tol = 1e-10
nl_abs_tol = 1e-8
nl_max_its = 15
l_tol = 1e-3
l_max_its = 10
[]
[Outputs]
exodus = true
velocity_as_vector = false
show = 'A rho vel p'
[]
(modules/thermal_hydraulics/test/tests/postprocessors/specific_impulse_1phase/Isp_1ph.i)
[GlobalParams]
gravity_vector = '0 0 0'
initial_p = 6e6
initial_T = 600
initial_vel = 0
scaling_factor_1phase = '1 1 1e-5'
closures = simple_closures
[]
[FluidProperties]
[eos]
type = IdealGasFluidProperties
gamma = 1.3066
molar_mass = 2.016e-3
k = 0.437
mu = 3e-5
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[pipe1]
type = FlowChannel1Phase
fp = eos
position = '0 0 0'
orientation = '1 0 0'
length = 1
n_elems = 10
A = 0.1
f = 0.
[]
[inlet]
type = InletMassFlowRateTemperature1Phase
m_dot = 0.1
T = 800
input = 'pipe1:in'
[]
[outlet]
type = Outlet1Phase
input = 'pipe1:out'
p = 6e6
[]
[]
[Preconditioning]
[SMP_PJFNK]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
[TimeStepper]
type = IterationAdaptiveDT
dt = 0.01
growth_factor = 1.4
optimal_iterations = 6
iteration_window = 2
[]
start_time = 0.0
end_time = 100
abort_on_solve_fail = true
solve_type = 'NEWTON'
line_search = 'basic'
nl_rel_tol = 1e-6
nl_abs_tol = 1e-6
nl_max_its = 10
l_tol = 1e-3
l_max_its = 10
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
[]
[Postprocessors]
# hand calcs show that Isp should start at 274.3 at 600 K
# and rise to 316.7 at 800 K.
[Isp]
type = ADSpecificImpulse1Phase
p_exit = 1e6
fp = eos
boundary = outlet
[]
[Isp_inst]
type = ADSpecificImpulse1Phase
p_exit = 1e6
fp = eos
cumulative = false
boundary = outlet
[]
[outletT]
type = SideAverageValue
variable = T
boundary = pipe1:out
[]
[]
[Outputs]
[out]
type = CSV
show = 'Isp Isp_inst'
execute_on = 'INITIAL FINAL'
[]
[]
(modules/thermal_hydraulics/test/tests/auxkernels/flow_model_gas_mix_aux/flow_model_gas_mix_aux.i)
mass_fraction = 0.4
vel = 10
area = 0.2
# computed at p = 1e5 Pa, T = 300 K:
rho = 1.30632939267729
e_value = 1.789042384551724e+05
E = ${fparse e_value + 0.5 * vel * vel}
rhoA = ${fparse rho * area}
xirhoA = ${fparse mass_fraction * rhoA}
rhouA = ${fparse rhoA * vel}
rhoEA = ${fparse rhoA * E}
[GlobalParams]
fluid_properties = mixture_fp
xirhoA = xirhoA
rhoA = rhoA
rhouA = rhouA
rhoEA = rhoEA
area = A
[]
[Mesh]
type = GeneratedMesh
dim = 1
nx = 5
[]
[FluidProperties]
[fp1]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.029
[]
[fp2]
type = IdealGasFluidProperties
gamma = 1.5
molar_mass = 0.04
[]
[mixture_fp]
type = IdealGasMixtureFluidProperties
component_fluid_properties = 'fp1 fp2'
[]
[]
[AuxVariables]
[A]
initial_condition = ${area}
[]
[xirhoA]
initial_condition = ${xirhoA}
[]
[rhoA]
initial_condition = ${rhoA}
[]
[rhouA]
initial_condition = ${rhouA}
[]
[rhoEA]
initial_condition = ${rhoEA}
[]
[p]
[]
[T]
[]
[]
[AuxKernels]
[p_aux]
type = FlowModelGasMixAux
variable = p
quantity = p
execute_on = 'INITIAL'
[]
[T_aux]
type = FlowModelGasMixAux
variable = T
quantity = T
execute_on = 'INITIAL'
[]
[]
[Postprocessors]
[p]
type = AverageNodalVariableValue
variable = p
execute_on = 'INITIAL'
[]
[T]
type = AverageNodalVariableValue
variable = T
execute_on = 'INITIAL'
[]
[]
[Problem]
solve = false
[]
[Executioner]
type = Steady
[]
[Outputs]
csv = true
execute_on = 'INITIAL'
[]
(modules/thermal_hydraulics/test/tests/materials/ad_wall_htc_gnielinski_annular/ad_wall_htc_gnielinski_annular.i)
rho = 3.1176
vel = 100
k = 0.38220
mu = 4.8587e-05
cp = 5189.8
p = 100e3
T = 1073
T_wall = 1074
D_inner = 0.01
D_outer = 0.015
length = 0.5
[GlobalParams]
execute_on = 'INITIAL'
[]
[Mesh]
type = GeneratedMesh
dim = 1
nx = 1
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Materials]
[props]
type = ADGenericConstantMaterial
prop_names = 'rho vel k mu cp p T T_wall'
prop_values = '${rho} ${vel} ${k} ${mu} ${cp} ${p} ${T} ${T_wall}'
[]
[test_material]
type = ADWallHTCGnielinskiAnnularMaterial
htc_wall = htc_wall
D_inner = ${D_inner}
D_outer = ${D_outer}
channel_length = ${length}
at_inner_wall = true
fluid_is_gas = true
gas_heating_correction_exponent = 0.15
fluid_properties = fp
[]
[]
[Problem]
solve = false
[]
[Executioner]
type = Steady
[]
[Postprocessors]
[htc_wall]
type = ADElementAverageMaterialProperty
mat_prop = htc_wall
[]
[]
[Outputs]
csv = true
[]
(modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/basic-conserved-pcnsfv-kt.i)
[GlobalParams]
fp = fp
limiter = 'central_difference'
two_term_boundary_expansion = true
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 1
xmin = .1
xmax = .6
nx = 2
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Problem]
fv_bcs_integrity_check = false
[]
[Variables]
[rho]
type = MooseVariableFVReal
[]
[rho_ud]
type = MooseVariableFVReal
[]
[rho_et]
type = MooseVariableFVReal
[]
[]
[ICs]
[pressure]
type = FunctionIC
variable = rho
function = 'exact_rho'
[]
[sup_vel_x]
type = FunctionIC
variable = rho_ud
function = 'exact_rho_ud'
[]
[T_fluid]
type = FunctionIC
variable = rho_et
function = 'exact_rho_et'
[]
[]
[FVKernels]
[mass_advection]
type = PCNSFVKT
variable = rho
eqn = "mass"
[]
[mass_fn]
type = FVBodyForce
variable = rho
function = 'forcing_rho'
[]
[momentum_x_advection]
type = PCNSFVKT
variable = rho_ud
momentum_component = x
eqn = "momentum"
[]
[momentum_fn]
type = FVBodyForce
variable = rho_ud
function = 'forcing_rho_ud'
[]
[fluid_energy_advection]
type = PCNSFVKT
variable = rho_et
eqn = "energy"
[]
[energy_fn]
type = FVBodyForce
variable = rho_et
function = 'forcing_rho_et'
[]
[]
[FVBCs]
[mass_left]
variable = rho
type = PCNSFVStrongBC
boundary = left
T_fluid = 'exact_T'
superficial_velocity = 'exact_superficial_velocity'
eqn = 'mass'
[]
[momentum_left]
variable = rho_ud
type = PCNSFVStrongBC
boundary = left
T_fluid = 'exact_T'
superficial_velocity = 'exact_superficial_velocity'
eqn = 'momentum'
momentum_component = 'x'
[]
[energy_left]
variable = rho_et
type = PCNSFVStrongBC
boundary = left
T_fluid = 'exact_T'
superficial_velocity = 'exact_superficial_velocity'
eqn = 'energy'
[]
[mass_right]
variable = rho
type = PCNSFVStrongBC
boundary = right
eqn = 'mass'
pressure = 'exact_p'
[]
[momentum_right]
variable = rho_ud
type = PCNSFVStrongBC
boundary = right
eqn = 'momentum'
momentum_component = 'x'
pressure = 'exact_p'
[]
[energy_right]
variable = rho_et
type = PCNSFVStrongBC
boundary = right
eqn = 'energy'
pressure = 'exact_p'
[]
# help gradient reconstruction
[rho_right]
type = FVFunctionDirichletBC
variable = rho
function = exact_rho
boundary = 'right'
[]
[rho_ud_left]
type = FVFunctionDirichletBC
variable = rho_ud
function = exact_rho_ud
boundary = 'left'
[]
[rho_et_left]
type = FVFunctionDirichletBC
variable = rho_et
function = exact_rho_et
boundary = 'left'
[]
[]
[Materials]
[var_mat]
type = PorousConservedVarMaterial
rho = rho
superficial_rhou = rho_ud
rho_et = rho_et
porosity = porosity
[]
[porosity]
type = GenericFunctionMaterial
prop_names = 'porosity'
prop_values = 'eps'
[]
[]
[Functions]
[exact_rho]
type = ParsedFunction
expression = '3.48788261470924*cos(x)'
[]
[forcing_rho]
type = ParsedFunction
expression = '-3.45300378856215*sin(1.1*x)'
[]
[exact_rho_ud]
type = ParsedFunction
expression = '3.13909435323832*cos(1.1*x)'
[]
[forcing_rho_ud]
type = ParsedFunction
expression = '-0.9*(10.6975765229419*cos(1.2*x)/cos(x) - 0.697576522941849*cos(1.1*x)^2/cos(x)^2)*sin(x) + 0.9*(10.6975765229419*sin(x)*cos(1.2*x)/cos(x)^2 - 1.3951530458837*sin(x)*cos(1.1*x)^2/cos(x)^3 + 1.53466835047207*sin(1.1*x)*cos(1.1*x)/cos(x)^2 - 12.8370918275302*sin(1.2*x)/cos(x))*cos(x) + 3.13909435323832*sin(x)*cos(1.1*x)^2/cos(x)^2 - 6.9060075771243*sin(1.1*x)*cos(1.1*x)/cos(x)'
[]
[exact_rho_et]
type = ParsedFunction
expression = '26.7439413073546*cos(1.2*x)'
[]
[forcing_rho_et]
type = ParsedFunction
expression = '0.9*(3.48788261470924*(3.06706896551724*cos(1.2*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.2*x))*sin(x)*cos(1.1*x)/cos(x)^2 - 0.99*(3.48788261470924*(3.06706896551724*cos(1.2*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.2*x))*sin(1.1*x)/cos(x) + 0.9*(-(10.6975765229419*cos(1.2*x)/cos(x) - 0.697576522941849*cos(1.1*x)^2/cos(x)^2)*sin(x) + (10.6975765229419*sin(x)*cos(1.2*x)/cos(x)^2 - 1.3951530458837*sin(x)*cos(1.1*x)^2/cos(x)^3 + 1.53466835047207*sin(1.1*x)*cos(1.1*x)/cos(x)^2 - 12.8370918275302*sin(1.2*x)/cos(x))*cos(x) - 32.0927295688256*sin(1.2*x))*cos(1.1*x)/cos(x)'
[]
[exact_T]
type = ParsedFunction
expression = '0.0106975765229418*cos(1.2*x)/cos(x) - 0.000697576522941848*cos(1.1*x)^2/cos(x)^2'
[]
[exact_eps_p]
type = ParsedFunction
expression = '3.13909435323832*(3.06706896551724*cos(1.2*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x)'
[]
[exact_p]
type = ParsedFunction
expression = '3.48788261470924*(3.06706896551724*cos(1.2*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x)'
[]
[exact_sup_vel_x]
type = ParsedFunction
expression = '0.9*cos(1.1*x)/cos(x)'
[]
[exact_superficial_velocity]
type = ParsedVectorFunction
expression_x = '0.9*cos(1.1*x)/cos(x)'
[]
[eps]
type = ParsedFunction
expression = '0.9'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
solve_type = NEWTON
type = Transient
num_steps = 1
dtmin = 1
petsc_options = '-snes_linesearch_monitor'
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_max_its = 50
line_search = bt
[]
[Outputs]
exodus = true
csv = true
[]
[Debug]
show_var_residual_norms = true
[]
[Postprocessors]
[h]
type = AverageElementSize
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2rho]
type = ElementL2Error
variable = rho
function = exact_rho
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2rho_ud]
variable = rho_ud
function = exact_rho_ud
type = ElementL2Error
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2rho_et]
variable = rho_et
function = exact_rho_et
type = ElementL2Error
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[]
(modules/navier_stokes/test/tests/finite_volume/cns/straight_channel_porosity_step/implicit-euler-basic-kt-primitive.i)
p_initial=1.01e5
T=273.15
# u refers to the superficial velocity
u_in=1
user_limiter='upwind'
[GlobalParams]
fp = fp
two_term_boundary_expansion = true
limiter = ${user_limiter}
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 1
xmin = 0
xmax = 18
nx = 180
[]
[to_pt5]
input = cartesian
type = SubdomainBoundingBoxGenerator
bottom_left = '2 0 0'
top_right = '4 1 0'
block_id = 1
[]
[pt5]
input = to_pt5
type = SubdomainBoundingBoxGenerator
bottom_left = '4 0 0'
top_right = '6 1 0'
block_id = 2
[]
[to_pt25]
input = pt5
type = SubdomainBoundingBoxGenerator
bottom_left = '6 0 0'
top_right = '8 1 0'
block_id = 3
[]
[pt25]
input = to_pt25
type = SubdomainBoundingBoxGenerator
bottom_left = '8 0 0'
top_right = '10 1 0'
block_id = 4
[]
[to_pt5_again]
input = pt25
type = SubdomainBoundingBoxGenerator
bottom_left = '10 0 0'
top_right = '12 1 0'
block_id = 5
[]
[pt5_again]
input = to_pt5_again
type = SubdomainBoundingBoxGenerator
bottom_left = '12 0 0'
top_right = '14 1 0'
block_id = 6
[]
[to_one]
input = pt5_again
type = SubdomainBoundingBoxGenerator
bottom_left = '14 0 0'
top_right = '16 1 0'
block_id = 7
[]
[one]
input = to_one
type = SubdomainBoundingBoxGenerator
bottom_left = '16 0 0'
top_right = '18 1 0'
block_id = 8
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Problem]
fv_bcs_integrity_check = false
[]
[Variables]
[pressure]
type = MooseVariableFVReal
initial_condition = ${p_initial}
[]
[sup_vel_x]
type = MooseVariableFVReal
initial_condition = 1e-15
scaling = 1e-2
[]
[T_fluid]
type = MooseVariableFVReal
initial_condition = ${T}
scaling = 1e-5
[]
[]
[AuxVariables]
[vel_x]
type = MooseVariableFVReal
[]
[sup_mom_x]
type = MooseVariableFVReal
[]
[rho]
type = MooseVariableFVReal
[]
[worst_courant]
type = MooseVariableFVReal
[]
[porosity]
type = MooseVariableFVReal
[]
[]
[AuxKernels]
[vel_x]
type = ADMaterialRealAux
variable = vel_x
property = vel_x
execute_on = 'timestep_end'
[]
[sup_mom_x]
type = ADMaterialRealAux
variable = sup_mom_x
property = superficial_rhou
execute_on = 'timestep_end'
[]
[rho]
type = ADMaterialRealAux
variable = rho
property = rho
execute_on = 'timestep_end'
[]
[worst_courant]
type = Courant
variable = worst_courant
u = sup_vel_x
execute_on = 'timestep_end'
[]
[porosity]
type = MaterialRealAux
variable = porosity
property = porosity
execute_on = 'timestep_end'
[]
[]
[FVKernels]
[mass_time]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rho_dt'
variable = pressure
[]
[mass_advection]
type = PCNSFVKT
variable = pressure
eqn = "mass"
[]
[momentum_time]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rhou_dt'
variable = sup_vel_x
[]
[momentum_advection]
type = PCNSFVKT
variable = sup_vel_x
eqn = "momentum"
momentum_component = 'x'
[]
[eps_grad]
type = PNSFVPGradEpsilon
variable = sup_vel_x
momentum_component = 'x'
epsilon_function = 'eps'
[]
[energy_time]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rho_et_dt'
variable = T_fluid
[]
[energy_advection]
type = PCNSFVKT
variable = T_fluid
eqn = "energy"
[]
[]
[FVBCs]
[rho_left]
type = PCNSFVStrongBC
boundary = 'left'
variable = pressure
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'mass'
[]
[rhou_left]
type = PCNSFVStrongBC
boundary = 'left'
variable = sup_vel_x
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'momentum'
momentum_component = 'x'
[]
[rho_et_left]
type = PCNSFVStrongBC
boundary = 'left'
variable = T_fluid
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'energy'
[]
[rho_right]
type = PCNSFVStrongBC
boundary = 'right'
variable = pressure
pressure = ${p_initial}
eqn = 'mass'
[]
[rhou_right]
type = PCNSFVStrongBC
boundary = 'right'
variable = sup_vel_x
pressure = ${p_initial}
eqn = 'momentum'
momentum_component = 'x'
[]
[rho_et_right]
type = PCNSFVStrongBC
boundary = 'right'
variable = T_fluid
pressure = ${p_initial}
eqn = 'energy'
[]
# Use these to help create more accurate cell centered gradients for cells adjacent to boundaries
[T_left]
type = FVDirichletBC
variable = T_fluid
value = ${T}
boundary = 'left'
[]
[sup_vel_left]
type = FVDirichletBC
variable = sup_vel_x
value = ${u_in}
boundary = 'left'
[]
[p_right]
type = FVDirichletBC
variable = pressure
value = ${p_initial}
boundary = 'right'
[]
[]
[Functions]
[ud_in]
type = ParsedVectorFunction
expression_x = '${u_in}'
[]
[eps]
type = ParsedFunction
expression = 'if(x < 2, 1,
if(x < 4, 1 - .5 / 2 * (x - 2),
if(x < 6, .5,
if(x < 8, .5 - .25 / 2 * (x - 6),
if(x < 10, .25,
if(x < 12, .25 + .25 / 2 * (x - 10),
if(x < 14, .5,
if(x < 16, .5 + .5 / 2 * (x - 14),
1))))))))'
[]
[]
[Materials]
[var_mat]
type = PorousPrimitiveVarMaterial
pressure = pressure
T_fluid = T_fluid
superficial_vel_x = sup_vel_x
fp = fp
porosity = porosity
[]
[porosity]
type = GenericFunctionMaterial
prop_names = 'porosity'
prop_values = 'eps'
[]
[]
[Executioner]
solve_type = NEWTON
line_search = 'bt'
type = Transient
nl_max_its = 20
[TimeStepper]
type = IterationAdaptiveDT
dt = 5e-5
optimal_iterations = 6
growth_factor = 1.2
[]
num_steps = 10000
end_time = 500
nl_abs_tol = 1e-8
[]
[Outputs]
[out]
type = Exodus
execute_on = 'final'
[]
checkpoint = true
[]
[Debug]
show_var_residual_norms = true
[]
(modules/thermal_hydraulics/test/tests/components/junction_one_to_one_1phase/junction_one_to_one_1phase.i)
# This input file simulates the Sod shock tube using a junction in the middle
# of the domain. The solution should be exactly equivalent to the problem with
# no junction. This test examines the solutions at the junction connections
# and compares them to gold values generated from a version of this input file
# that has no junction.
[GlobalParams]
gravity_vector = '0 0 0'
closures = simple_closures
[]
[Functions]
[p_ic_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.5 1.0'
y = '1.0 0.1'
[]
[T_ic_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.5 1.0'
y = '1.4 1.12'
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 11.64024372
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[left_boundary]
type = FreeBoundary1Phase
input = 'left_channel:in'
[]
[left_channel]
type = FlowChannel1Phase
fp = fp
position = '0 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = 50
A = 1.0
initial_T = T_ic_fn
initial_p = p_ic_fn
initial_vel = 0
f = 0
[]
[junction]
type = JunctionOneToOne1Phase
connections = 'left_channel:out right_channel:in'
[]
[right_channel]
type = FlowChannel1Phase
fp = fp
position = '0.5 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = 50
A = 1.0
initial_T = T_ic_fn
initial_p = p_ic_fn
initial_vel = 0
f = 0
[]
[right_boundary]
type = FreeBoundary1Phase
input = 'right_channel:out'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
solve_type = NEWTON
nl_rel_tol = 1e-10
nl_abs_tol = 1e-8
nl_max_its = 60
l_tol = 1e-4
start_time = 0.0
dt = 1e-3
num_steps = 5
abort_on_solve_fail = true
[]
[Postprocessors]
[rhoA_left]
type = SideAverageValue
variable = rhoA
boundary = left_channel:out
execute_on = 'initial timestep_end'
[]
[rhouA_left]
type = SideAverageValue
variable = rhouA
boundary = left_channel:out
execute_on = 'initial timestep_end'
[]
[rhoEA_left]
type = SideAverageValue
variable = rhoEA
boundary = left_channel:out
execute_on = 'initial timestep_end'
[]
[rhoA_right]
type = SideAverageValue
variable = rhoA
boundary = right_channel:in
execute_on = 'initial timestep_end'
[]
# rhouA_right is added by tests file
[rhoEA_right]
type = SideAverageValue
variable = rhoEA
boundary = right_channel:in
execute_on = 'initial timestep_end'
[]
# This is present to test that junction sidesets work properly
[p_avg_junction]
type = SideAverageValue
boundary = 'junction'
variable = p
execute_on = 'initial timestep_end'
[]
[]
[Outputs]
csv = true
show = 'rhoA_left rhouA_left rhoEA_left rhoA_right rhouA_right rhoEA_right'
execute_on = 'initial timestep_end'
[]
(modules/fluid_properties/test/tests/fp_interrogator/1ph.rho_rhou_rhoE.i)
[FluidPropertiesInterrogator]
fp = fp
rho = 0.5
rhou = 0.5
rhoE = 2.75
[]
[FluidProperties]
[./fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 11.640243719999999
[../]
[]
(modules/fluid_properties/test/tests/fp_interrogator/1ph.p_T.i)
[FluidPropertiesInterrogator]
fp = fp
p = 1e5
T = 300
[]
[FluidProperties]
[./fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02900055737704918
mu = 1.823e-05
k = 0.02568
[../]
[]
(modules/thermal_hydraulics/tutorials/single_phase_flow/05_secondary_side.i)
T_in = 300. # K
m_dot_in = 1e-2 # kg/s
press = 10e5 # Pa
# core parameters
core_length = 1. # m
core_n_elems = 25
core_dia = '${units 2. cm -> m}'
core_pitch = '${units 8.7 cm -> m}'
A_core = '${fparse core_pitch^2 - 0.25 *pi * core_dia^2}'
P_wet_core = '${fparse 4*core_pitch + pi * core_dia}'
Dh_core = '${fparse 4 * A_core / P_wet_core}'
# pipe parameters
pipe_dia = '${units 10. cm -> m}'
A_pipe = '${fparse 0.25 * pi * pipe_dia^2}'
tot_power = 2000 # W
# heat exchanger parameters
hx_dia_inner = '${units 12. cm -> m}'
hx_wall_thickness = '${units 5. mm -> m}'
hx_dia_outer = '${units 50. cm -> m}'
hx_radius_wall = '${fparse hx_dia_inner / 2. + hx_wall_thickness}'
hx_length = 1.5 # m
hx_n_elems = 25
m_dot_sec_in = 1. # kg/s
[GlobalParams]
initial_p = ${press}
initial_vel = 0.0001
initial_T = ${T_in}
initial_vel_x = 0
initial_vel_y = 0
initial_vel_z = 0
gravity_vector = '0 0 0'
rdg_slope_reconstruction = minmod
scaling_factor_1phase = '1 1e-2 1e-4'
scaling_factor_rhoV = 1
scaling_factor_rhouV = 1e-2
scaling_factor_rhovV = 1e-2
scaling_factor_rhowV = 1e-2
scaling_factor_rhoEV = 1e-4
closures = thm_closures
fp = he
[]
[Functions]
[m_dot_sec_fn]
type = PiecewiseLinear
xy_data = '
0 0
10 ${m_dot_sec_in}'
[]
[]
[FluidProperties]
[he]
type = IdealGasFluidProperties
molar_mass = 4e-3
gamma = 1.67
k = 0.2556
mu = 3.22639e-5
[]
[water]
type = StiffenedGasFluidProperties
gamma = 2.35
cv = 1816.0
q = -1.167e6
p_inf = 1.0e9
q_prime = 0
[]
[]
[Closures]
[thm_closures]
type = Closures1PhaseTHM
[]
[]
[SolidProperties]
[steel]
type = ThermalFunctionSolidProperties
rho = 8050
k = 45
cp = 466
[]
[]
[Components]
[total_power]
type = TotalPower
power = ${tot_power}
[]
[up_pipe_1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '0 0 1'
length = 0.5
n_elems = 15
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct1]
type = JunctionParallelChannels1Phase
position = '0 0 0.5'
connections = 'up_pipe_1:out core_chan:in'
volume = 1e-5
[]
[core_chan]
type = FlowChannel1Phase
position = '0 0 0.5'
orientation = '0 0 1'
length = ${core_length}
n_elems = ${core_n_elems}
roughness = .0001
A = ${A_core}
D_h = ${Dh_core}
[]
[core_hs]
type = HeatStructureCylindrical
position = '0 0 0.5'
orientation = '0 0 1'
length = ${core_length}
n_elems = ${core_n_elems}
names = 'block'
widths = '${fparse core_dia / 2.}'
solid_properties = 'steel'
solid_properties_T_ref = '300'
n_part_elems = 3
[]
[core_heating]
type = HeatSourceFromTotalPower
hs = core_hs
regions = block
power = total_power
[]
[core_ht]
type = HeatTransferFromHeatStructure1Phase
flow_channel = core_chan
hs = core_hs
hs_side = outer
P_hf = '${fparse pi * core_dia}'
[]
[jct2]
type = JunctionParallelChannels1Phase
position = '0 0 1.5'
connections = 'core_chan:out up_pipe_2:in'
volume = 1e-5
[]
[up_pipe_2]
type = FlowChannel1Phase
position = '0 0 1.5'
orientation = '0 0 1'
length = 0.5
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct3]
type = JunctionOneToOne1Phase
connections = 'up_pipe_2:out top_pipe_1:in'
[]
[top_pipe_1]
type = FlowChannel1Phase
position = '0 0 2'
orientation = '1 0 0'
length = 0.5
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[top_pipe_2]
type = FlowChannel1Phase
position = '0.5 0 2'
orientation = '1 0 0'
length = 0.5
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct4]
type = VolumeJunction1Phase
position = '0.5 0 2'
volume = 1e-5
connections = 'top_pipe_1:out top_pipe_2:in press_pipe:in'
[]
[press_pipe]
type = FlowChannel1Phase
position = '0.5 0 2'
orientation = '0 1 0'
length = 0.2
n_elems = 5
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[pressurizer]
type = InletStagnationPressureTemperature1Phase
p0 = ${press}
T0 = ${T_in}
input = press_pipe:out
[]
[jct5]
type = JunctionOneToOne1Phase
connections = 'top_pipe_2:out down_pipe_1:in'
[]
[down_pipe_1]
type = FlowChannel1Phase
position = '1 0 2'
orientation = '0 0 -1'
length = 0.25
A = ${A_pipe}
n_elems = 5
[]
[jct6]
type = JunctionParallelChannels1Phase
position = '1 0 1.75'
connections = 'down_pipe_1:out hx/pri:in'
volume = 1e-5
[]
[hx]
[pri]
type = FlowChannel1Phase
position = '1 0 1.75'
orientation = '0 0 -1'
length = ${hx_length}
n_elems = ${hx_n_elems}
roughness = 1e-5
A = '${fparse pi * hx_dia_inner * hx_dia_inner / 4.}'
D_h = ${hx_dia_inner}
[]
[ht_pri]
type = HeatTransferFromHeatStructure1Phase
hs = hx/wall
hs_side = inner
flow_channel = hx/pri
P_hf = '${fparse pi * hx_dia_inner}'
[]
[wall]
type = HeatStructureCylindrical
position = '1 0 1.75'
orientation = '0 0 -1'
length = ${hx_length}
n_elems = ${hx_n_elems}
widths = '${hx_wall_thickness}'
n_part_elems = '3'
solid_properties = 'steel'
solid_properties_T_ref = '300'
names = '0'
inner_radius = '${fparse hx_dia_inner / 2.}'
[]
[ht_sec]
type = HeatTransferFromHeatStructure1Phase
hs = hx/wall
hs_side = outer
flow_channel = hx/sec
P_hf = '${fparse 2 * pi * hx_radius_wall}'
[]
[sec]
type = FlowChannel1Phase
position = '${fparse 1 + hx_wall_thickness} 0 0.25'
orientation = '0 0 1'
length = ${hx_length}
n_elems = ${hx_n_elems}
A = '${fparse pi * (hx_dia_outer * hx_dia_outer / 4. - hx_radius_wall * hx_radius_wall)}'
D_h = '${fparse hx_dia_outer - (2 * hx_radius_wall)}'
fp = water
initial_T = 300
[]
[]
[jct7]
type = JunctionParallelChannels1Phase
position = '1 0 0.5'
connections = 'hx/pri:out down_pipe_2:in'
volume = 1e-5
[]
[down_pipe_2]
type = FlowChannel1Phase
position = '1 0 0.25'
orientation = '0 0 -1'
length = 0.25
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct8]
type = JunctionOneToOne1Phase
connections = 'down_pipe_2:out bottom_1:in'
[]
[bottom_1]
type = FlowChannel1Phase
position = '1 0 0'
orientation = '-1 0 0'
length = 0.5
n_elems = 5
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[pump]
type = Pump1Phase
position = '0.5 0 0'
connections = 'bottom_1:out bottom_2:in'
volume = 1e-4
A_ref = ${A_pipe}
head = 0
[]
[bottom_2]
type = FlowChannel1Phase
position = '0.5 0 0'
orientation = '-1 0 0'
length = 0.5
n_elems = 5
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct9]
type = JunctionOneToOne1Phase
connections = 'bottom_2:out up_pipe_1:in'
[]
[inlet_sec]
type = InletMassFlowRateTemperature1Phase
input = 'hx/sec:in'
m_dot = 0
T = 300
[]
[outlet_sec]
type = Outlet1Phase
input = 'hx/sec:out'
p = 1e5
[]
[]
[ControlLogic]
[set_point]
type = GetFunctionValueControl
function = ${m_dot_in}
[]
[pid]
type = PIDControl
initial_value = 0.0
set_point = set_point:value
input = m_dot_pump
K_p = 1.
K_i = 4.
K_d = 0
[]
[set_pump_head]
type = SetComponentRealValueControl
component = pump
parameter = head
value = pid:output
[]
[m_dot_sec_inlet_ctrl]
type = GetFunctionValueControl
function = m_dot_sec_fn
[]
[set_m_dot_sec_ctrl]
type = SetComponentRealValueControl
component = inlet_sec
parameter = m_dot
value = m_dot_sec_inlet_ctrl:value
[]
[]
[Postprocessors]
[power_to_coolant]
type = ADHeatRateConvection1Phase
block = core_chan
P_hf = '${fparse pi *core_dia}'
[]
[m_dot_pump]
type = ADFlowJunctionFlux1Phase
boundary = core_chan:in
connection_index = 1
equation = mass
junction = jct7
[]
[core_T_out]
type = SideAverageValue
boundary = core_chan:out
variable = T
[]
[core_p_in]
type = SideAverageValue
boundary = core_chan:in
variable = p
[]
[core_p_out]
type = SideAverageValue
boundary = core_chan:out
variable = p
[]
[core_delta_p]
type = ParsedPostprocessor
pp_names = 'core_p_in core_p_out'
expression = 'core_p_in - core_p_out'
[]
[hx_pri_T_out]
type = SideAverageValue
boundary = hx/pri:out
variable = T
[]
[hx_sec_T_in]
type = SideAverageValue
boundary = inlet_sec
variable = T
[]
[hx_sec_T_out]
type = SideAverageValue
boundary = outlet_sec
variable = T
[]
[m_dot_sec]
type = ADFlowBoundaryFlux1Phase
boundary = inlet_sec
equation = mass
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
start_time = 0
[TimeStepper]
type = IterationAdaptiveDT
dt = 1
[]
dtmax = 5
end_time = 500
line_search = basic
solve_type = NEWTON
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_rel_tol = 0
nl_abs_tol = 1e-8
nl_max_its = 25
[]
[Outputs]
exodus = true
[console]
type = Console
max_rows = 1
outlier_variable_norms = false
[]
print_linear_residuals = false
[]
(modules/porous_flow/test/tests/jacobian/esbc02.i)
# Tests the Jacobian of PorousFlowEnthalpySink when pressure
[Mesh]
type = GeneratedMesh
dim = 2
[]
[GlobalParams]
PorousFlowDictator = dictator
at_nodes = true
[]
[UserObjects]
[dictator]
type = PorousFlowDictator
porous_flow_vars = 'pp temp'
number_fluid_phases = 1
number_fluid_components = 1
[]
[pc]
type = PorousFlowCapillaryPressureConst
pc = 0.1
[]
[]
[Variables]
[pp]
initial_condition = 1
[]
[temp]
initial_condition = 2
[]
[]
[AuxVariables]
[pressure]
[]
[]
[Kernels]
[mass0]
type = TimeDerivative
variable = pp
[]
[heat_conduction]
type = TimeDerivative
variable = temp
[]
[]
[FluidProperties]
[simple_fluid]
type = IdealGasFluidProperties
[]
[]
[Materials]
[ppss]
type = PorousFlow1PhaseFullySaturated
porepressure = pp
[]
[simple_fluid]
type = PorousFlowSingleComponentFluid
fp = simple_fluid
phase = 0
[]
[temperature]
type = PorousFlowTemperature
temperature = temp
[]
[]
[BCs]
[left]
type = PorousFlowEnthalpySink
variable = temp
boundary = left
porepressure_var = pressure
T_in = 300
fp = simple_fluid
flux_function = -23
[]
[]
[Preconditioning]
[andy]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
solve_type = Newton
dt = 0.1
num_steps = 1
nl_rel_tol = 1E-12
nl_abs_tol = 1E-12
petsc_options_iname = '-snes_test_err'
petsc_options_value = '1e-1'
[]
(modules/fluid_properties/test/tests/materials/fluid_properties_material/test_ve.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 2
ny = 2
elem_type = QUAD4
[]
[Functions]
[fn_1]
type = ParsedFunction
expression = '2000 + 100*x'
[]
[fn_2]
type = ParsedFunction
expression = '0.02 * (x*x+y*y)'
[]
[]
[AuxVariables]
[e]
[InitialCondition]
type = FunctionIC
function = fn_1
[]
[]
[v]
[InitialCondition]
type = FunctionIC
function = fn_2
[]
[]
[p]
family = MONOMIAL
order = CONSTANT
[]
[T]
family = MONOMIAL
order = CONSTANT
[]
[cp]
family = MONOMIAL
order = CONSTANT
[]
[cv]
family = MONOMIAL
order = CONSTANT
[]
[c]
family = MONOMIAL
order = CONSTANT
[]
[mu]
family = MONOMIAL
order = CONSTANT
[]
[k]
family = MONOMIAL
order = CONSTANT
[]
[s]
family = MONOMIAL
order = CONSTANT
[]
[g]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[p]
type = MaterialRealAux
variable = p
property = pressure
[]
[T]
type = MaterialRealAux
variable = T
property = temperature
[]
[cp]
type = MaterialRealAux
variable = cp
property = cp
[]
[cv]
type = MaterialRealAux
variable = cv
property = cv
[]
[c]
type = MaterialRealAux
variable = c
property = c
[]
[mu]
type = MaterialRealAux
variable = mu
property = mu
[]
[k]
type = MaterialRealAux
variable = k
property = k
[]
[s]
type = MaterialRealAux
variable = s
property = s
[]
[g]
type = MaterialRealAux
variable = g
property = g
[]
[]
[FluidProperties]
[ideal_gas]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 1.000536678700361
[]
[]
[Materials]
[fp_mat]
type = FluidPropertiesMaterialVE
e = e
v = v
fp = ideal_gas
[]
[]
[Executioner]
type = Steady
solve_type = NEWTON
[]
[Problem]
solve = false
[]
[Outputs]
exodus = true
[]
(modules/thermal_hydraulics/test/tests/problems/square_wave/square_wave.i)
# Square wave problem
[GlobalParams]
gravity_vector = '0 0 0'
rdg_slope_reconstruction = minmod
closures = simple_closures
[]
[Functions]
[T_ic_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.1 0.6 1.0'
y = '2.8 1.4 2.8'
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 11.64024372
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[pipe]
type = FlowChannel1Phase
fp = fp
# geometry
position = '0 0 0'
orientation = '1 0 0'
length = 1.0
n_elems = 400
A = 1.0
# IC
initial_T = T_ic_fn
initial_p = 1
initial_vel = 1
f = 0
[]
[left_boundary]
type = FreeBoundary1Phase
input = 'pipe:in'
[]
[right_boundary]
type = FreeBoundary1Phase
input = 'pipe:out'
[]
[]
[Executioner]
type = Transient
[TimeIntegrator]
type = ExplicitSSPRungeKutta
order = 2
[]
solve_type = LINEAR
l_tol = 1e-4
nl_rel_tol = 1e-20
nl_abs_tol = 1e-8
nl_max_its = 60
# run to t = 0.3
start_time = 0.0
dt = 2e-4
num_steps = 1500
abort_on_solve_fail = true
[]
[Outputs]
file_base = 'square_wave'
velocity_as_vector = false
execute_on = 'initial timestep_end'
[out]
type = Exodus
show = 'p T vel'
[]
[]
(modules/thermal_hydraulics/test/tests/problems/sedov_blast_wave/sedov_blast_wave.i)
# This test problem is the Sedov blast wave test problem,
# which is a Riemann problem with the following parameters:
# * domain = (0,1)
# * gravity = 0
# * EoS: Ideal gas EoS with gamma = 1.4, R = 0.71428571428571428571
# * interface: x = 0.5
# * typical end time: 0.15
# Left initial values:
# * rho = 0.445
# * vel = 0.692
# * p = 3.52874226
# Right initial values:
# * rho = 0.5
# * vel = 0
# * p = 0.571
[GlobalParams]
gravity_vector = '0 0 0'
closures = simple_closures
[]
[Functions]
[p_ic_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.0025 1'
y = '1.591549333333333e+06 6.666666666666668e-09'
[]
[T_ic_fn]
type = PiecewiseConstant
axis = x
direction = right
x = '0.0025 1'
y = '2.228169066666667e+06 9.333333333333334e-09'
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.66666666666666666667
molar_mass = 11.64024372
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[pipe]
type = FlowChannel1Phase
fp = fp
# geometry
position = '0 0 0'
orientation = '1 0 0'
length = 1.0
n_elems = 400
A = 1.0
# IC
initial_T = T_ic_fn
initial_p = p_ic_fn
initial_vel = 0
f = 0
[]
[left_boundary]
type = SolidWall1Phase
input = 'pipe:in'
[]
[right_boundary]
type = FreeBoundary1Phase
input = 'pipe:out'
[]
[]
[Executioner]
type = Transient
[TimeIntegrator]
type = ExplicitSSPRungeKutta
order = 2
[]
solve_type = LINEAR
l_tol = 1e-4
nl_rel_tol = 1e-20
nl_abs_tol = 1e-8
nl_max_its = 60
# run to t = 0.005
start_time = 0.0
dt = 1e-6
num_steps = 5000
abort_on_solve_fail = true
[]
[Outputs]
file_base = 'sedov_blast_wave'
velocity_as_vector = false
execute_on = 'initial timestep_end'
[out]
type = Exodus
show = 'p T vel'
[]
[]
(modules/navier_stokes/test/tests/finite_volume/cns/pressure_outlet/subsonic_nozzle_fixed_inflow_hllc.i)
inlet_vel = 120
rho_in = 0.8719748696
H_in = 4.0138771448e+05
gamma = 1.4
R = 8.3145
molar_mass = 29e-3
R_specific = ${fparse R / molar_mass}
cp = ${fparse gamma * R_specific / (gamma - 1)}
cv = ${fparse cp / gamma}
T_in = ${fparse H_in / gamma / cv}
mass_flux = ${fparse inlet_vel * rho_in}
outlet_pressure = 0.9e5
[GlobalParams]
fp = fp
[]
[Debug]
show_material_props = true
[]
[Mesh]
[file]
type = FileMeshGenerator
file = subsonic_nozzle.e
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Variables]
[rho]
family = MONOMIAL
order = CONSTANT
fv = true
initial_condition = 0.8719748696
[]
[rho_u]
family = MONOMIAL
order = CONSTANT
fv = true
initial_condition = 1e-4
[]
[rho_v]
family = MONOMIAL
order = CONSTANT
fv = true
[]
[rho_E]
family = MONOMIAL
order = CONSTANT
fv = true
initial_condition = 2.5e5
[]
[]
[FVKernels]
# Mass conservation
[mass_time]
type = FVTimeKernel
variable = rho
[]
[mass_advection]
type = CNSFVMassHLLC
variable = rho
[]
# Momentum x conservation
[momentum_x_time]
type = FVTimeKernel
variable = rho_u
[]
[momentum_x_advection]
type = CNSFVMomentumHLLC
variable = rho_u
momentum_component = x
[]
# Momentum y conservation
[momentum_y_time]
type = FVTimeKernel
variable = rho_v
[]
[momentum_y_advection]
type = CNSFVMomentumHLLC
variable = rho_v
momentum_component = y
[]
# Fluid energy conservation
[fluid_energy_time]
type = FVTimeKernel
variable = rho_E
[]
[fluid_energy_advection]
type = CNSFVFluidEnergyHLLC
variable = rho_E
[]
[]
[FVBCs]
## inflow boundaries
[mass_inflow]
type = CNSFVHLLCSpecifiedMassFluxAndTemperatureMassBC
variable = rho
boundary = left
rhou = ${mass_flux}
rhov = 0
temperature = ${T_in}
[]
[momentum_x_inflow]
type = CNSFVHLLCSpecifiedMassFluxAndTemperatureMomentumBC
variable = rho_u
boundary = left
rhou = ${mass_flux}
rhov = 0
temperature = ${T_in}
momentum_component = x
[]
[momentum_y_inflow]
type = CNSFVHLLCSpecifiedMassFluxAndTemperatureMomentumBC
variable = rho_v
boundary = left
rhou = ${mass_flux}
rhov = 0
temperature = ${T_in}
momentum_component = y
[]
[fluid_energy_inflow]
type = CNSFVHLLCSpecifiedMassFluxAndTemperatureFluidEnergyBC
variable = rho_E
boundary = left
rhou = ${mass_flux}
rhov = 0
temperature = ${T_in}
[]
## outflow conditions
[mass_outflow]
type = CNSFVHLLCSpecifiedPressureMassBC
variable = rho
boundary = right
pressure = ${outlet_pressure}
[]
[momentum_x_outflow]
type = CNSFVHLLCSpecifiedPressureMomentumBC
variable = rho_u
boundary = right
momentum_component = x
pressure = ${outlet_pressure}
[]
[momentum_y_outflow]
type = CNSFVHLLCSpecifiedPressureMomentumBC
variable = rho_v
boundary = right
momentum_component = y
pressure = ${outlet_pressure}
[]
[fluid_energy_outflow]
type = CNSFVHLLCSpecifiedPressureFluidEnergyBC
variable = rho_E
boundary = right
pressure = ${outlet_pressure}
[]
# wall conditions
[momentum_x_pressure_wall]
type = CNSFVMomImplicitPressureBC
variable = rho_u
momentum_component = x
boundary = wall
[]
[momentum_y_pressure_wall]
type = CNSFVMomImplicitPressureBC
variable = rho_v
momentum_component = y
boundary = wall
[]
[]
[AuxVariables]
[Ma]
family = MONOMIAL
order = CONSTANT
[]
[p]
family = MONOMIAL
order = CONSTANT
[]
[Ma_layered]
family = MONOMIAL
order = CONSTANT
[]
[]
[UserObjects]
[layered_Ma_UO]
type = LayeredAverage
variable = Ma
num_layers = 10
direction = x
[]
[]
[AuxKernels]
[Ma_aux]
type = NSMachAux
variable = Ma
fluid_properties = fp
use_material_properties = true
[]
[p_aux]
type = ADMaterialRealAux
variable = p
property = pressure
[]
[Ma_layered_aux]
type = SpatialUserObjectAux
variable = Ma_layered
user_object = layered_Ma_UO
[]
[]
[Materials]
[var_mat]
type = ConservedVarValuesMaterial
rho = rho
rhou = rho_u
rhov = rho_v
rho_et = rho_E
[]
[sound_speed]
type = SoundspeedMat
[]
[]
[Postprocessors]
[outflow_Ma]
type = SideAverageValue
variable = Ma
boundary = right
[]
[outflow_pressure]
type = SideAverageValue
variable = p
boundary = right
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
[]
[]
[Executioner]
type = Transient
end_time = 10
solve_type = NEWTON
nl_abs_tol = 1e-7
[TimeIntegrator]
type = ImplicitEuler
[]
[TimeStepper]
type = IterationAdaptiveDT
dt = 5e-3
optimal_iterations = 6
growth_factor = 1.5
[]
[]
[VectorPostprocessors]
[Ma_layered]
type = LineValueSampler
variable = Ma_layered
start_point = '0 0 0'
end_point = '3 0 0'
num_points = 100
sort_by = x
warn_discontinuous_face_values = false
[]
[]
[Outputs]
[out]
type = Exodus
execute_on = 'final'
[]
[]
(modules/thermal_hydraulics/test/tests/components/component/err.nonexisting_component.i)
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Components]
[cmp]
type = HeatTransferFromSpecifiedTemperature1Phase
flow_channel = pipe
T_wall = 100
[]
[]
[Problem]
solve = false
[]
[Executioner]
type = Transient
num_steps = 1
[]
(modules/thermal_hydraulics/test/tests/components/gate_valve_1phase/gate_valve_1phase.i)
# This input file is used to test the gate valve component.
# This problem consists of a T junction of 3 pipes. The inlet pipe is one of the
# 2 pipes of the "top" of the T. The other 2 pipes each have a gate valve.
# Initially, one of the 2 outlet pipes has an open valve and the other has a
# closed valve. Later in the transient, the valves gradually open/close to switch
# the outlet flow direction.
p = 1.0e5
T = 300.0
rho = 1.161430436 # @ 1e5 Pa, 300 K
D = 0.1
A = ${fparse pi * D^2 / 4.0}
V_junction = ${fparse pi * D^3 / 4.0}
vel_in = 2.0
m_dot = ${fparse rho * vel_in * A}
t_begin = 0.3
delta_t_open = 0.1
[GlobalParams]
gravity_vector = '0 0 0'
closures = simple_closures
fp = fp
f = 0.0
initial_T = ${T}
initial_p = ${p}
initial_vel = 0
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02897
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Functions]
[pipe3_open_fn]
type = TimeRampFunction
initial_value = 1
final_value = 0
initial_time = ${t_begin}
ramp_duration = ${delta_t_open}
[]
[pipe2_open_fn]
type = ParsedFunction
expression = '1 - pipe3_phi'
symbol_names = 'pipe3_phi'
symbol_values = 'pipe3_open_fn'
[]
[]
[Components]
[inlet]
type = InletMassFlowRateTemperature1Phase
input = 'pipe1:in'
m_dot = ${m_dot}
T = ${T}
[]
[pipe1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 1.0
n_elems = 50
A = ${A}
[]
[volume_junction]
type = VolumeJunction1Phase
position = '1 0 0'
connections = 'pipe1:out pipe2A:in pipe3A:in'
volume = ${V_junction}
initial_vel_x = 0
initial_vel_y = 0
initial_vel_z = 0
[]
[pipe2A]
type = FlowChannel1Phase
position = '1 0 0'
orientation = '0 1 0'
length = 0.5
n_elems = 25
A = ${A}
[]
[pipe2_valve]
type = GateValve1Phase
connections = 'pipe2A:out pipe2B:in'
open_area_fraction = 0 # (controlled via 'pipe2_valve_control')
[]
[pipe2B]
type = FlowChannel1Phase
position = '1 0.5 0'
orientation = '0 1 0'
length = 0.5
n_elems = 25
A = ${A}
[]
[pipe2_outlet]
type = Outlet1Phase
input = 'pipe2B:out'
p = ${p}
[]
[pipe3A]
type = FlowChannel1Phase
position = '1 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = 25
A = ${A}
[]
[pipe3_valve]
type = GateValve1Phase
connections = 'pipe3A:out pipe3B:in'
open_area_fraction = 0 # (controlled via 'pipe3_valve_control')
[]
[pipe3B]
type = FlowChannel1Phase
position = '1.5 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = 25
A = ${A}
[]
[pipe3_outlet]
type = Outlet1Phase
input = 'pipe3B:out'
p = ${p}
[]
[]
[ControlLogic]
[pipe2_valve_control]
type = TimeFunctionComponentControl
component = pipe2_valve
parameter = open_area_fraction
function = pipe2_open_fn
[]
[pipe3_valve_control]
type = TimeFunctionComponentControl
component = pipe3_valve
parameter = open_area_fraction
function = pipe3_open_fn
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
solve_type = PJFNK
nl_rel_tol = 1e-8
nl_abs_tol = 1e-8
nl_max_its = 20
l_tol = 1e-4
start_time = 0.0
end_time = 1.0
dt = 0.01
abort_on_solve_fail = true
[]
[Outputs]
exodus = true
show = 'p T vel'
velocity_as_vector = false
print_linear_residuals = false
[console]
type = Console
max_rows = 1
[]
[]
(modules/fluid_properties/test/tests/tabulated/tabulated_v_e.i)
# Test thermophysical property calculations using TabulatedBiCubic/LinearFluidProperties.
# Calculations for density, internal energy and enthalpy using bicubic or bilinear
# interpolation of data generated using CO2FluidProperties.
[Mesh]
type = GeneratedMesh
dim = 2
# This test uses ElementalVariableValue postprocessors on specific
# elements, so element numbering needs to stay unchanged
allow_renumbering = false
[]
[AuxVariables]
[p]
family = MONOMIAL
order = CONSTANT
[]
[T]
family = MONOMIAL
order = CONSTANT
[]
[mu]
family = MONOMIAL
order = CONSTANT
[]
[s]
family = MONOMIAL
order = CONSTANT
[]
[cv]
family = MONOMIAL
order = CONSTANT
[]
[cp]
family = MONOMIAL
order = CONSTANT
[]
[c]
family = MONOMIAL
order = CONSTANT
[]
[k]
family = MONOMIAL
order = CONSTANT
[]
[g]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[pressure]
type = MaterialRealAux
variable = p
property = pressure
[]
[temperature]
type = MaterialRealAux
variable = T
property = temperature
[]
[viscosity]
type = MaterialRealAux
variable = mu
property = mu
[]
[s]
type = MaterialRealAux
variable = 's'
property = 's'
[]
[cv]
type = MaterialRealAux
variable = cv
property = cv
[]
[cp]
type = MaterialRealAux
variable = cp
property = cp
[]
[c]
type = MaterialRealAux
variable = c
property = c
[]
[thermal_conductivity]
type = MaterialRealAux
variable = k
property = k
[]
[g]
type = MaterialRealAux
variable = g
property = g
[]
[]
[FluidProperties]
[co2]
type = IdealGasFluidProperties
[]
[tabulated]
type = TabulatedBicubicFluidProperties
interpolated_properties = 'density enthalpy viscosity internal_energy k c cv cp entropy'
# Uncomment this to read the tabulation
# fluid_property_file = fluid_properties.csv
# Uncomment this to use the CO2 fluid properties above
# fp = 'co2'
# Uncomment this to write out a tabulation
# fluid_property_output_file = 'fluid_properties.csv'
# Enable the use of the (v,e) variables
construct_pT_from_ve = true
construct_pT_from_vh = true
out_of_bounds_behavior = 'set_to_closest_bound'
# Tabulation range
temperature_min = 280
temperature_max = 600
pressure_min = 1e5
pressure_max = 7e5
# Newton parameters
tolerance = 1e-8
T_initial_guess = 310
p_initial_guess = 1.8e5
[]
[]
[Materials]
[fp_mat_ve]
type = FluidPropertiesMaterialVE
v = 0.03108975251
e = -30797.6
fp = tabulated
[]
[]
[Executioner]
type = Steady
solve_type = NEWTON
[]
[Problem]
solve = false
[]
[Postprocessors]
[p]
type = ElementalVariableValue
elementid = 0
variable = p
[]
[T]
type = ElementalVariableValue
elementid = 0
variable = T
[]
[mu]
type = ElementalVariableValue
elementid = 0
variable = mu
[]
[s]
type = ElementalVariableValue
elementid = 0
variable = s
[]
[cv]
type = ElementalVariableValue
elementid = 0
variable = cv
[]
[cp]
type = ElementalVariableValue
elementid = 0
variable = cp
[]
[c]
type = ElementalVariableValue
elementid = 0
variable = c
[]
[k]
type = ElementalVariableValue
elementid = 0
variable = k
[]
[g]
type = ElementalVariableValue
elementid = 0
variable = g
[]
[]
[Outputs]
csv = true
file_base = tabulated_v_e_bilinear_out
execute_on = 'TIMESTEP_END'
[]
(modules/thermal_hydraulics/test/tests/components/flow_channel_gasmix/flow_channel_gasmix.i)
initial_p = 1e5
initial_T = 500
[FluidProperties]
[fp1]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.029
[]
[fp2]
type = IdealGasFluidProperties
gamma = 1.5
molar_mass = 0.04
[]
[fp_mix]
type = IdealGasMixtureFluidProperties
component_fluid_properties = 'fp1 fp2'
[]
[]
[Closures]
[closures]
type = FunctorClosures
properties = 'f_D mass_diffusion_coefficient'
functors = '0 0.26e-4'
[]
[]
[Functions]
[initial_mass_fraction_fn]
type = PiecewiseConstant
axis = x
x = '0 5.0'
y = '0.2 0.4'
[]
[]
[Components]
[pipe]
type = FlowChannelGasMix
position = '0 0 0'
orientation = '1 0 0'
length = 10.0
n_elems = 50
A = 0.2
initial_mass_fraction = initial_mass_fraction_fn
initial_p = ${initial_p}
initial_T = ${initial_T}
initial_vel = 0
fp = fp_mix
closures = 'closures'
scaling_factor_rhoEA = 1e-5
[]
[inlet]
type = SolidWallGasMix
input = 'pipe:in'
[]
[outlet]
type = SolidWallGasMix
input = 'pipe:out'
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
dt = 1000
num_steps = 5
solve_type = NEWTON
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_rel_tol = 1e-8
nl_abs_tol = 1e-8
nl_max_its = 15
l_tol = 1e-3
l_max_its = 10
[]
[Outputs]
[exodus]
type = Exodus
file_base = flow_channel_gasmix
show = 'mass_fraction p T'
[]
[]
(modules/navier_stokes/test/tests/finite_volume/pwcns/channel-flow/2d-transient-gas.i)
# Fluid properties
mu = 'mu'
rho = 'rho'
k = 'k'
# Solid properties
cp_s = 2
rho_s = 4
k_s = 1e-2
h_fs = 10
# Operating conditions
u_inlet = 1
T_inlet = 200
p_outlet = 10
top_side_temperature = 150
# Numerical scheme
advected_interp_method = 'upwind'
velocity_interp_method = 'rc'
[Mesh]
[gen]
type = GeneratedMeshGenerator
dim = 2
xmin = 0
xmax = 10
ymin = 0
ymax = 1
nx = 20
ny = 5
[]
[]
[GlobalParams]
rhie_chow_user_object = 'rc'
[]
[UserObjects]
[rc]
type = PINSFVRhieChowInterpolator
u = superficial_vel_x
v = superficial_vel_y
pressure = pressure
porosity = porosity
[]
[]
[Variables]
[superficial_vel_x]
type = PINSFVSuperficialVelocityVariable
initial_condition = ${u_inlet}
[]
[superficial_vel_y]
type = PINSFVSuperficialVelocityVariable
[]
[pressure]
type = INSFVPressureVariable
initial_condition = ${p_outlet}
[]
[T_fluid]
type = INSFVEnergyVariable
initial_condition = ${T_inlet}
[]
[T_solid]
type = MooseVariableFVReal
initial_condition = 100
[]
[]
[AuxVariables]
[porosity]
type = MooseVariableFVReal
initial_condition = 0.5
[]
[]
[FVKernels]
[mass_time]
type = PWCNSFVMassTimeDerivative
variable = pressure
porosity = 'porosity'
drho_dt = 'drho_dt'
[]
[mass]
type = PWCNSFVMassAdvection
variable = pressure
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = ${rho}
[]
[u_time]
type = WCNSFVMomentumTimeDerivative
variable = superficial_vel_x
rho = ${rho}
drho_dt = 'drho_dt'
momentum_component = 'x'
[]
[u_advection]
type = PINSFVMomentumAdvection
variable = superficial_vel_x
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = ${rho}
porosity = porosity
momentum_component = 'x'
[]
[u_viscosity]
type = PINSFVMomentumDiffusion
variable = superficial_vel_x
mu = ${mu}
porosity = porosity
momentum_component = 'x'
[]
[u_pressure]
type = PINSFVMomentumPressure
variable = superficial_vel_x
momentum_component = 'x'
pressure = pressure
porosity = porosity
[]
[v_time]
type = WCNSFVMomentumTimeDerivative
variable = superficial_vel_y
rho = ${rho}
drho_dt = 'drho_dt'
momentum_component = 'y'
[]
[v_advection]
type = PINSFVMomentumAdvection
variable = superficial_vel_y
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = ${rho}
porosity = porosity
momentum_component = 'y'
[]
[v_viscosity]
type = PINSFVMomentumDiffusion
variable = superficial_vel_y
mu = ${mu}
porosity = porosity
momentum_component = 'y'
[]
[v_pressure]
type = PINSFVMomentumPressure
variable = superficial_vel_y
momentum_component = 'y'
pressure = pressure
porosity = porosity
[]
[energy_time]
type = PINSFVEnergyTimeDerivative
variable = T_fluid
h = 'h'
dh_dt = 'dh_dt'
rho = ${rho}
drho_dt = 'drho_dt'
is_solid = false
porosity = porosity
[]
[energy_advection]
type = PINSFVEnergyAdvection
variable = T_fluid
velocity_interp_method = ${velocity_interp_method}
advected_interp_method = ${advected_interp_method}
[]
[energy_diffusion]
type = PINSFVEnergyDiffusion
variable = T_fluid
k = ${k}
porosity = porosity
[]
[energy_convection]
type = PINSFVEnergyAmbientConvection
variable = T_fluid
is_solid = false
T_fluid = T_fluid
T_solid = T_solid
h_solid_fluid = 'h_cv'
[]
[solid_energy_time]
type = PINSFVEnergyTimeDerivative
variable = T_solid
cp = ${cp_s}
rho = ${rho_s}
is_solid = true
porosity = porosity
[]
[solid_energy_diffusion]
type = FVDiffusion
variable = T_solid
coeff = ${k_s}
[]
[solid_energy_convection]
type = PINSFVEnergyAmbientConvection
variable = T_solid
is_solid = true
T_fluid = T_fluid
T_solid = T_solid
h_solid_fluid = 'h_cv'
[]
[]
[FVBCs]
[inlet-u]
type = INSFVInletVelocityBC
boundary = 'left'
variable = superficial_vel_x
functor = ${u_inlet}
[]
[inlet-v]
type = INSFVInletVelocityBC
boundary = 'left'
variable = superficial_vel_y
functor = 0
[]
[inlet-T]
type = FVDirichletBC
variable = T_fluid
value = ${T_inlet}
boundary = 'left'
[]
[no-slip-u]
type = INSFVNoSlipWallBC
boundary = 'top'
variable = superficial_vel_x
function = 0
[]
[no-slip-v]
type = INSFVNoSlipWallBC
boundary = 'top'
variable = superficial_vel_y
function = 0
[]
[heated-side]
type = FVDirichletBC
boundary = 'top'
variable = 'T_solid'
value = ${top_side_temperature}
[]
[symmetry-u]
type = PINSFVSymmetryVelocityBC
boundary = 'bottom'
variable = superficial_vel_x
u = superficial_vel_x
v = superficial_vel_y
mu = ${mu}
momentum_component = 'x'
[]
[symmetry-v]
type = PINSFVSymmetryVelocityBC
boundary = 'bottom'
variable = superficial_vel_y
u = superficial_vel_x
v = superficial_vel_y
mu = ${mu}
momentum_component = 'y'
[]
[symmetry-p]
type = INSFVSymmetryPressureBC
boundary = 'bottom'
variable = pressure
[]
[outlet-p]
type = INSFVOutletPressureBC
boundary = 'right'
variable = pressure
function = ${p_outlet}
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
[]
[]
[FunctorMaterials]
[fluid_props_to_mat_props]
type = GeneralFunctorFluidProps
fp = fp
pressure = 'pressure'
T_fluid = 'T_fluid'
speed = 'speed'
# To initialize with a high viscosity
mu_rampdown = 'mu_rampdown'
# For porous flow
characteristic_length = 1
porosity = 'porosity'
[]
[ins_fv]
type = INSFVEnthalpyFunctorMaterial
rho = ${rho}
temperature = 'T_fluid'
[]
[constants]
type = ADGenericFunctorMaterial
prop_names = 'h_cv'
prop_values = '${h_fs}'
[]
[speed]
type = PINSFVSpeedFunctorMaterial
porosity = 'porosity'
superficial_vel_x = 'superficial_vel_x'
superficial_vel_y = 'superficial_vel_y'
[]
[]
[Functions]
[mu_rampdown]
type = PiecewiseLinear
x = '1 2 3 4'
y = '1e3 1e2 1e1 1'
[]
[]
[Executioner]
type = Transient
solve_type = 'NEWTON'
petsc_options_iname = '-pc_type -ksp_gmres_restart -sub_pc_type -sub_pc_factor_shift_type'
petsc_options_value = 'asm 100 lu NONZERO'
line_search = 'none'
nl_rel_tol = 1e-12
nl_abs_tol = 1e-10
automatic_scaling = true
end_time = 3.0
[]
# Some basic Postprocessors to examine the solution
[Postprocessors]
[inlet-p]
type = SideAverageValue
variable = pressure
boundary = 'left'
[]
[outlet-u]
type = VolumetricFlowRate
boundary = 'right'
advected_quantity = '1'
advected_interp_method = ${advected_interp_method}
vel_x = 'superficial_vel_x'
vel_y = 'superficial_vel_y'
[]
[outlet-temp]
type = SideAverageValue
variable = T_fluid
boundary = 'right'
[]
[solid-temp]
type = ElementAverageValue
variable = T_solid
[]
[]
[Outputs]
exodus = true
csv = true
[]
(modules/navier_stokes/test/tests/ics/pns_test.i)
p_initial=1.01e5
T=273.15
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 2
xmin = 0
xmax = 1
ymin = 1
ymax = 2
nx = 4
ny = 4
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Problem]
kernel_coverage_check = false
solve = false
skip_nl_system_check = true
[]
[AuxVariables]
[porosity]
initial_condition = 0.2
[]
[pressure]
type = MooseVariableFVReal
[]
[superficial_vel_x]
type = MooseVariableFVReal
[]
[superficial_vel_y]
type = MooseVariableFVReal
[]
[superficial_vel_z]
type = MooseVariableFVReal
[]
[temperature]
type = MooseVariableFVReal
[]
[vel_x]
type = MooseVariableFVReal
[]
[vel_y]
type = MooseVariableFVReal
[]
[vel_z]
type = MooseVariableFVReal
[]
[superficial_rho_ht]
type = MooseVariableFVReal
[]
[ht]
type = MooseVariableFVReal
[]
[e]
type = MooseVariableFVReal
[]
[Mach]
type = MooseVariableFVReal
[]
[superficial_rho]
type = MooseVariableFVReal
[]
[superficial_rhou]
type = MooseVariableFVReal
[]
[superficial_rhov]
type = MooseVariableFVReal
[]
[superficial_rhow]
type = MooseVariableFVReal
[]
[superficial_rho_et]
type = MooseVariableFVReal
[]
[rho]
type = MooseVariableFVReal
[]
[rhou]
type = MooseVariableFVReal
[]
[rhov]
type = MooseVariableFVReal
[]
[rhow]
type = MooseVariableFVReal
[]
[rho_et]
type = MooseVariableFVReal
[]
[specific_volume]
type = MooseVariableFVReal
[]
[pressure_2]
[]
[superficial_vel_x_2]
[]
[superficial_vel_y_2]
[]
[superficial_vel_z_2]
[]
[vel_x_2]
[]
[vel_y_2]
[]
[vel_z_2]
[]
[temperature_2]
[]
[ht_2]
[]
[superficial_rho_ht_2]
[]
[e_2]
[]
[Mach_2]
[]
[superficial_rho_2]
[]
[superficial_rhou_2]
[]
[superficial_rhov_2]
[]
[superficial_rhow_2]
[]
[superficial_rho_et_2]
[]
[rho_2]
[]
[rhou_2]
[]
[rhov_2]
[]
[rhow_2]
[]
[rho_et_2]
[]
[specific_volume_2]
[]
[]
[GlobalParams]
fluid_properties = 'fp'
initial_pressure = ${p_initial}
initial_temperature = ${T}
initial_superficial_velocity = '1 0.2 18'
porosity = porosity
[]
[ICs]
[p]
type = PNSInitialCondition
variable = 'pressure'
[]
[vel_x]
type = PNSInitialCondition
variable = 'vel_x'
[]
[vel_y]
type = PNSInitialCondition
variable = 'vel_y'
[]
[vel_z]
type = PNSInitialCondition
variable = 'vel_z'
[]
[superficial_vel_x]
type = PNSInitialCondition
variable = 'superficial_vel_x'
[]
[superficial_vel_y]
type = PNSInitialCondition
variable = 'superficial_vel_y'
[]
[superficial_vel_z]
type = PNSInitialCondition
variable = 'superficial_vel_z'
[]
[temperature]
type = PNSInitialCondition
variable = 'temperature'
[]
[ht]
type = PNSInitialCondition
variable = 'ht'
[]
[superficial_rho_ht]
type = PNSInitialCondition
variable = 'superficial_rho_ht'
[]
[e]
type = PNSInitialCondition
variable = 'e'
[]
[Mach]
type = PNSInitialCondition
variable = 'Mach'
[]
[superficial_rho]
type = PNSInitialCondition
variable = 'superficial_rho'
[]
[superficial_rhou]
type = PNSInitialCondition
fluid_properties = 'fp'
initial_pressure = ${p_initial}
initial_temperature = ${T}
initial_superficial_velocity = '1 0.2 18'
porosity = porosity
variable = 'superficial_rhou'
[]
[superficial_rhov]
type = PNSInitialCondition
variable = 'superficial_rhov'
[]
[superficial_rhow]
type = PNSInitialCondition
variable = 'superficial_rhow'
[]
[rho]
type = PNSInitialCondition
variable = 'rho'
[]
[rhou]
type = PNSInitialCondition
variable = 'rhou'
[]
[rhov]
type = PNSInitialCondition
variable = 'rhov'
[]
[rhow]
type = PNSInitialCondition
variable = 'rhow'
[]
[rho_et]
type = PNSInitialCondition
variable = 'rho_et'
[]
[superficial_rho_et]
type = PNSInitialCondition
variable = 'superficial_rho_et'
[]
[specific_volume]
type = PNSInitialCondition
variable = 'specific_volume'
[]
[p_2]
type = PNSInitialCondition
variable = 'pressure_2'
variable_type = 'pressure'
[]
[superficial_vel_x_2]
type = PNSInitialCondition
variable = 'superficial_vel_x_2'
variable_type = 'superficial_vel_x'
[]
[superficial_vel_y_2]
type = PNSInitialCondition
variable = 'superficial_vel_y_2'
variable_type = 'superficial_vel_y'
[]
[superficial_vel_z_2]
type = PNSInitialCondition
variable = 'superficial_vel_z_2'
variable_type = 'superficial_vel_z'
[]
[vel_x_2]
type = PNSInitialCondition
variable = 'vel_x_2'
variable_type = 'vel_x'
[]
[vel_y_2]
type = PNSInitialCondition
variable = 'vel_y_2'
variable_type = 'vel_y'
[]
[vel_z_2]
type = PNSInitialCondition
variable = 'vel_z_2'
variable_type = 'vel_z'
[]
[temperature_2]
type = PNSInitialCondition
variable = 'temperature_2'
variable_type = 'temperature'
[]
[superficial_ht_2]
type = PNSInitialCondition
variable = 'superficial_rho_ht_2'
variable_type = 'superficial_rho_ht'
[]
[ht_2]
type = PNSInitialCondition
variable = 'ht_2'
variable_type = 'ht'
[]
[e_2]
type = PNSInitialCondition
variable = 'e_2'
variable_type = 'e'
[]
[Mach_2]
type = PNSInitialCondition
variable = 'Mach_2'
variable_type = 'Mach'
[]
[superficial_rho_2]
type = PNSInitialCondition
variable = 'superficial_rho_2'
variable_type = 'superficial_rho'
[]
[superficial_rhou_2]
type = PNSInitialCondition
variable = 'superficial_rhou_2'
variable_type = 'superficial_rhou'
[]
[superficial_rhov_2]
type = PNSInitialCondition
variable = 'superficial_rhov_2'
variable_type = 'superficial_rhov'
[]
[superficial_rhow_2]
type = PNSInitialCondition
variable = 'superficial_rhow_2'
variable_type = 'superficial_rhow'
[]
[superficial_rho_et_2]
type = PNSInitialCondition
variable = 'superficial_rho_et_2'
variable_type = 'superficial_rho_et'
[]
[rho_2]
type = PNSInitialCondition
variable = 'rho_2'
variable_type = 'rho'
[]
[rhou_2]
type = PNSInitialCondition
variable = 'rhou_2'
variable_type = 'rhou'
[]
[rhov_2]
type = PNSInitialCondition
variable = 'rhov_2'
variable_type = 'rhov'
[]
[rhow_2]
type = PNSInitialCondition
variable = 'rhow_2'
variable_type = 'rhow'
[]
[rho_et_2]
type = PNSInitialCondition
variable = 'rho_et_2'
variable_type = 'rho_et'
[]
[specific_volume_2]
type = PNSInitialCondition
variable = 'specific_volume_2'
variable_type = 'specific_volume'
[]
[]
[Executioner]
type = Steady
[]
[Outputs]
exodus = true
[]
(modules/fluid_properties/test/tests/functions/saturation_pressure_function/saturation_pressure_function.i)
# TestTwoPhaseFluidProperties has the following saturation pressure function:
# p_sat(p) = 3 T
# Thus for T = 5, p_sat should be 15.
[Mesh]
type = GeneratedMesh
dim = 1
nx = 1
[]
[FluidProperties]
[./fp_liquid]
type = IdealGasFluidProperties
[../]
[./fp_vapor]
type = IdealGasFluidProperties
[../]
[./fp_2phase]
type = TestTwoPhaseFluidProperties
fp_liquid = fp_liquid
fp_vapor = fp_vapor
[../]
[]
[Functions]
[./T]
type = ConstantFunction
value = 5
[../]
[./p_sat]
type = SaturationPressureFunction
T = T
fp_2phase = fp_2phase
[../]
[]
[Postprocessors]
[./p_sat_pp]
type = FunctionValuePostprocessor
function = p_sat
execute_on = 'INITIAL'
[../]
[]
[Problem]
solve = false
[]
[Executioner]
type = Steady
[]
[Outputs]
csv = true
[]
(modules/thermal_hydraulics/test/tests/problems/brayton_cycle/recuperated_brayton_cycle.i)
# This input file models an open, recuperated Brayton cycle with a PID
# controlled start up using a coupled motor.
#
# Heat is supplied to the system by a volumetric heat source, and a second heat
# source is used to model a recuperator. The recuperator transfers heat from the
# turbine exhaust gas to the compressor outlet gas.
#
# Initially the fluid and heat structures are at rest at ambient conditions,
# and the shaft speed is zero.
# The transient is controlled as follows:
# * 0 - 2000 s: Motor increases shaft speed to approx. 85,000 RPM by PID control
# * 1000 - 8600 s: Power in main heat source increases from 0 - 104 kW
# * 2000 - 200000 s: Torque supplied by turbine increases to steady state level
# as working fluid temperature increases. Torque supplied by
# the motor is ramped down to 0 N-m transitioning shaft control
# to the turbine at its rated speed of 96,000 RPM.
I_motor = 1.0
I_generator = 1.0
generator_torque_per_shaft_speed = -0.00025
motor_ramp_up_duration = 3605
motor_ramp_down_duration = 1800
post_motor_time = 2160000
t1 = ${motor_ramp_up_duration}
t2 = ${fparse t1 + motor_ramp_down_duration}
t3 = ${fparse t2 + post_motor_time}
D1 = 0.15
D2 = ${D1}
D3 = ${D1}
D4 = ${D1}
D5 = ${D1}
D6 = ${D1}
D7 = ${D1}
D8 = ${D1}
A1 = ${fparse 0.25 * pi * D1^2}
A2 = ${fparse 0.25 * pi * D2^2}
A3 = ${fparse 0.25 * pi * D3^2}
A4 = ${fparse 0.25 * pi * D4^2}
A5 = ${fparse 0.25 * pi * D5^2}
A6 = ${fparse 0.25 * pi * D6^2}
A7 = ${fparse 0.25 * pi * D7^2}
A8 = ${fparse 0.25 * pi * D8^2}
recuperator_width = 0.15
L1 = 5.0
L2 = ${L1}
L3 = ${fparse 2 * L1}
L4 = ${fparse 2 * L1}
L5 = ${L1}
L6 = ${L1}
L7 = ${fparse L1 + recuperator_width}
L8 = ${L1}
x1 = 0.0
x2 = ${fparse x1 + L1}
x3 = ${fparse x2 + L2}
x4 = ${x3}
x5 = ${fparse x4 - L4}
x6 = ${x5}
x7 = ${fparse x6 + L6}
x8 = ${fparse x7 + L7}
y1 = 0
y2 = ${y1}
y3 = ${y2}
y4 = ${fparse y3 - L3}
y5 = ${y4}
y6 = ${fparse y5 + L5}
y7 = ${y6}
y8 = ${y7}
x1_out = ${fparse x1 + L1 - 0.001}
x2_in = ${fparse x2 + 0.001}
y5_in = ${fparse y5 + 0.001}
x6_out = ${fparse x6 + L6 - 0.001}
x7_in = ${fparse x7 + 0.001}
y8_in = ${fparse y8 + 0.001}
y8_out = ${fparse y8 + L8 - 0.001}
hot_leg_in = ${y8_in}
hot_leg_out = ${y8_out}
cold_leg_in = ${fparse y3 - 0.001}
cold_leg_out = ${fparse y3 - (L3/2) - 0.001}
n_elems1 = 5
n_elems2 = ${n_elems1}
n_elems3 = ${fparse 2 * n_elems1}
n_elems4 = ${fparse 2 * n_elems1}
n_elems5 = ${n_elems1}
n_elems6 = ${n_elems1}
n_elems7 = ${n_elems1}
n_elems8 = ${n_elems1}
A_ref_comp = ${fparse 0.5 * (A1 + A2)}
V_comp = ${fparse A_ref_comp * 1.0}
I_comp = 1.0
A_ref_turb = ${fparse 0.5 * (A4 + A5)}
V_turb = ${fparse A_ref_turb * 1.0}
I_turb = 1.0
c0_rated_comp = 351.6925137
rho0_rated_comp = 1.146881112
rated_mfr = 0.25
speed_rated_rpm = 96000
speed_rated = ${fparse speed_rated_rpm * 2 * pi / 60.0}
speed_initial = 0
eff_comp = 0.79
eff_turb = 0.843
T_ambient = 300
p_ambient = 1e5
hs_power = 105750
[GlobalParams]
gravity_vector = '0 0 0'
initial_p = ${p_ambient}
initial_T = ${T_ambient}
initial_vel = 0
initial_vel_x = 0
initial_vel_y = 0
initial_vel_z = 0
fp = fp_air
closures = closures
f = 0
scaling_factor_1phase = '1 1 1e-5'
scaling_factor_rhoV = 1
scaling_factor_rhouV = 1e-2
scaling_factor_rhovV = 1e-2
scaling_factor_rhowV = 1e-2
scaling_factor_rhoEV = 1e-5
scaling_factor_temperature = 1e-2
rdg_slope_reconstruction = none
[]
[FluidProperties]
[fp_air]
type = IdealGasFluidProperties
emit_on_nan = none
[]
[]
[SolidProperties]
[steel]
type = ThermalFunctionSolidProperties
rho = 8050
k = 45
cp = 466
[]
[]
[Closures]
[closures]
type = Closures1PhaseSimple
[]
[]
[Functions]
##########################
# Motor
##########################
# Functions for control logic that determines when to shut off the PID system
[is_tripped_fn]
type = ParsedFunction
symbol_names = 'motor_torque turbine_torque'
symbol_values = 'motor_torque turbine_torque'
expression = 'turbine_torque > motor_torque'
[]
[PID_tripped_constant_value]
type = ConstantFunction
value = 1
[]
[PID_tripped_status_fn]
type = ParsedFunction
symbol_values = 'PID_trip_status'
symbol_names = 'PID_trip_status'
expression = 'PID_trip_status'
[]
[time_fn]
type = ParsedFunction
expression = t
[]
# Shutdown function which ramps down the motor once told by the control logic
[motor_torque_fn_shutdown]
type = ParsedFunction
symbol_values = 'PID_trip_status time_trip'
symbol_names = 'PID_trip_status time_trip'
expression = 'if(PID_trip_status = 1, max(2.4 - (2.4 * ((t - time_trip) / 35000)),0.0), 1)'
[]
# Generates motor power curve
[motor_power_fn]
type = ParsedFunction
expression = 'torque * speed'
symbol_names = 'torque speed'
symbol_values = 'motor_torque shaft:omega'
[]
##########################
# Generator
##########################
# Generates generator torque curve
[generator_torque_fn]
type = ParsedFunction
expression = 'slope * t'
symbol_names = 'slope'
symbol_values = '${generator_torque_per_shaft_speed}'
[]
# Generates generator power curve
[generator_power_fn]
type = ParsedFunction
expression = 'torque * speed'
symbol_names = 'torque speed'
symbol_values = 'generator_torque shaft:omega'
[]
##########################
# Reactor
##########################
# Ramps up reactor power when activated by control logic
[power_fn]
type = PiecewiseLinear
x = '0 1000 8600'
y = '0 0 ${hs_power}'
[]
##########################
# Compressor
##########################
# compressor pressure ratios
[rp_comp1]
type = PiecewiseLinear
data_file = 'rp_comp1.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_comp2]
type = PiecewiseLinear
data_file = 'rp_comp2.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_comp3]
type = PiecewiseLinear
data_file = 'rp_comp3.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_comp4]
type = PiecewiseLinear
data_file = 'rp_comp4.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_comp5]
type = PiecewiseLinear
data_file = 'rp_comp5.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
# compressor efficiencies
[eff_comp1]
type = ConstantFunction
value = ${eff_comp}
[]
[eff_comp2]
type = ConstantFunction
value = ${eff_comp}
[]
[eff_comp3]
type = ConstantFunction
value = ${eff_comp}
[]
[eff_comp4]
type = ConstantFunction
value = ${eff_comp}
[]
[eff_comp5]
type = ConstantFunction
value = ${eff_comp}
[]
##########################
# Turbine
##########################
# turbine pressure ratios
[rp_turb0]
type = ConstantFunction
value = 1
[]
[rp_turb1]
type = PiecewiseLinear
data_file = 'rp_turb1.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_turb2]
type = PiecewiseLinear
data_file = 'rp_turb2.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_turb3]
type = PiecewiseLinear
data_file = 'rp_turb3.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_turb4]
type = PiecewiseLinear
data_file = 'rp_turb4.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_turb5]
type = PiecewiseLinear
data_file = 'rp_turb5.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
# turbine efficiency
[eff_turb1]
type = ConstantFunction
value = ${eff_turb}
[]
[eff_turb2]
type = ConstantFunction
value = ${eff_turb}
[]
[eff_turb3]
type = ConstantFunction
value = ${eff_turb}
[]
[eff_turb4]
type = ConstantFunction
value = ${eff_turb}
[]
[eff_turb5]
type = ConstantFunction
value = ${eff_turb}
[]
[]
[Components]
# system inlet pulling air from the open atmosphere
[inlet]
type = InletStagnationPressureTemperature1Phase
input = 'pipe1:in'
p0 = ${p_ambient}
T0 = ${T_ambient}
[]
# Inlet pipe
[pipe1]
type = FlowChannel1Phase
position = '${x1} ${y1} 0'
orientation = '1 0 0'
length = ${L1}
n_elems = ${n_elems1}
A = ${A1}
[]
# Compressor as defined in MAGNET PCU document (Guillen 2020)
[compressor]
type = ShaftConnectedCompressor1Phase
position = '${x2} ${y2} 0'
inlet = 'pipe1:out'
outlet = 'pipe2:in'
A_ref = ${A_ref_comp}
volume = ${V_comp}
omega_rated = ${speed_rated}
mdot_rated = ${rated_mfr}
c0_rated = ${c0_rated_comp}
rho0_rated = ${rho0_rated_comp}
# Determines which compression ratio curve and efficiency curve to use depending on ratio of speed/rated_speed
speeds = '0.5208 0.6250 0.7292 0.8333 0.9375'
Rp_functions = 'rp_comp1 rp_comp2 rp_comp3 rp_comp4 rp_comp5'
eff_functions = 'eff_comp1 eff_comp2 eff_comp3 eff_comp4 eff_comp5'
min_pressure_ratio = 1.0
speed_cr_I = 0
inertia_const = ${I_comp}
inertia_coeff = '${I_comp} 0 0 0'
# assume no shaft friction
speed_cr_fr = 0
tau_fr_const = 0
tau_fr_coeff = '0 0 0 0'
[]
# Outlet pipe from the compressor
[pipe2]
type = FlowChannel1Phase
position = '${x2} ${y2} 0'
orientation = '1 0 0'
length = ${L2}
n_elems = ${n_elems2}
A = ${A2}
[]
# 90 degree connection between pipe 2 and 3
[junction2_cold_leg]
type = VolumeJunction1Phase
connections = 'pipe2:out cold_leg:in'
position = '${x3} ${y3} 0'
volume = ${fparse A2*0.1}
[]
# Cold leg of the recuperator
[cold_leg]
type = FlowChannel1Phase
position = '${x3} ${y3} 0'
orientation = '0 -1 0'
length = ${fparse L3/2}
n_elems = ${fparse n_elems3/2}
A = ${A3}
[]
# Recuperator which transfers heat from exhaust gas to reactor inlet gas to improve thermal efficency
[recuperator]
type = HeatStructureCylindrical
orientation = '0 -1 0'
position = '${x3} ${y3} 0'
length = ${fparse L3/2}
widths = ${recuperator_width}
n_elems = ${fparse n_elems3/2}
n_part_elems = 2
names = recuperator
solid_properties = steel
solid_properties_T_ref = '300'
inner_radius = ${D1}
[]
# heat transfer from recuperator to cold leg
[heat_transfer_cold_leg]
type = HeatTransferFromHeatStructure1Phase
flow_channel = cold_leg
hs = recuperator
hs_side = OUTER
Hw = 10000
[]
# heat transfer from hot leg to recuperator
[heat_transfer_hot_leg]
type = HeatTransferFromHeatStructure1Phase
flow_channel = hot_leg
hs = recuperator
hs_side = INNER
Hw = 10000
[]
[junction_cold_leg_3]
type = JunctionOneToOne1Phase
connections = 'cold_leg:out pipe3:in'
[]
[pipe3]
type = FlowChannel1Phase
position = '${x3} ${fparse y3 - (L3/2)} 0'
orientation = '0 -1 0'
length = ${fparse L3/2}
n_elems = ${fparse n_elems3/2}
A = ${A3}
[]
# 90 degree connection between pipe 3 and 4
[junction3_4]
type = VolumeJunction1Phase
connections = 'pipe3:out pipe4:in'
position = '${x4} ${y4} 0'
volume = ${fparse A3*0.1}
[]
# Pipe through the "reactor core"
[pipe4]
type = FlowChannel1Phase
position = '${x4} ${y4} 0'
orientation = '-1 0 0'
length = ${L4}
n_elems = ${n_elems4}
A = ${A4}
[]
# "Reactor Core" and it's associated heat transfer to pipe 4
[reactor]
type = HeatStructureCylindrical
orientation = '-1 0 0'
position = '${x4} ${y4} 0'
length = ${L4}
widths = 0.15
n_elems = ${n_elems4}
n_part_elems = 2
names = core
solid_properties = steel
solid_properties_T_ref = '300'
[]
[total_power]
type = TotalPower
power = 0
[]
[heat_generation]
type = HeatSourceFromTotalPower
power = total_power
hs = reactor
regions = core
[]
[heat_transfer]
type = HeatTransferFromHeatStructure1Phase
flow_channel = pipe4
hs = reactor
hs_side = OUTER
Hw = 10000
[]
# 90 degree connection between pipe 4 and 5
[junction4_5]
type = VolumeJunction1Phase
connections = 'pipe4:out pipe5:in'
position = '${x5} ${y5} 0'
volume = ${fparse A4*0.1}
[]
# Pipe carrying hot gas back to the PCU
[pipe5]
type = FlowChannel1Phase
position = '${x5} ${y5} 0'
orientation = '0 1 0'
length = ${L5}
n_elems = ${n_elems5}
A = ${A5}
[]
# 90 degree connection between pipe 5 and 6
[junction5_6]
type = VolumeJunction1Phase
connections = 'pipe5:out pipe6:in'
position = '${x6} ${y6} 0'
volume = ${fparse A5*0.1}
[]
# Inlet pipe to the turbine
[pipe6]
type = FlowChannel1Phase
position = '${x6} ${y6} 0'
orientation = '1 0 0'
length = ${L6}
n_elems = ${n_elems6}
A = ${A6}
[]
# Turbine as defined in MAGNET PCU document (Guillen 2020) and (Wright 2006)
[turbine]
type = ShaftConnectedCompressor1Phase
position = '${x7} ${y7} 0'
inlet = 'pipe6:out'
outlet = 'pipe7:in'
A_ref = ${A_ref_turb}
volume = ${V_turb}
# A turbine is treated as an "inverse" compressor, this value determines if component is to be treated as turbine or compressor
# If treat_as_turbine is omitted, code automatically assumes it is a compressor
treat_as_turbine = true
omega_rated = ${speed_rated}
mdot_rated = ${rated_mfr}
c0_rated = ${c0_rated_comp}
rho0_rated = ${rho0_rated_comp}
# Determines which compression ratio curve and efficiency curve to use depending on ratio of speed/rated_speed
speeds = '0 0.5208 0.6250 0.7292 0.8333 0.9375'
Rp_functions = 'rp_turb0 rp_turb1 rp_turb2 rp_turb3 rp_turb4 rp_turb5'
eff_functions = 'eff_turb1 eff_turb1 eff_turb2 eff_turb3 eff_turb4 eff_turb5'
min_pressure_ratio = 1.0
speed_cr_I = 0
inertia_const = ${I_turb}
inertia_coeff = '${I_turb} 0 0 0'
# assume no shaft friction
speed_cr_fr = 0
tau_fr_const = 0
tau_fr_coeff = '0 0 0 0'
[]
# Outlet pipe from turbine
[pipe7]
type = FlowChannel1Phase
position = '${x7} ${y7} 0'
orientation = '1 0 0'
length = ${L7}
n_elems = ${n_elems7}
A = ${A7}
[]
# 90 degree connection between pipe 7 and 8
[junction7_hot_leg]
type = VolumeJunction1Phase
connections = 'pipe7:out hot_leg:in'
position = '${x8} ${y8} 0'
volume = ${fparse A7*0.1}
[]
# Hot leg of the recuperator
[hot_leg]
type = FlowChannel1Phase
position = '${x8} ${y8} 0'
orientation = '0 1 0'
length = ${L8}
n_elems = ${n_elems8}
A = ${A8}
[]
# System outlet dumping exhaust gas to the atmosphere
[outlet]
type = Outlet1Phase
input = 'hot_leg:out'
p = ${p_ambient}
[]
# Roatating shaft connecting motor, compressor, turbine, and generator
[shaft]
type = Shaft
connected_components = 'motor compressor turbine generator'
initial_speed = ${speed_initial}
[]
# 3-Phase electircal motor used for system start-up, controlled by PID
[motor]
type = ShaftConnectedMotor
inertia = ${I_motor}
torque = 0 # controlled
[]
# Electric generator supplying power to the grid
[generator]
type = ShaftConnectedMotor
inertia = ${I_generator}
torque = generator_torque_fn
[]
[]
# Control logics which govern startup of the motor, startup of the "reactor core", and shutdown of the motor
[ControlLogic]
# Sets desired shaft speed to be reached by motor NOTE: SHOULD BE SET LOWER THAN RATED TURBINE RPM
[set_point]
type = GetFunctionValueControl
function = ${fparse speed_rated_rpm - 9000}
[]
# PID with gains determined by iterative process NOTE: Gain values are system specific
[initial_motor_PID]
type = PIDControl
set_point = set_point:value
input = shaft_RPM
initial_value = 0
K_p = 0.0011
K_i = 0.00000004
K_d = 0
[]
# Determines when the PID system should be running and when it should begin the shutdown cycle. If needed: PID output, else: shutdown function
[logic]
type = ParsedFunctionControl
function = 'if(motor+0.5 > turb, PID, shutdown_fn)'
symbol_names = 'motor turb PID shutdown_fn'
symbol_values = 'motor_torque turbine_torque initial_motor_PID:output motor_torque_fn_shutdown'
[]
# Takes the output generated in [logic] and applies it to the motor torque
[motor_PID]
type = SetComponentRealValueControl
component = motor
parameter = torque
value = logic:value
[]
# Determines when to turn on heat source
[power_logic]
type = ParsedFunctionControl
function = 'power_fn'
symbol_names = 'power_fn'
symbol_values = 'power_fn'
[]
# Applies heat source to the total_power block
[power_applied]
type = SetComponentRealValueControl
component = total_power
parameter = power
value = power_logic:value
[]
[]
[Controls]
# Enables set_PID_tripped
[PID_trip_status]
type = ConditionalFunctionEnableControl
conditional_function = is_tripped_fn
enable_objects = 'AuxScalarKernels::PID_trip_status_aux'
execute_on = 'TIMESTEP_END'
[]
# Enables set_time_PID
[time_PID]
type = ConditionalFunctionEnableControl
conditional_function = PID_tripped_status_fn
disable_objects = 'AuxScalarKernels::time_trip_aux'
execute_on = 'TIMESTEP_END'
[]
[]
[AuxVariables]
# Creates a variable that will later be set to the time when tau_turbine > tau_motor
[time_trip]
order = FIRST
family = SCALAR
[]
# Creates variable which indicates if tau_turbine > tau_motor....... If tau_motor > tau_turbine, 0, else 1
[PID_trip_status]
order = FIRST
family = SCALAR
initial_condition = 0
[]
[]
[AuxScalarKernels]
# Creates variable from time_fn which indicates when tau_turbine > tau_motor
[time_trip_aux]
type = FunctionScalarAux
function = time_fn
variable = time_trip
execute_on = 'TIMESTEP_END'
[]
# Overwrites variable PID_trip_status to the value from PID_tripped_constant_value (changes 0 to 1)
[PID_trip_status_aux]
type = FunctionScalarAux
function = PID_tripped_constant_value
variable = PID_trip_status
execute_on = 'TIMESTEP_END'
enable = false
[]
[]
[Postprocessors]
# Indicates when tau_turbine > tau_motor
[trip_time]
type = ScalarVariable
variable = time_trip
execute_on = 'TIMESTEP_END'
[]
##########################
# Motor
##########################
[motor_torque]
type = RealComponentParameterValuePostprocessor
component = motor
parameter = torque
execute_on = 'INITIAL TIMESTEP_END'
[]
[motor_power]
type = FunctionValuePostprocessor
function = motor_power_fn
execute_on = 'INITIAL TIMESTEP_END'
[]
##########################
# generator
##########################
[generator_torque]
type = ShaftConnectedComponentPostprocessor
quantity = torque
shaft_connected_component_uo = generator:shaftconnected_uo
execute_on = 'INITIAL TIMESTEP_END'
[]
[generator_power]
type = FunctionValuePostprocessor
function = generator_power_fn
execute_on = 'INITIAL TIMESTEP_END'
[]
##########################
# Shaft
##########################
# Speed in rad/s
[shaft_speed]
type = ScalarVariable
variable = 'shaft:omega'
execute_on = 'INITIAL TIMESTEP_END'
[]
# speed in RPM
[shaft_RPM]
type = ParsedPostprocessor
pp_names = 'shaft_speed'
expression = '(shaft_speed * 60) /( 2 * ${fparse pi})'
execute_on = 'INITIAL TIMESTEP_END'
[]
##########################
# Compressor
##########################
[comp_dissipation_torque]
type = ElementAverageValue
variable = dissipation_torque
block = 'compressor'
execute_on = 'INITIAL TIMESTEP_END'
[]
[comp_isentropic_torque]
type = ElementAverageValue
variable = isentropic_torque
block = 'compressor'
execute_on = 'INITIAL TIMESTEP_END'
[]
[comp_friction_torque]
type = ElementAverageValue
variable = friction_torque
block = 'compressor'
execute_on = 'INITIAL TIMESTEP_END'
[]
[compressor_torque]
type = ParsedPostprocessor
pp_names = 'comp_dissipation_torque comp_isentropic_torque comp_friction_torque'
expression = 'comp_dissipation_torque + comp_isentropic_torque + comp_friction_torque'
[]
[p_in_comp]
type = PointValue
variable = p
point = '${x1_out} ${y1} 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_out_comp]
type = PointValue
variable = p
point = '${x2_in} ${y2} 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_ratio_comp]
type = ParsedPostprocessor
pp_names = 'p_in_comp p_out_comp'
expression = 'p_out_comp / p_in_comp'
execute_on = 'INITIAL TIMESTEP_END'
[]
[T_in_comp]
type = PointValue
variable = T
point = '${x1_out} ${y1} 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[T_out_comp]
type = PointValue
variable = T
point = '${x2_in} ${y2} 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[T_ratio_comp]
type = ParsedPostprocessor
pp_names = 'T_in_comp T_out_comp'
expression = '(T_out_comp - T_in_comp) / T_out_comp'
execute_on = 'INITIAL TIMESTEP_END'
[]
[mfr_comp]
type = ADFlowJunctionFlux1Phase
boundary = pipe1:out
connection_index = 0
equation = mass
junction = compressor
[]
##########################
# turbine
##########################
[turb_dissipation_torque]
type = ElementAverageValue
variable = dissipation_torque
block = 'turbine'
execute_on = 'INITIAL TIMESTEP_END'
[]
[turb_isentropic_torque]
type = ElementAverageValue
variable = isentropic_torque
block = 'turbine'
execute_on = 'INITIAL TIMESTEP_END'
[]
[turb_friction_torque]
type = ElementAverageValue
variable = friction_torque
block = 'turbine'
execute_on = 'INITIAL TIMESTEP_END'
[]
[turbine_torque]
type = ParsedPostprocessor
pp_names = 'turb_dissipation_torque turb_isentropic_torque turb_friction_torque'
expression = 'turb_dissipation_torque + turb_isentropic_torque + turb_friction_torque'
[]
[p_in_turb]
type = PointValue
variable = p
point = '${x6_out} ${y6} 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_out_turb]
type = PointValue
variable = p
point = '${x7_in} ${y7} 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_ratio_turb]
type = ParsedPostprocessor
pp_names = 'p_in_turb p_out_turb'
expression = 'p_in_turb / p_out_turb'
execute_on = 'INITIAL TIMESTEP_END'
[]
[T_in_turb]
type = PointValue
variable = T
point = '${x6_out} ${y6} 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[T_out_turb]
type = PointValue
variable = T
point = '${x7_in} ${y7} 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[mfr_turb]
type = ADFlowJunctionFlux1Phase
boundary = pipe6:out
connection_index = 0
equation = mass
junction = turbine
[]
##########################
# Recuperator
##########################
[cold_leg_in]
type = PointValue
variable = T
point = '${x3} ${cold_leg_in} 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[cold_leg_out]
type = PointValue
variable = T
point = '${x3} ${cold_leg_out} 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[hot_leg_in]
type = PointValue
variable = T
point = '${x8} ${hot_leg_in} 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[hot_leg_out]
type = PointValue
variable = T
point = '${x8} ${hot_leg_out} 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
##########################
# Reactor
##########################
[reactor_inlet]
type = PointValue
variable = T
point = '${x4} ${y4} 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[reactor_outlet]
type = PointValue
variable = T
point = '${x5} ${y5_in} 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[]
[Executioner]
type = Transient
scheme = 'bdf2'
end_time = ${t3}
[TimeStepper]
type = IterationAdaptiveDT
dt = 0.01
growth_factor = 1.1
cutback_factor = 0.9
[]
dtmin = 1e-5
dtmax = 1000
steady_state_detection = true
steady_state_start_time = 200000
solve_type = NEWTON
nl_rel_tol = 1e-8
nl_abs_tol = 1e-8
nl_max_its = 15
l_tol = 1e-4
l_max_its = 10
petsc_options_iname = '-pc_type'
petsc_options_value = ' lu '
[]
[Outputs]
[e]
type = Exodus
file_base = 'recuperated_brayton_cycle_out'
[]
[csv]
type = CSV
file_base = 'recuperated_brayton_cycle'
execute_vector_postprocessors_on = 'INITIAL'
[]
[console]
type = Console
show = 'shaft_speed p_ratio_comp p_ratio_turb pressure_ratio pressure_ratio'
[]
[]
(modules/navier_stokes/test/tests/finite_volume/cns/userobject/HLLC/hllc_uo_1D.i)
rho_left = 1.162633159
E_left = 2.1502913276e+05
u_left = 100
rho_right = 1.116127833
E_right = 1.7919094397e+05
u_right = 90
[Mesh]
allow_renumbering = false
[./cartesian]
type = GeneratedMeshGenerator
dim = 1
xmin = 0
xmax = 1
nx = 2
[../]
[]
[FluidProperties]
[./fp]
type = IdealGasFluidProperties
allow_imperfect_jacobians = true
[../]
[]
[Problem]
kernel_coverage_check = false
[]
[Variables]
[./rho]
order = CONSTANT
family = MONOMIAL
[../]
[./rho_u]
order = CONSTANT
family = MONOMIAL
[../]
[./rho_E]
order = CONSTANT
family = MONOMIAL
[../]
[]
[ICs]
[./rho_ic]
type = FunctionIC
variable = rho
function = 'if (x < 0.5, ${rho_left}, ${rho_right})'
[../]
[./rho_u_ic]
type = FunctionIC
variable = rho_u
function = 'if (x < 0.5, ${fparse rho_left * u_left}, ${fparse rho_right * u_right})'
[../]
[./rho_E_ic]
type = FunctionIC
variable = rho_E
function = 'if (x < 0.5, ${fparse E_left * rho_left}, ${fparse E_right * rho_right})'
[../]
[]
[Materials]
[./var_mat]
type = ConservedVarValuesMaterial
rho = rho
rhou = rho_u
rho_et = rho_E
fp = fp
[../]
[]
[UserObjects]
[./hllc]
type = HLLCUserObject
fp = fp
[../]
[]
[VectorPostprocessors]
[./wave_speeds]
type = WaveSpeedVPP
hllc_uo = hllc
elem_id = 0
side_id = 1
[../]
[]
[Executioner]
type = Steady
[]
[Outputs]
csv = true
[]
(modules/thermal_hydraulics/test/tests/components/flow_connection/err.connection_format.i)
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 28.964e-3
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[left_wall]
type = SolidWall1Phase
[]
[pipe]
type = FlowChannel1Phase
fp = fp
closures = simple_closures
position = '0 0 0'
orientation = '1 0 0'
length = 1.0
n_elems = 5
A = 1.0
initial_T = 300
initial_p = 1e5
initial_vel = 0
f = 0
[]
[right_wall]
type = SolidWall1Phase
input = 'pipe:out'
[]
[]
[Executioner]
type = Transient
scheme = 'bdf2'
nl_rel_tol = 0
nl_abs_tol = 1e-6
nl_max_its = 15
l_tol = 1e-3
l_max_its = 10
start_time = 0.0
dt = 0.01
num_steps = 1
abort_on_solve_fail = true
[Quadrature]
type = GAUSS
order = SECOND
[]
[]
(modules/thermal_hydraulics/test/tests/problems/brayton_cycle/closed_brayton_cycle.i)
# This input file is used to demonstrate a simple closed, air Brayton cycle using
# a compressor, turbine, shaft, motor, and generator.
# The flow length is divided into 6 segments as illustrated below, where
# - "(C)" denotes the compressor
# - "(T)" denotes the turbine
# - "*" denotes a fictitious junction
#
# Heated section Cooled section
# *-----(C)-----*--------------*-----(T)-----*--------------*
# 1 2 3 4 5 6
#
# Initially the fluid is at rest at ambient conditions, the shaft speed is zero,
# and no heat transfer occurs with the system.
# The transient is controlled as follows:
# * 0 - 100 s: motor ramps up torque linearly from zero
# * 100 - 200 s: motor ramps down torque linearly to zero, HTC ramps up linearly from zero.
# * 200 - 300 s: (no changes; should approach steady condition)
I_motor = 1.0
motor_torque_max = 400.0
I_generator = 1.0
generator_torque_per_shaft_speed = -0.00025
motor_ramp_up_duration = 100.0
motor_ramp_down_duration = 100.0
post_motor_time = 100.0
t1 = ${motor_ramp_up_duration}
t2 = ${fparse t1 + motor_ramp_down_duration}
t3 = ${fparse t2 + post_motor_time}
D1 = 0.15
D2 = ${D1}
D3 = ${D1}
D4 = ${D1}
D5 = ${D1}
D6 = ${D1}
A1 = ${fparse 0.25 * pi * D1^2}
A2 = ${fparse 0.25 * pi * D2^2}
A3 = ${fparse 0.25 * pi * D3^2}
A4 = ${fparse 0.25 * pi * D4^2}
A5 = ${fparse 0.25 * pi * D5^2}
A6 = ${fparse 0.25 * pi * D6^2}
L1 = 10.0
L2 = ${L1}
L3 = ${L1}
L4 = ${L1}
L5 = ${L1}
L6 = ${L1}
x1 = 0.0
x2 = ${fparse x1 + L1}
x3 = ${fparse x2 + L2}
x4 = ${fparse x3 + L3}
x5 = ${fparse x4 + L4}
x6 = ${fparse x5 + L5}
x2_minus = ${fparse x2 - 0.001}
x2_plus = ${fparse x2 + 0.001}
x5_minus = ${fparse x5 - 0.001}
x5_plus = ${fparse x5 + 0.001}
n_elems1 = 10
n_elems2 = ${n_elems1}
n_elems3 = ${n_elems1}
n_elems4 = ${n_elems1}
n_elems5 = ${n_elems1}
n_elems6 = ${n_elems1}
A_ref_comp = ${fparse 0.5 * (A1 + A2)}
V_comp = ${fparse A_ref_comp * 1.0}
I_comp = 1.0
A_ref_turb = ${fparse 0.5 * (A4 + A5)}
V_turb = ${fparse A_ref_turb * 1.0}
I_turb = 1.0
c0_rated_comp = 351.6925137
rho0_rated_comp = 1.146881112
rated_mfr = 0.25
speed_rated_rpm = 96000
speed_rated = ${fparse speed_rated_rpm * 2 * pi / 60.0}
speed_initial = 0
eff_comp = 0.79
eff_turb = 0.843
T_hot = 1000
T_cold = 300
T_ambient = 300
p_ambient = 1e5
[GlobalParams]
orientation = '1 0 0'
gravity_vector = '0 0 0'
initial_p = ${p_ambient}
initial_T = ${T_ambient}
initial_vel = 0
initial_vel_x = 0
initial_vel_y = 0
initial_vel_z = 0
fp = fp_air
closures = closures
f = 0
scaling_factor_1phase = '1 1 1e-5'
scaling_factor_rhoV = 1
scaling_factor_rhouV = 1
scaling_factor_rhovV = 1
scaling_factor_rhowV = 1
scaling_factor_rhoEV = 1e-5
rdg_slope_reconstruction = none
[]
[Functions]
[motor_torque_fn]
type = PiecewiseLinear
x = '0 ${t1} ${t2}'
y = '0 ${motor_torque_max} 0'
[]
[motor_power_fn]
type = ParsedFunction
expression = 'torque * speed'
symbol_names = 'torque speed'
symbol_values = 'motor_torque shaft:omega'
[]
[generator_torque_fn]
type = ParsedFunction
expression = 'slope * t'
symbol_names = 'slope'
symbol_values = '${generator_torque_per_shaft_speed}'
[]
[generator_power_fn]
type = ParsedFunction
expression = 'torque * speed'
symbol_names = 'torque speed'
symbol_values = 'generator_torque shaft:omega'
[]
[htc_wall_fn]
type = PiecewiseLinear
x = '0 ${t1} ${t2}'
y = '0 0 1e3'
[]
[]
[FluidProperties]
[fp_air]
type = IdealGasFluidProperties
emit_on_nan = none
[]
[]
[Closures]
[closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[shaft]
type = Shaft
connected_components = 'motor compressor turbine generator'
initial_speed = ${speed_initial}
scaling_factor_omega = 1e-3
[]
[motor]
type = ShaftConnectedMotor
inertia = ${I_motor}
torque = 0 # controlled
[]
[generator]
type = ShaftConnectedMotor
inertia = ${I_generator}
torque = generator_torque_fn
[]
[pipe1]
type = FlowChannel1Phase
position = '${x1} 0 0'
length = ${L1}
n_elems = ${n_elems1}
A = ${A1}
[]
[compressor]
type = ShaftConnectedCompressor1Phase
position = '${x2} 0 0'
inlet = 'pipe1:out'
outlet = 'pipe2:in'
A_ref = ${A_ref_comp}
volume = ${V_comp}
omega_rated = ${speed_rated}
mdot_rated = ${rated_mfr}
c0_rated = ${c0_rated_comp}
rho0_rated = ${rho0_rated_comp}
speeds = '0.5208 0.6250 0.7292 0.8333 0.9375'
Rp_functions = 'rp_comp1 rp_comp2 rp_comp3 rp_comp4 rp_comp5'
eff_functions = 'eff_comp1 eff_comp2 eff_comp3 eff_comp4 eff_comp5'
min_pressure_ratio = 1.0
speed_cr_I = 0
inertia_const = ${I_comp}
inertia_coeff = '${I_comp} 0 0 0'
# assume no shaft friction
speed_cr_fr = 0
tau_fr_const = 0
tau_fr_coeff = '0 0 0 0'
[]
[pipe2]
type = FlowChannel1Phase
position = '${x2} 0 0'
length = ${L2}
n_elems = ${n_elems2}
A = ${A2}
[]
[junction2_3]
type = JunctionOneToOne1Phase
connections = 'pipe2:out pipe3:in'
[]
[pipe3]
type = FlowChannel1Phase
position = '${x3} 0 0'
length = ${L3}
n_elems = ${n_elems3}
A = ${A3}
[]
[junction3_4]
type = JunctionOneToOne1Phase
connections = 'pipe3:out pipe4:in'
[]
[pipe4]
type = FlowChannel1Phase
position = '${x4} 0 0'
length = ${L4}
n_elems = ${n_elems4}
A = ${A4}
[]
[turbine]
type = ShaftConnectedCompressor1Phase
position = '${x5} 0 0'
inlet = 'pipe4:out'
outlet = 'pipe5:in'
A_ref = ${A_ref_turb}
volume = ${V_turb}
treat_as_turbine = true
omega_rated = ${speed_rated}
mdot_rated = ${rated_mfr}
c0_rated = ${c0_rated_comp}
rho0_rated = ${rho0_rated_comp}
speeds = '0 0.5208 0.6250 0.7292 0.8333 0.9375'
Rp_functions = 'rp_turb0 rp_turb1 rp_turb2 rp_turb3 rp_turb4 rp_turb5'
eff_functions = 'eff_turb1 eff_turb1 eff_turb2 eff_turb3 eff_turb4 eff_turb5'
min_pressure_ratio = 1.0
speed_cr_I = 0
inertia_const = ${I_turb}
inertia_coeff = '${I_turb} 0 0 0'
# assume no shaft friction
speed_cr_fr = 0
tau_fr_const = 0
tau_fr_coeff = '0 0 0 0'
[]
[pipe5]
type = FlowChannel1Phase
position = '${x5} 0 0'
length = ${L5}
n_elems = ${n_elems5}
A = ${A5}
[]
[junction5_6]
type = JunctionOneToOne1Phase
connections = 'pipe5:out pipe6:in'
[]
[pipe6]
type = FlowChannel1Phase
position = '${x6} 0 0'
length = ${L6}
n_elems = ${n_elems6}
A = ${A6}
[]
[junction6_1]
type = JunctionOneToOne1Phase
connections = 'pipe6:out pipe1:in'
[]
[heating]
type = HeatTransferFromSpecifiedTemperature1Phase
flow_channel = pipe3
T_wall = ${T_hot}
Hw = htc_wall_fn
[]
[cooling]
type = HeatTransferFromSpecifiedTemperature1Phase
flow_channel = pipe6
T_wall = ${T_cold}
Hw = htc_wall_fn
[]
[]
[ControlLogic]
[motor_ctrl]
type = TimeFunctionComponentControl
component = motor
parameter = torque
function = motor_torque_fn
[]
[]
[Postprocessors]
[heating_rate]
type = ADHeatRateConvection1Phase
block = 'pipe3'
T = T
T_wall = T_wall
Hw = Hw
P_hf = P_hf
execute_on = 'INITIAL TIMESTEP_END'
[]
[cooling_rate]
type = ADHeatRateConvection1Phase
block = 'pipe6'
T = T
T_wall = T_wall
Hw = Hw
P_hf = P_hf
execute_on = 'INITIAL TIMESTEP_END'
[]
[motor_torque]
type = RealComponentParameterValuePostprocessor
component = motor
parameter = torque
execute_on = 'INITIAL TIMESTEP_END'
[]
[motor_power]
type = FunctionValuePostprocessor
function = motor_power_fn
execute_on = 'INITIAL TIMESTEP_END'
indirect_dependencies = 'motor_torque shaft:omega'
[]
[generator_torque]
type = ShaftConnectedComponentPostprocessor
quantity = torque
shaft_connected_component_uo = generator:shaftconnected_uo
execute_on = 'INITIAL TIMESTEP_END'
[]
[generator_power]
type = FunctionValuePostprocessor
function = generator_power_fn
execute_on = 'INITIAL TIMESTEP_END'
indirect_dependencies = 'generator_torque shaft:omega'
[]
[shaft_speed]
type = ScalarVariable
variable = 'shaft:omega'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_in_comp]
type = PointValue
variable = p
point = '${x2_minus} 0 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_out_comp]
type = PointValue
variable = p
point = '${x2_plus} 0 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_ratio_comp]
type = ParsedPostprocessor
pp_names = 'p_in_comp p_out_comp'
expression = 'p_out_comp / p_in_comp'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_in_turb]
type = PointValue
variable = p
point = '${x5_minus} 0 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_out_turb]
type = PointValue
variable = p
point = '${x5_plus} 0 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_ratio_turb]
type = ParsedPostprocessor
pp_names = 'p_in_turb p_out_turb'
expression = 'p_in_turb / p_out_turb'
execute_on = 'INITIAL TIMESTEP_END'
[]
[mfr_comp]
type = ADFlowJunctionFlux1Phase
boundary = pipe1:out
connection_index = 0
equation = mass
junction = compressor
[]
[mfr_turb]
type = ADFlowJunctionFlux1Phase
boundary = pipe4:out
connection_index = 0
equation = mass
junction = turbine
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'bdf2'
end_time = ${t3}
dt = 0.1
solve_type = NEWTON
nl_rel_tol = 1e-50
nl_abs_tol = 1e-10
nl_max_its = 15
l_tol = 1e-4
l_max_its = 10
[]
[Outputs]
[csv]
type = CSV
file_base = 'closed_brayton_cycle'
execute_vector_postprocessors_on = 'INITIAL'
[]
[console]
type = Console
show = 'shaft_speed p_ratio_comp p_ratio_turb compressor:pressure_ratio turbine:pressure_ratio'
[]
[]
[Functions]
# compressor pressure ratio
[rp_comp1]
type = PiecewiseLinear
data_file = 'rp_comp1.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_comp2]
type = PiecewiseLinear
data_file = 'rp_comp2.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_comp3]
type = PiecewiseLinear
data_file = 'rp_comp3.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_comp4]
type = PiecewiseLinear
data_file = 'rp_comp4.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_comp5]
type = PiecewiseLinear
data_file = 'rp_comp5.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
# compressor efficiency
[eff_comp1]
type = ConstantFunction
value = ${eff_comp}
[]
[eff_comp2]
type = ConstantFunction
value = ${eff_comp}
[]
[eff_comp3]
type = ConstantFunction
value = ${eff_comp}
[]
[eff_comp4]
type = ConstantFunction
value = ${eff_comp}
[]
[eff_comp5]
type = ConstantFunction
value = ${eff_comp}
[]
# turbine pressure ratio
[rp_turb0]
type = ConstantFunction
value = 1
[]
[rp_turb1]
type = PiecewiseLinear
data_file = 'rp_turb1.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_turb2]
type = PiecewiseLinear
data_file = 'rp_turb2.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_turb3]
type = PiecewiseLinear
data_file = 'rp_turb3.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_turb4]
type = PiecewiseLinear
data_file = 'rp_turb4.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_turb5]
type = PiecewiseLinear
data_file = 'rp_turb5.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
# turbine efficiency
[eff_turb1]
type = ConstantFunction
value = ${eff_turb}
[]
[eff_turb2]
type = ConstantFunction
value = ${eff_turb}
[]
[eff_turb3]
type = ConstantFunction
value = ${eff_turb}
[]
[eff_turb4]
type = ConstantFunction
value = ${eff_turb}
[]
[eff_turb5]
type = ConstantFunction
value = ${eff_turb}
[]
[]
(modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/basic-primitive-pcnsfv-kt.i)
[GlobalParams]
fp = fp
limiter = 'central_difference'
two_term_boundary_expansion = true
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 1
xmin = .1
xmax = .6
nx = 2
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Problem]
fv_bcs_integrity_check = false
[]
[Variables]
[pressure]
type = MooseVariableFVReal
[]
[sup_vel_x]
type = MooseVariableFVReal
[]
[T_fluid]
type = MooseVariableFVReal
[]
[]
[ICs]
[pressure]
type = FunctionIC
variable = pressure
function = 'exact_p'
[]
[sup_vel_x]
type = FunctionIC
variable = sup_vel_x
function = 'exact_sup_vel_x'
[]
[T_fluid]
type = FunctionIC
variable = T_fluid
function = 'exact_T'
[]
[]
[FVKernels]
[mass_advection]
type = PCNSFVKT
variable = pressure
eqn = "mass"
[]
[mass_fn]
type = FVBodyForce
variable = pressure
function = 'forcing_rho'
[]
[momentum_x_advection]
type = PCNSFVKT
variable = sup_vel_x
momentum_component = x
eqn = "momentum"
[]
[momentum_fn]
type = FVBodyForce
variable = sup_vel_x
function = 'forcing_rho_ud'
[]
[fluid_energy_advection]
type = PCNSFVKT
variable = T_fluid
eqn = "energy"
[]
[energy_fn]
type = FVBodyForce
variable = T_fluid
function = 'forcing_rho_et'
[]
[]
[FVBCs]
[mass_left]
variable = pressure
type = PCNSFVStrongBC
boundary = left
T_fluid = 'exact_T'
superficial_velocity = 'exact_superficial_velocity'
eqn = 'mass'
[]
[momentum_left]
variable = sup_vel_x
type = PCNSFVStrongBC
boundary = left
T_fluid = 'exact_T'
superficial_velocity = 'exact_superficial_velocity'
eqn = 'momentum'
momentum_component = 'x'
[]
[energy_left]
variable = T_fluid
type = PCNSFVStrongBC
boundary = left
T_fluid = 'exact_T'
superficial_velocity = 'exact_superficial_velocity'
eqn = 'energy'
[]
[mass_right]
variable = pressure
type = PCNSFVStrongBC
boundary = right
eqn = 'mass'
pressure = 'exact_p'
[]
[momentum_right]
variable = sup_vel_x
type = PCNSFVStrongBC
boundary = right
eqn = 'momentum'
momentum_component = 'x'
pressure = 'exact_p'
[]
[energy_right]
variable = T_fluid
type = PCNSFVStrongBC
boundary = right
eqn = 'energy'
pressure = 'exact_p'
[]
# help gradient reconstruction
[pressure_right]
type = FVFunctionDirichletBC
variable = pressure
function = exact_p
boundary = 'right'
[]
[sup_vel_x_left]
type = FVFunctionDirichletBC
variable = sup_vel_x
function = exact_sup_vel_x
boundary = 'left'
[]
[T_fluid_left]
type = FVFunctionDirichletBC
variable = T_fluid
function = exact_T
boundary = 'left'
[]
[]
[Materials]
[var_mat]
type = PorousPrimitiveVarMaterial
pressure = pressure
superficial_vel_x = sup_vel_x
T_fluid = T_fluid
porosity = porosity
[]
[porosity]
type = GenericFunctionMaterial
prop_names = 'porosity'
prop_values = 'eps'
[]
[]
[Functions]
[exact_rho]
type = ParsedFunction
expression = '3.48788261470924*cos(x)'
[]
[forcing_rho]
type = ParsedFunction
expression = '-3.45300378856215*sin(1.1*x)'
[]
[exact_rho_ud]
type = ParsedFunction
expression = '3.13909435323832*cos(1.1*x)'
[]
[forcing_rho_ud]
type = ParsedFunction
expression = '-0.9*(10.6975765229419*cos(1.2*x)/cos(x) - 0.697576522941849*cos(1.1*x)^2/cos(x)^2)*sin(x) + 0.9*(10.6975765229419*sin(x)*cos(1.2*x)/cos(x)^2 - 1.3951530458837*sin(x)*cos(1.1*x)^2/cos(x)^3 + 1.53466835047207*sin(1.1*x)*cos(1.1*x)/cos(x)^2 - 12.8370918275302*sin(1.2*x)/cos(x))*cos(x) + 3.13909435323832*sin(x)*cos(1.1*x)^2/cos(x)^2 - 6.9060075771243*sin(1.1*x)*cos(1.1*x)/cos(x)'
[]
[exact_rho_et]
type = ParsedFunction
expression = '26.7439413073546*cos(1.2*x)'
[]
[forcing_rho_et]
type = ParsedFunction
expression = '0.9*(3.48788261470924*(3.06706896551724*cos(1.2*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.2*x))*sin(x)*cos(1.1*x)/cos(x)^2 - 0.99*(3.48788261470924*(3.06706896551724*cos(1.2*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.2*x))*sin(1.1*x)/cos(x) + 0.9*(-(10.6975765229419*cos(1.2*x)/cos(x) - 0.697576522941849*cos(1.1*x)^2/cos(x)^2)*sin(x) + (10.6975765229419*sin(x)*cos(1.2*x)/cos(x)^2 - 1.3951530458837*sin(x)*cos(1.1*x)^2/cos(x)^3 + 1.53466835047207*sin(1.1*x)*cos(1.1*x)/cos(x)^2 - 12.8370918275302*sin(1.2*x)/cos(x))*cos(x) - 32.0927295688256*sin(1.2*x))*cos(1.1*x)/cos(x)'
[]
[exact_T]
type = ParsedFunction
expression = '0.0106975765229418*cos(1.2*x)/cos(x) - 0.000697576522941848*cos(1.1*x)^2/cos(x)^2'
[]
[exact_eps_p]
type = ParsedFunction
expression = '3.13909435323832*(3.06706896551724*cos(1.2*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x)'
[]
[exact_p]
type = ParsedFunction
expression = '3.48788261470924*(3.06706896551724*cos(1.2*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x)'
[]
[exact_sup_vel_x]
type = ParsedFunction
expression = '0.9*cos(1.1*x)/cos(x)'
[]
[exact_superficial_velocity]
type = ParsedVectorFunction
expression_x = '0.9*cos(1.1*x)/cos(x)'
[]
[eps]
type = ParsedFunction
expression = '0.9'
[]
[]
[Executioner]
solve_type = NEWTON
type = Transient
num_steps = 1
dtmin = 1
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_max_its = 50
line_search = bt
nl_rel_tol = 1e-12
nl_abs_tol = 1e-12
[]
[Outputs]
exodus = true
csv = true
[]
[Debug]
show_var_residual_norms = true
[]
[Postprocessors]
[h]
type = AverageElementSize
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2pressure]
type = ElementL2Error
variable = pressure
function = exact_p
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2sup_vel_x]
variable = sup_vel_x
function = exact_sup_vel_x
type = ElementL2Error
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2T_fluid]
variable = T_fluid
function = exact_T
type = ElementL2Error
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[]
(modules/thermal_hydraulics/test/tests/problems/double_rarefaction/1phase.i)
# Riemann problem that has a double-rarefaction solution
[GlobalParams]
gravity_vector = '0 0 0'
rdg_slope_reconstruction = minmod
closures = simple_closures
[]
[Functions]
[vel_ic_fn]
type = PiecewiseConstant
axis = x
direction = right
x = ' 0.0 0.1'
y = '-1.0 1.0'
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 11.64024372
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[pipe]
type = FlowChannel1Phase
fp = fp
# geometry
position = '-1 0 0'
orientation = '1 0 0'
length = 2.0
n_elems = 100
A = 1.0
# IC
initial_T = 0.04
initial_p = 0.2
initial_vel = vel_ic_fn
f = 0
[]
[left_boundary]
type = FreeBoundary1Phase
input = 'pipe:in'
[]
[right_boundary]
type = FreeBoundary1Phase
input = 'pipe:out'
[]
[]
[Executioner]
type = Transient
[TimeIntegrator]
type = ExplicitSSPRungeKutta
order = 2
[]
solve_type = LINEAR
l_tol = 1e-4
nl_rel_tol = 1e-20
nl_abs_tol = 1e-8
nl_max_its = 60
# run to t = 0.6
start_time = 0.0
dt = 1e-3
num_steps = 600
abort_on_solve_fail = true
[]
[Outputs]
file_base = '1phase'
velocity_as_vector = false
execute_on = 'initial timestep_end'
[out]
type = Exodus
show = 'p T vel'
[]
[]
(modules/thermal_hydraulics/test/tests/components/shaft_connected_turbine_1phase/turbine_startup.i)
# This test tests that the turbine can startup from rest and reach full power.
# The mass flow rate for the inlet component is ramped up over 10s. The dyno
# component and pid_ctrl controler are used to maintain the turbine's rated shaft
# speed. The turbine should supply ~1e6 W of power to the shaft by the end of the test.
omega_rated = 450
mdot = 5.0
T_in = 1000.0
p_out = 1e6
[GlobalParams]
f = 1
scaling_factor_1phase = '0.04 0.04 0.04e-5'
closures = simple_closures
n_elems = 20
initial_T = ${T_in}
initial_p = ${p_out}
initial_vel = 0
initial_vel_x = 0
initial_vel_y = 0
initial_vel_z = 0
[]
[FluidProperties]
[eos]
type = IdealGasFluidProperties
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[ch_in]
type = FlowChannel1Phase
position = '-1 0 0'
orientation = '1 0 0'
length = 1
A = 0.1
D_h = 1
fp = eos
[]
[inlet]
type = InletMassFlowRateTemperature1Phase
input = 'ch_in:in'
m_dot = 0
T = ${T_in}
[]
[turbine]
type = ShaftConnectedTurbine1Phase
inlet = 'ch_in:out'
outlet = 'ch_out:in'
position = '0 0 0'
scaling_factor_rhoEV = 1e-5
A_ref = 0.1
volume = 0.0002
inertia_coeff = '1 1 1 1'
inertia_const = 1.61397
speed_cr_I = 1e12
speed_cr_fr = 0
tau_fr_coeff = '0 0 0 0'
tau_fr_const = 0
omega_rated = ${omega_rated}
D_wheel = 0.4
head_coefficient = head
power_coefficient = power
[]
[ch_out]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 1
A = 0.1
D_h = 1
fp = eos
[]
[outlet]
type = Outlet1Phase
input = 'ch_out:out'
p = ${p_out}
[]
[dyno]
type = ShaftConnectedMotor
inertia = 10
torque = -450
[]
[shaft]
type = Shaft
connected_components = 'turbine dyno'
initial_speed = ${omega_rated}
[]
[]
[Functions]
[head]
type = PiecewiseLinear
x = '0 7e-3 1e-2'
y = '0 15 20'
[]
[power]
type = PiecewiseLinear
x = '0 6e-3 1e-2'
y = '0 0.05 0.18'
[]
[mfr_fn]
type = PiecewiseLinear
x = '0 10'
y = '1e-6 ${mdot}'
[]
[dts]
type = PiecewiseConstant
y = '5e-3 1e-2 5e-2 5e-1'
x = '0 0.5 1 10'
[]
[]
[ControlLogic]
[mfr_cntrl]
type = TimeFunctionComponentControl
component = inlet
parameter = m_dot
function = mfr_fn
[]
[speed_set_point]
type = GetFunctionValueControl
function = ${omega_rated}
[]
[pid_ctrl]
type = PIDControl
input = omega
set_point = speed_set_point:value
K_i = 2
K_p = 5
K_d = 5
initial_value = -450
[]
[set_torque_value]
type = SetComponentRealValueControl
component = dyno
parameter = torque
value = pid_ctrl:output
[]
[]
[Postprocessors]
[omega]
type = ScalarVariable
variable = shaft:omega
execute_on = 'initial timestep_end'
[]
[flow_coefficient]
type = ElementAverageValue
variable = flow_coeff
block = 'turbine'
execute_on = 'initial timestep_end'
[]
[delta_p]
type = ElementAverageValue
variable = delta_p
block = 'turbine'
execute_on = 'initial timestep_end'
[]
[power]
type = ElementAverageValue
variable = power
block = 'turbine'
execute_on = 'initial timestep_end'
[]
[]
[Preconditioning]
[SMP]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'implicit-euler'
start_time = 0
[TimeStepper]
type = FunctionDT
function = dts
[]
end_time = 20
abort_on_solve_fail = true
solve_type = 'PJFNK'
line_search = 'basic'
nl_rel_tol = 1e-6
nl_abs_tol = 1e-4
nl_max_its = 30
l_tol = 1e-4
l_max_its = 20
[Quadrature]
type = GAUSS
order = SECOND
[]
[]
[Outputs]
[console]
type = Console
max_rows = 1
[]
print_linear_residuals = false
[]
(modules/navier_stokes/test/tests/finite_volume/cns/straight_channel_porosity_step/rotated-2d-bkt-function-porosity-mixed.i)
p_initial=1.01e5
T=273.15
# u refers to the superficial velocity
u_in=1
rho_in=1.30524
sup_mom_y_in=${fparse u_in * rho_in}
user_limiter='upwind'
friction_coeff=10
[GlobalParams]
fp = fp
two_term_boundary_expansion = true
limiter = ${user_limiter}
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 2
xmin = 0
xmax = 1
nx = 3
ymin = 0
ymax = 18
ny = 90
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Problem]
fv_bcs_integrity_check = false
[]
[Variables]
[pressure]
type = MooseVariableFVReal
initial_condition = ${p_initial}
[]
[sup_mom_x]
type = MooseVariableFVReal
initial_condition = 1e-15
scaling = 1e-2
[]
[sup_mom_y]
type = MooseVariableFVReal
initial_condition = 1e-15
scaling = 1e-2
[]
[T_fluid]
type = MooseVariableFVReal
initial_condition = ${T}
scaling = 1e-5
[]
[]
[AuxVariables]
[vel_y]
type = MooseVariableFVReal
[]
[rho]
type = MooseVariableFVReal
[]
[eps]
type = MooseVariableFVReal
[]
[]
[AuxKernels]
[vel_y]
type = ADMaterialRealAux
variable = vel_y
property = vel_y
execute_on = 'timestep_end'
[]
[rho]
type = ADMaterialRealAux
variable = rho
property = rho
execute_on = 'timestep_end'
[]
[eps]
type = MaterialRealAux
variable = eps
property = porosity
execute_on = 'timestep_end'
[]
[]
[FVKernels]
[mass_time]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rho_dt'
variable = pressure
[]
[mass_advection]
type = PCNSFVKT
variable = pressure
eqn = "mass"
[]
[momentum_time]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rhou_dt'
variable = sup_mom_x
[]
[momentum_advection]
type = PCNSFVKT
variable = sup_mom_x
eqn = "momentum"
momentum_component = 'x'
[]
[eps_grad]
type = PNSFVPGradEpsilon
variable = sup_mom_x
momentum_component = 'x'
epsilon_function = 'eps'
[]
[drag]
type = PCNSFVMomentumFriction
variable = sup_mom_x
momentum_component = 'x'
Darcy_name = 'cl'
momentum_name = superficial_rhou
[]
[momentum_time_y]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rhov_dt'
variable = sup_mom_y
[]
[momentum_advection_y]
type = PCNSFVKT
variable = sup_mom_y
eqn = "momentum"
momentum_component = 'y'
[]
[eps_grad_y]
type = PNSFVPGradEpsilon
variable = sup_mom_y
momentum_component = 'y'
epsilon_function = 'eps'
[]
[drag_y]
type = PCNSFVMomentumFriction
variable = sup_mom_y
momentum_component = 'y'
Darcy_name = 'cl'
momentum_name = superficial_rhov
[]
[energy_time]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rho_et_dt'
variable = T_fluid
[]
[energy_advection]
type = PCNSFVKT
variable = T_fluid
eqn = "energy"
[]
[]
[FVBCs]
[rho_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = pressure
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'mass'
velocity_function_includes_rho = true
[]
[rhou_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = sup_mom_x
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'momentum'
momentum_component = 'x'
velocity_function_includes_rho = true
[]
[rhov_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = sup_mom_y
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'momentum'
momentum_component = 'y'
velocity_function_includes_rho = true
[]
[rho_et_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = T_fluid
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'energy'
velocity_function_includes_rho = true
[]
[rho_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = pressure
pressure = ${p_initial}
eqn = 'mass'
[]
[rhou_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = sup_mom_x
pressure = ${p_initial}
eqn = 'momentum'
momentum_component = 'x'
[]
[rhov_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = sup_mom_y
pressure = ${p_initial}
eqn = 'momentum'
momentum_component = 'y'
[]
[rho_et_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = T_fluid
pressure = ${p_initial}
eqn = 'energy'
[]
[wall_pressure_x]
type = PCNSFVImplicitMomentumPressureBC
momentum_component = 'x'
boundary = 'left right'
variable = sup_mom_x
[]
[wall_pressure_y]
type = PCNSFVImplicitMomentumPressureBC
momentum_component = 'y'
boundary = 'left right'
variable = sup_mom_y
[]
# Use these to help create more accurate cell centered gradients for cells adjacent to boundaries
[T_bottom]
type = FVDirichletBC
variable = T_fluid
value = ${T}
boundary = 'bottom'
[]
[sup_mom_x_bottom_and_walls]
type = FVDirichletBC
variable = sup_mom_x
value = 0
boundary = 'bottom left right'
[]
[sup_mom_y_walls]
type = FVDirichletBC
variable = sup_mom_y
value = 0
boundary = 'left right'
[]
[sup_mom_y_bottom]
type = FVDirichletBC
variable = sup_mom_y
value = ${sup_mom_y_in}
boundary = 'bottom'
[]
[p_top]
type = FVDirichletBC
variable = pressure
value = ${p_initial}
boundary = 'top'
[]
[]
[Functions]
[ud_in]
type = ParsedVectorFunction
expression_x = '0'
expression_y = '${sup_mom_y_in}'
[]
[eps]
type = ParsedFunction
expression = 'if(y < 2.8, 1,
if(y < 3.2, 1 - .5 / .4 * (y - 2.8),
if(y < 6.8, .5,
if(y < 7.2, .5 - .25 / .4 * (y - 6.8),
if(y < 10.8, .25,
if(y < 11.2, .25 + .25 / .4 * (y - 10.8),
if(y < 14.8, .5,
if(y < 15.2, .5 + .5 / .4 * (y - 14.8),
1))))))))'
[]
[]
[Materials]
[var_mat]
type = PorousMixedVarMaterial
pressure = pressure
T_fluid = T_fluid
superficial_rhou = sup_mom_x
superficial_rhov = sup_mom_y
fp = fp
porosity = porosity
[]
[porosity]
type = GenericFunctionMaterial
prop_names = 'porosity'
prop_values = 'eps'
[]
[ad_generic]
type = ADGenericConstantVectorMaterial
prop_names = 'cl'
prop_values = '${friction_coeff} ${friction_coeff} ${friction_coeff}'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
solve_type = NEWTON
line_search = 'bt'
type = Transient
nl_max_its = 20
[TimeStepper]
type = IterationAdaptiveDT
dt = 5e-5
optimal_iterations = 6
growth_factor = 1.2
[]
num_steps = 10000
end_time = 500
nl_abs_tol = 1e-7
petsc_options_iname = '-pc_type -pc_factor_mat_solver_type'
petsc_options_value = 'lu mumps'
[]
[Outputs]
[out]
type = Exodus
execute_on = 'final'
[]
checkpoint = true
[]
[Debug]
show_var_residual_norms = true
[]
(modules/fluid_properties/test/tests/fp_interrogator/err.no_params.i)
[FluidPropertiesInterrogator]
fp = fp
[]
[FluidProperties]
[./fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.02900055737704918
mu = 1.823e-05
k = 0.02568
[../]
[]
(modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/free-flow-hllc.i)
diff_coeff = 0.1
[GlobalParams]
fp = fp
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 1
xmin = .1
xmax = 1.1
nx = 2
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Variables]
[rho]
type = MooseVariableFVReal
[]
[rho_u]
type = MooseVariableFVReal
[]
[rho_et]
type = MooseVariableFVReal
[]
[]
[ICs]
[rho]
type = FunctionIC
variable = rho
function = 'exact_rho'
[]
[rho_u]
type = FunctionIC
variable = rho_u
function = 'exact_rho_u'
[]
[rho_et]
type = FunctionIC
variable = rho_et
function = 'exact_rho_et'
[]
[]
[FVKernels]
[mass_advection]
type = CNSFVMassHLLC
variable = rho
[]
[mass_fn]
type = FVBodyForce
variable = rho
function = 'forcing_rho'
[]
[momentum_x_advection]
type = CNSFVMomentumHLLC
variable = rho_u
momentum_component = x
[]
[momentum_fn]
type = FVBodyForce
variable = rho_u
function = 'forcing_rho_u'
[]
[fluid_energy_advection]
type = CNSFVFluidEnergyHLLC
variable = rho_et
[]
[energy_fn]
type = FVBodyForce
variable = rho_et
function = 'forcing_rho_et'
[]
[mass_diff]
type = FVDiffusion
variable = rho
coeff = ${diff_coeff}
[]
[momentum_diff]
type = FVDiffusion
variable = rho_u
coeff = ${diff_coeff}
[]
[energy_diff]
type = FVDiffusion
variable = rho_et
coeff = ${diff_coeff}
[]
[]
[FVBCs]
[mass_in]
variable = rho
type = CNSFVHLLCSpecifiedMassFluxAndTemperatureMassBC
boundary = left
temperature = 'exact_T'
rhou = 'exact_rho_u'
[]
[momentum_in]
variable = rho_u
type = CNSFVHLLCSpecifiedMassFluxAndTemperatureMomentumBC
boundary = left
temperature = 'exact_T'
rhou = 'exact_rho_u'
momentum_component = 'x'
[]
[energy_in]
variable = rho_et
type = CNSFVHLLCSpecifiedMassFluxAndTemperatureFluidEnergyBC
boundary = left
temperature = 'exact_T'
rhou = 'exact_rho_u'
[]
[mass_out]
variable = rho
type = CNSFVHLLCSpecifiedPressureMassBC
boundary = right
pressure = 'exact_p'
[]
[momentum_out]
variable = rho_u
type = CNSFVHLLCSpecifiedPressureMomentumBC
boundary = right
pressure = 'exact_p'
momentum_component = 'x'
[]
[energy_out]
variable = rho_et
type = CNSFVHLLCSpecifiedPressureFluidEnergyBC
boundary = right
pressure = 'exact_p'
[]
[left_mass_diffusion]
type = FVFunctionNeumannBC
variable = rho
function = minus_rho_bc
boundary = 'left'
[]
[left_momentum_diffusion]
type = FVFunctionNeumannBC
variable = rho_u
function = minus_rho_u_bc
boundary = 'left'
[]
[left_energy_diffusion]
type = FVFunctionNeumannBC
variable = rho_et
function = minus_rho_et_bc
boundary = 'left'
[]
[right_mass_diffusion]
type = FVFunctionNeumannBC
variable = rho
function = rho_bc
boundary = 'right'
[]
[right_momentum_diffusion]
type = FVFunctionNeumannBC
variable = rho_u
function = rho_u_bc
boundary = 'right'
[]
[right_energy_diffusion]
type = FVFunctionNeumannBC
variable = rho_et
function = rho_et_bc
boundary = 'right'
[]
[]
[Materials]
[var_mat]
type = ConservedVarValuesMaterial
rho = rho
rhou = rho_u
rho_et = rho_et
[]
[]
[Functions]
[exact_rho]
type = ParsedFunction
expression = '3.48788261470924*cos(x)'
[]
[rho_bc]
type = ParsedFunction
value = '-diff_coeff*3.48788261470924*sin(x)'
vars = 'diff_coeff'
vals = '${diff_coeff}'
[]
[minus_rho_bc]
type = ParsedFunction
value = 'diff_coeff*3.48788261470924*sin(x)'
vars = 'diff_coeff'
vals = '${diff_coeff}'
[]
[forcing_rho]
type = ParsedFunction
expression = '-3.83667087618017*sin(1.1*x) + 0.348788261470924*cos(x)'
[]
[exact_rho_u]
type = ParsedFunction
expression = '3.48788261470924*cos(1.1*x)'
[]
[rho_u_bc]
type = ParsedFunction
value = '-diff_coeff*3.48788261470924*1.1*sin(1.1*x)'
vars = 'diff_coeff'
vals = '${diff_coeff}'
[]
[minus_rho_u_bc]
type = ParsedFunction
value = 'diff_coeff*3.48788261470924*1.1*sin(1.1*x)'
vars = 'diff_coeff'
vals = '${diff_coeff}'
[]
[forcing_rho_u]
type = ParsedFunction
expression = '-(10.6975765229419*cos(1.2*x)/cos(x) - 0.697576522941849*cos(1.1*x)^2/cos(x)^2)*sin(x) + (10.6975765229419*sin(x)*cos(1.2*x)/cos(x)^2 - 1.3951530458837*sin(x)*cos(1.1*x)^2/cos(x)^3 + 1.53466835047207*sin(1.1*x)*cos(1.1*x)/cos(x)^2 - 12.8370918275302*sin(1.2*x)/cos(x))*cos(x) + 3.48788261470924*sin(x)*cos(1.1*x)^2/cos(x)^2 - 7.67334175236034*sin(1.1*x)*cos(1.1*x)/cos(x) + 0.422033796379819*cos(1.1*x)'
[]
[exact_rho_et]
type = ParsedFunction
expression = '26.7439413073546*cos(1.2*x)'
[]
[rho_et_bc]
type = ParsedFunction
value = '-diff_coeff*26.7439413073546*1.2*sin(1.2*x)'
vars = 'diff_coeff'
vals = '${diff_coeff}'
[]
[minus_rho_et_bc]
type = ParsedFunction
value = 'diff_coeff*26.7439413073546*1.2*sin(1.2*x)'
vars = 'diff_coeff'
vals = '${diff_coeff}'
[]
[forcing_rho_et]
type = ParsedFunction
expression = '1.0*(3.48788261470924*(3.06706896551724*cos(1.2*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.2*x))*sin(x)*cos(1.1*x)/cos(x)^2 - 1.1*(3.48788261470924*(3.06706896551724*cos(1.2*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.2*x))*sin(1.1*x)/cos(x) + 1.0*(-(10.6975765229419*cos(1.2*x)/cos(x) - 0.697576522941849*cos(1.1*x)^2/cos(x)^2)*sin(x) + (10.6975765229419*sin(x)*cos(1.2*x)/cos(x)^2 - 1.3951530458837*sin(x)*cos(1.1*x)^2/cos(x)^3 + 1.53466835047207*sin(1.1*x)*cos(1.1*x)/cos(x)^2 - 12.8370918275302*sin(1.2*x)/cos(x))*cos(x) - 32.0927295688256*sin(1.2*x))*cos(1.1*x)/cos(x) + 3.85112754825907*cos(1.2*x)'
[]
[exact_T]
type = ParsedFunction
expression = '0.0106975765229418*cos(1.2*x)/cos(x) - 0.000697576522941848*cos(1.1*x)^2/cos(x)^2'
[]
[exact_p]
type = ParsedFunction
expression = '3.48788261470924*(3.06706896551724*cos(1.2*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x)'
[]
[]
[Executioner]
solve_type = NEWTON
type = Steady
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_max_its = 50
line_search = none
nl_rel_tol = 1e-11
nl_abs_tol = 1e-11
[]
[Outputs]
exodus = true
csv = true
[]
[Debug]
show_var_residual_norms = true
[]
[Postprocessors]
[h]
type = AverageElementSize
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2rho]
type = ElementL2Error
variable = rho
function = exact_rho
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2rho_u]
variable = rho_u
function = exact_rho_u
type = ElementL2Error
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2rho_et]
variable = rho_et
function = exact_rho_et
type = ElementL2Error
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[]
(modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/varying-eps-basic-kt-primitive.i)
[GlobalParams]
fp = fp
limiter = 'central_difference'
two_term_boundary_expansion = true
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 1
xmin = .1
xmax = .6
nx = 2
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Problem]
fv_bcs_integrity_check = false
[]
[Variables]
[pressure]
type = MooseVariableFVReal
[]
[sup_vel_x]
type = MooseVariableFVReal
[]
[T_fluid]
type = MooseVariableFVReal
[]
[]
[ICs]
[pressure]
type = FunctionIC
variable = pressure
function = 'exact_p'
[]
[sup_vel_x]
type = FunctionIC
variable = sup_vel_x
function = 'exact_sup_vel_x'
[]
[T_fluid]
type = FunctionIC
variable = T_fluid
function = 'exact_T'
[]
[]
[FVKernels]
[mass_advection]
type = PCNSFVKT
variable = pressure
eqn = "mass"
[]
[mass_fn]
type = FVBodyForce
variable = pressure
function = 'forcing_rho'
[]
[momentum_x_advection]
type = PCNSFVKT
variable = sup_vel_x
momentum_component = x
eqn = "momentum"
[]
[eps_grad]
type = PNSFVPGradEpsilon
variable = sup_vel_x
momentum_component = 'x'
epsilon_function = 'eps'
[]
[momentum_fn]
type = FVBodyForce
variable = sup_vel_x
function = 'forcing_rho_ud'
[]
[fluid_energy_advection]
type = PCNSFVKT
variable = T_fluid
eqn = "energy"
[]
[energy_fn]
type = FVBodyForce
variable = T_fluid
function = 'forcing_rho_et'
[]
[]
[FVBCs]
[mass_left]
variable = pressure
type = PCNSFVStrongBC
boundary = left
T_fluid = 'exact_T'
superficial_velocity = 'exact_superficial_velocity'
eqn = 'mass'
[]
[momentum_left]
variable = sup_vel_x
type = PCNSFVStrongBC
boundary = left
T_fluid = 'exact_T'
superficial_velocity = 'exact_superficial_velocity'
eqn = 'momentum'
momentum_component = 'x'
[]
[energy_left]
variable = T_fluid
type = PCNSFVStrongBC
boundary = left
T_fluid = 'exact_T'
superficial_velocity = 'exact_superficial_velocity'
eqn = 'energy'
[]
[mass_right]
variable = pressure
type = PCNSFVStrongBC
boundary = right
eqn = 'mass'
pressure = 'exact_p'
[]
[momentum_right]
variable = sup_vel_x
type = PCNSFVStrongBC
boundary = right
eqn = 'momentum'
momentum_component = 'x'
pressure = 'exact_p'
[]
[energy_right]
variable = T_fluid
type = PCNSFVStrongBC
boundary = right
eqn = 'energy'
pressure = 'exact_p'
[]
# help gradient reconstruction
[pressure_right]
type = FVFunctionDirichletBC
variable = pressure
function = exact_p
boundary = 'right'
[]
[sup_vel_x_left]
type = FVFunctionDirichletBC
variable = sup_vel_x
function = exact_sup_vel_x
boundary = 'left'
[]
[T_fluid_left]
type = FVFunctionDirichletBC
variable = T_fluid
function = exact_T
boundary = 'left'
[]
[]
[Materials]
[var_mat]
type = PorousPrimitiveVarMaterial
pressure = pressure
superficial_vel_x = sup_vel_x
T_fluid = T_fluid
porosity = porosity
[]
[porosity]
type = GenericFunctionMaterial
prop_names = 'porosity'
prop_values = 'eps'
[]
[]
[Functions]
[exact_rho]
type = ParsedFunction
expression = '3.48788261470924*cos(x)'
[]
[forcing_rho]
type = ParsedFunction
expression = '-3.83667087618017*sin(1.1*x)*cos(1.3*x) - 4.53424739912202*sin(1.3*x)*cos(1.1*x)'
[]
[exact_rho_ud]
type = ParsedFunction
expression = '3.48788261470924*cos(1.1*x)*cos(1.3*x)'
[]
[forcing_rho_ud]
type = ParsedFunction
expression = '(-(10.6975765229419*cos(1.5*x)/cos(x) - 0.697576522941849*cos(1.1*x)^2/cos(x)^2)*sin(x) + (10.6975765229419*sin(x)*cos(1.5*x)/cos(x)^2 - 1.3951530458837*sin(x)*cos(1.1*x)^2/cos(x)^3 + 1.53466835047207*sin(1.1*x)*cos(1.1*x)/cos(x)^2 - 16.0463647844128*sin(1.5*x)/cos(x))*cos(x))*cos(1.3*x) + 3.48788261470924*sin(x)*cos(1.1*x)^2*cos(1.3*x)/cos(x)^2 - 7.67334175236034*sin(1.1*x)*cos(1.1*x)*cos(1.3*x)/cos(x) - 4.53424739912202*sin(1.3*x)*cos(1.1*x)^2/cos(x)'
[]
[exact_rho_et]
type = ParsedFunction
expression = '26.7439413073546*cos(1.5*x)'
[]
[forcing_rho_et]
type = ParsedFunction
expression = '1.0*(3.48788261470924*(3.06706896551724*cos(1.5*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.5*x))*sin(x)*cos(1.1*x)*cos(1.3*x)/cos(x)^2 - 1.1*(3.48788261470924*(3.06706896551724*cos(1.5*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.5*x))*sin(1.1*x)*cos(1.3*x)/cos(x) - 1.3*(3.48788261470924*(3.06706896551724*cos(1.5*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x) + 26.7439413073546*cos(1.5*x))*sin(1.3*x)*cos(1.1*x)/cos(x) + 1.0*(-(10.6975765229419*cos(1.5*x)/cos(x) - 0.697576522941849*cos(1.1*x)^2/cos(x)^2)*sin(x) + (10.6975765229419*sin(x)*cos(1.5*x)/cos(x)^2 - 1.3951530458837*sin(x)*cos(1.1*x)^2/cos(x)^3 + 1.53466835047207*sin(1.1*x)*cos(1.1*x)/cos(x)^2 - 16.0463647844128*sin(1.5*x)/cos(x))*cos(x) - 40.1159119610319*sin(1.5*x))*cos(1.1*x)*cos(1.3*x)/cos(x)'
[]
[exact_T]
type = ParsedFunction
expression = '0.0106975765229418*cos(1.5*x)/cos(x) - 0.000697576522941848*cos(1.1*x)^2/cos(x)^2'
[]
[exact_eps_p]
type = ParsedFunction
expression = '3.48788261470924*(3.06706896551724*cos(1.5*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x)*cos(1.3*x)'
[]
[exact_p]
type = ParsedFunction
expression = '3.48788261470924*(3.06706896551724*cos(1.5*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x)'
[]
[exact_sup_vel_x]
type = ParsedFunction
expression = '1.0*cos(1.1*x)*cos(1.3*x)/cos(x)'
[]
[eps]
type = ParsedFunction
expression = 'cos(1.3*x)'
[]
[exact_superficial_velocity]
type = ParsedVectorFunction
expression_x = '1.0*cos(1.1*x)*cos(1.3*x)/cos(x)'
[]
[]
[Executioner]
solve_type = NEWTON
type = Transient
num_steps = 1
dtmin = 1
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_max_its = 50
line_search = bt
nl_rel_tol = 1e-12
nl_abs_tol = 1e-12
[]
[Outputs]
exodus = true
csv = true
[]
[Debug]
show_var_residual_norms = true
[]
[Postprocessors]
[h]
type = AverageElementSize
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2pressure]
type = ElementL2Error
variable = pressure
function = exact_p
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2sup_vel_x]
variable = sup_vel_x
function = exact_sup_vel_x
type = ElementL2Error
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2T_fluid]
variable = T_fluid
function = exact_T
type = ElementL2Error
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[]
(modules/thermal_hydraulics/test/tests/components/junction_one_to_one_1phase/constriction_1phase.i)
# This test is used to test the JunctionOneToOne1Phase1Phase component with unequal areas
# at the junction. The downstream flow channel has an area half that of the
# upstream pipe, so there should be a pressure increase just upstream of the
# junction due to the partial wall. The velocity should increase through the
# junction (approximately by a factor of 2, but there are compressibility effects).
[GlobalParams]
gravity_vector = '0 0 0'
fp = fp
closures = simple_closures
f = 0
initial_T = 300
initial_p = 1e5
initial_vel = 1
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 11.64024372
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[left_boundary]
type = InletDensityVelocity1Phase
input = 'left_channel:in'
rho = 466.6666667
vel = 1
[]
[left_channel]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = 50
A = 1.0
[]
[junction]
type = JunctionOneToOne1Phase
connections = 'left_channel:out right_channel:in'
[]
[right_channel]
type = FlowChannel1Phase
position = '0.5 0 0'
orientation = '1 0 0'
length = 0.5
n_elems = 50
A = 0.5
[]
[right_boundary]
type = Outlet1Phase
input = 'right_channel:out'
p = 1e5
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
dt = 0.01
num_steps = 10
abort_on_solve_fail = true
solve_type = NEWTON
nl_rel_tol = 1e-10
nl_abs_tol = 1e-8
nl_max_its = 60
l_tol = 1e-4
[]
[Outputs]
exodus = true
show = 'p T vel'
execute_on = 'initial timestep_end'
velocity_as_vector = false
[]
(modules/thermal_hydraulics/test/tests/problems/pressure_drop/pressure_drop.i)
nelem = 100
friction_factor = 1e4
area = 0.176752
mfr_final = 1.0
p_out = 7e6
T_in = 300
ramp_time = 5.0
[GlobalParams]
gravity_vector = '0 0 0'
initial_T = ${T_in}
initial_p = ${p_out}
initial_vel = 0
closures = closures
rdg_slope_reconstruction = full
scaling_factor_1phase = '1 1 1e-5'
[]
[FluidProperties]
[h2]
type = IdealGasFluidProperties
gamma = 1.3066
molar_mass = 2.016e-3
k = 0.437
mu = 3e-5
[]
[]
[Closures]
[closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[bc_inlet]
type = InletMassFlowRateTemperature1Phase
input = 'ch_1:in'
m_dot = 0 # This value is controlled by 'mfr_ctrl'
T = ${T_in}
[]
[ch_1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 1.0
n_elems = ${nelem}
A = ${area}
f = ${friction_factor}
fp = h2
[]
[bc_outlet]
type = Outlet1Phase
input = 'ch_1:out'
p = ${p_out}
[]
[]
[Functions]
[mfr_fn]
type = PiecewiseLinear
x = '0 ${ramp_time}'
y = '0 ${mfr_final}'
[]
[]
[ControlLogic]
[mfr_ctrl]
type = TimeFunctionComponentControl
component = bc_inlet
parameter = m_dot
function = mfr_fn
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[VectorPostprocessors]
[pressure_vpp]
type = ADSampler1DReal
block = 'ch_1'
property = 'p'
sort_by = x
execute_on = 'FINAL'
[]
[]
[Executioner]
type = Transient
scheme = bdf2
start_time = 0
end_time = 50
dt = 1
steady_state_detection = true
steady_state_start_time = ${ramp_time}
petsc_options_iname = '-pc_type'
petsc_options_value = ' lu '
nl_rel_tol = 1e-6
nl_abs_tol = 1e-6
nl_max_its = 15
l_tol = 1e-4
l_max_its = 10
[]
[Outputs]
[csv]
type = CSV
create_final_symlink = true
execute_on = 'FINAL'
[]
[]
(modules/thermal_hydraulics/test/tests/components/heat_transfer_from_heat_structure_1phase/hs_boundary.i)
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[SolidProperties]
[sp_ss316]
type = ThermalSS316Properties
[]
[]
[Functions]
[T0_fn]
type = ParsedFunction
expression = '290 + 20 * (y - 1)'
[]
[]
[Components]
[left_wall]
type = SolidWall1Phase
input = 'pipe:in'
[]
[pipe]
type = FlowChannel1Phase
position = '5.0 0 0'
orientation = '1 0 0'
length = 5.0
n_elems = 5
A = 1.0
initial_T = 300
initial_p = 1e5
initial_vel = 0
f = 0
fp = fp
closures = simple_closures
scaling_factor_1phase = '1 1 1e-5'
[]
[right_wall]
type = SolidWall1Phase
input = 'pipe:out'
[]
[heat_transfer]
type = HeatTransferFromHeatStructure1Phase
flow_channel = pipe
hs = heat_structure
hs_boundary = heat_structure:region2:inner
Hw = 1e3
[]
[heat_structure]
type = HeatStructureCylindrical
position = '0 0 0'
orientation = '1 0 0'
length = '5.0 5.0'
n_elems = '5 5'
axial_region_names = 'region1 region2'
names = 'main'
solid_properties = 'sp_ss316'
solid_properties_T_ref = '500'
widths = '1.0'
n_part_elems = '1'
inner_radius = 1.0
initial_T = 500
scaling_factor_temperature = 1e-8
[]
[]
[Postprocessors]
[T_avg]
type = ElementAverageValue
block = 'pipe'
variable = T
execute_on = 'INITIAL TIMESTEP_END'
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'bdf2'
dt = 0.01
num_steps = 1
solve_type = NEWTON
nl_rel_tol = 0
nl_abs_tol = 1e-6
nl_max_its = 15
l_tol = 1e-3
l_max_its = 10
[]
[Outputs]
csv = true
[]
(modules/navier_stokes/test/tests/finite_volume/ins/boussinesq/transient-wcnsfv.i)
mu = 1
rho = 'rho'
k = 1
cp = 1
l = 10
velocity_interp_method = 'rc'
advected_interp_method = 'average'
cold_temp=300
hot_temp=310
[GlobalParams]
two_term_boundary_expansion = true
rhie_chow_user_object = 'rc'
[]
[UserObjects]
[rc]
type = INSFVRhieChowInterpolator
u = u
v = v
pressure = pressure
[]
[]
[Mesh]
[gen]
type = GeneratedMeshGenerator
dim = 2
xmin = 0
xmax = ${l}
ymin = 0
ymax = ${l}
nx = 16
ny = 16
[]
[]
[Variables]
[u]
type = INSFVVelocityVariable
initial_condition = 1e-15
[]
[v]
type = INSFVVelocityVariable
initial_condition = 1e-15
[]
[pressure]
type = INSFVPressureVariable
initial_condition = 1e5
[]
[T]
type = INSFVEnergyVariable
scaling = 1e-4
initial_condition = ${cold_temp}
[]
[]
[AuxVariables]
[U]
order = CONSTANT
family = MONOMIAL
fv = true
[]
[vel_x]
order = FIRST
family = MONOMIAL
[]
[vel_y]
order = FIRST
family = MONOMIAL
[]
[viz_T]
order = FIRST
family = MONOMIAL
[]
[]
[AuxKernels]
[mag]
type = VectorMagnitudeAux
variable = U
x = u
y = v
execute_on = 'initial timestep_end'
[]
[vel_x]
type = ParsedAux
variable = vel_x
expression = 'u'
execute_on = 'initial timestep_end'
coupled_variables = 'u'
[]
[vel_y]
type = ParsedAux
variable = vel_y
expression = 'v'
execute_on = 'initial timestep_end'
coupled_variables = 'v'
[]
[viz_T]
type = ParsedAux
variable = viz_T
expression = 'T'
execute_on = 'initial timestep_end'
coupled_variables = 'T'
[]
[]
[FVKernels]
[mass_time]
type = WCNSFVMassTimeDerivative
variable = pressure
drho_dt = drho_dt
[]
[mass]
type = WCNSFVMassAdvection
variable = pressure
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = ${rho}
[]
[u_time]
type = WCNSFVMomentumTimeDerivative
variable = u
drho_dt = drho_dt
rho = rho
momentum_component = 'x'
[]
[u_advection]
type = INSFVMomentumAdvection
variable = u
velocity_interp_method = ${velocity_interp_method}
advected_interp_method = ${advected_interp_method}
rho = ${rho}
momentum_component = 'x'
[]
[u_viscosity]
type = INSFVMomentumDiffusion
variable = u
mu = ${mu}
momentum_component = 'x'
[]
[u_pressure]
type = INSFVMomentumPressure
variable = u
momentum_component = 'x'
pressure = pressure
[]
[u_gravity]
type = INSFVMomentumGravity
variable = u
gravity = '0 -1 0'
rho = ${rho}
momentum_component = 'x'
[]
[v_time]
type = WCNSFVMomentumTimeDerivative
variable = v
drho_dt = drho_dt
rho = rho
momentum_component = 'y'
[]
[v_advection]
type = INSFVMomentumAdvection
variable = v
velocity_interp_method = ${velocity_interp_method}
advected_interp_method = ${advected_interp_method}
rho = ${rho}
momentum_component = 'y'
[]
[v_viscosity]
type = INSFVMomentumDiffusion
variable = v
mu = ${mu}
momentum_component = 'y'
[]
[v_pressure]
type = INSFVMomentumPressure
variable = v
momentum_component = 'y'
pressure = pressure
[]
[v_gravity]
type = INSFVMomentumGravity
variable = v
gravity = '0 -1 0'
rho = ${rho}
momentum_component = 'y'
[]
[temp_conduction]
type = FVDiffusion
coeff = 'k'
variable = T
[]
[temp_advection]
type = INSFVEnergyAdvection
variable = T
velocity_interp_method = ${velocity_interp_method}
advected_interp_method = ${advected_interp_method}
[]
[]
[FVBCs]
[no_slip_x]
type = INSFVNoSlipWallBC
variable = u
boundary = 'left right top bottom'
function = 0
[]
[no_slip_y]
type = INSFVNoSlipWallBC
variable = v
boundary = 'left right top bottom'
function = 0
[]
[T_hot]
type = FVDirichletBC
variable = T
boundary = left
value = ${hot_temp}
[]
[T_cold]
type = FVDirichletBC
variable = T
boundary = right
value = ${cold_temp}
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[FunctorMaterials]
[const_functor]
type = ADGenericFunctorMaterial
prop_names = 'cp k'
prop_values = '${cp} ${k}'
[]
[rho]
type = RhoFromPTFunctorMaterial
fp = fp
temperature = T
pressure = pressure
[]
[ins_fv]
type = INSFVEnthalpyFunctorMaterial
temperature = 'T'
rho = ${rho}
[]
[]
[Functions]
[lid_function]
type = ParsedFunction
expression = '4*x*(1-x)'
[]
[]
[Executioner]
type = Transient
solve_type = 'NEWTON'
petsc_options_iname = '-pc_type -pc_factor_shift_type'
petsc_options_value = 'lu NONZERO'
steady_state_detection = true
[TimeStepper]
type = IterationAdaptiveDT
dt = 1e-5
optimal_iterations = 6
[]
nl_abs_tol = 1e-9
normalize_solution_diff_norm_by_dt = false
nl_max_its = 10
[]
[Outputs]
[out]
type = Exodus
[]
[]
(modules/navier_stokes/test/tests/finite_volume/cns/benchmark_shock_tube_1D/hllc_sod_shocktube.i)
rho_left = 1
E_left = 2.501505578
u_left = 1e-15
rho_right = 0.125
E_right = 1.999770935
u_right = 1e-15
middle = 50
[GlobalParams]
fp = fp
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 1
xmin = 0
xmax = ${fparse 2 * middle}
nx = 1000
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Variables]
[rho]
order = CONSTANT
family = MONOMIAL
fv = true
[]
[rho_u]
order = CONSTANT
family = MONOMIAL
fv = true
[]
[rho_E]
order = CONSTANT
family = MONOMIAL
fv = true
[]
[]
[AuxVariables]
[rho_a]
order = CONSTANT
family = MONOMIAL
[]
[]
[FVKernels]
[mass_time]
type = FVTimeKernel
variable = rho
[]
[mass_advection]
type = CNSFVMassHLLC
variable = rho
[]
[momentum_time]
type = FVTimeKernel
variable = rho_u
[]
[momentum_advection]
type = CNSFVMomentumHLLC
variable = rho_u
momentum_component = x
[]
[fluid_energy_time]
type = FVTimeKernel
variable = rho_E
[../]
[fluid_energy_advection]
type = CNSFVFluidEnergyHLLC
variable = rho_E
[]
[]
[FVBCs]
[mass_implicit]
type = CNSFVHLLCMassImplicitBC
variable = rho
fp = fp
boundary = 'left right'
[]
[mom_implicit]
type = CNSFVHLLCMomentumImplicitBC
variable = rho_u
momentum_component = x
fp = fp
boundary = 'left right'
[]
[fluid_energy_implicit]
type = CNSFVHLLCFluidEnergyImplicitBC
variable = rho_E
fp = fp
boundary = 'left right'
[]
[]
[ICs]
[rho_ic]
type = FunctionIC
variable = rho
function = 'if (x < ${middle}, ${rho_left}, ${rho_right})'
[]
[rho_u_ic]
type = FunctionIC
variable = rho_u
function = 'if (x < ${middle}, ${fparse rho_left * u_left}, ${fparse rho_right * u_right})'
[]
[rho_E_ic]
type = FunctionIC
variable = rho_E
function = 'if (x < ${middle}, ${fparse E_left * rho_left}, ${fparse E_right * rho_right})'
[]
[]
[Materials]
[var_mat]
type = ConservedVarValuesMaterial
rho = rho
rhou = rho_u
rho_et = rho_E
fp = fp
[]
[]
[Preconditioning]
active = ''
[./smp]
type = SMP
full = true
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
[../]
[]
[Executioner]
type = Transient
[TimeIntegrator]
type = ExplicitSSPRungeKutta
order = 2
[]
l_tol = 1e-8
start_time = 0.0
dt = 1e-2
end_time = 20
abort_on_solve_fail = true
[]
[Outputs]
exodus = true
perf_graph = true
[]
(modules/navier_stokes/test/tests/finite_volume/cns/straight_channel_porosity_step/dc.i)
p_initial=1.01e5
T=273.15
# u refers to the superficial velocity
u_in=1
rho_in=1.30524
sup_mom_y_in=${fparse u_in * rho_in}
user_limiter='min_mod'
friction_coeff=10
[GlobalParams]
fp = fp
two_term_boundary_expansion = true
limiter = ${user_limiter}
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 2
xmin = 0
xmax = 1
nx = 3
ymin = 0
ymax = 18
ny = 90
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Problem]
fv_bcs_integrity_check = false
[]
[Variables]
[pressure]
type = MooseVariableFVReal
initial_condition = ${p_initial}
[]
[sup_mom_x]
type = MooseVariableFVReal
initial_condition = 1e-15
[]
[sup_mom_y]
type = MooseVariableFVReal
initial_condition = 1e-15
[]
[T_fluid]
type = MooseVariableFVReal
initial_condition = ${T}
[]
[]
[AuxVariables]
[vel_y]
type = MooseVariableFVReal
[]
[rho]
type = MooseVariableFVReal
[]
[eps]
type = MooseVariableFVReal
[]
[]
[AuxKernels]
[vel_y]
type = ADMaterialRealAux
variable = vel_y
property = vel_y
execute_on = 'timestep_end'
[]
[rho]
type = ADMaterialRealAux
variable = rho
property = rho
execute_on = 'timestep_end'
[]
[eps]
type = MaterialRealAux
variable = eps
property = porosity
execute_on = 'timestep_end'
[]
[]
[FVKernels]
[mass_time]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rho_dt'
variable = pressure
[]
[mass_advection]
type = PCNSFVKTDC
variable = pressure
eqn = "mass"
[]
[momentum_time]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rhou_dt'
variable = sup_mom_x
[]
[momentum_advection]
type = PCNSFVKTDC
variable = sup_mom_x
eqn = "momentum"
momentum_component = 'x'
[]
[eps_grad]
type = PNSFVPGradEpsilon
variable = sup_mom_x
momentum_component = 'x'
epsilon_function = 'eps'
[]
[drag]
type = PCNSFVMomentumFriction
variable = sup_mom_x
momentum_component = 'x'
Darcy_name = 'cl'
momentum_name = superficial_rhou
[]
[momentum_time_y]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rhov_dt'
variable = sup_mom_y
[]
[momentum_advection_y]
type = PCNSFVKTDC
variable = sup_mom_y
eqn = "momentum"
momentum_component = 'y'
[]
[eps_grad_y]
type = PNSFVPGradEpsilon
variable = sup_mom_y
momentum_component = 'y'
epsilon_function = 'eps'
[]
[drag_y]
type = PCNSFVMomentumFriction
variable = sup_mom_y
momentum_component = 'y'
Darcy_name = 'cl'
momentum_name = superficial_rhov
[]
[energy_time]
type = FVMatPropTimeKernel
mat_prop_time_derivative = 'dsuperficial_rho_et_dt'
variable = T_fluid
[]
[energy_advection]
type = PCNSFVKTDC
variable = T_fluid
eqn = "energy"
[]
[]
[FVBCs]
[rho_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = pressure
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'mass'
velocity_function_includes_rho = true
[]
[rhou_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = sup_mom_x
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'momentum'
momentum_component = 'x'
velocity_function_includes_rho = true
[]
[rhov_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = sup_mom_y
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'momentum'
momentum_component = 'y'
velocity_function_includes_rho = true
[]
[rho_et_bottom]
type = PCNSFVStrongBC
boundary = 'bottom'
variable = T_fluid
superficial_velocity = 'ud_in'
T_fluid = ${T}
eqn = 'energy'
velocity_function_includes_rho = true
[]
[rho_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = pressure
pressure = ${p_initial}
eqn = 'mass'
[]
[rhou_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = sup_mom_x
pressure = ${p_initial}
eqn = 'momentum'
momentum_component = 'x'
[]
[rhov_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = sup_mom_y
pressure = ${p_initial}
eqn = 'momentum'
momentum_component = 'y'
[]
[rho_et_top]
type = PCNSFVStrongBC
boundary = 'top'
variable = T_fluid
pressure = ${p_initial}
eqn = 'energy'
[]
[wall_pressure_x]
type = PCNSFVImplicitMomentumPressureBC
momentum_component = 'x'
boundary = 'left right'
variable = sup_mom_x
[]
[wall_pressure_y]
type = PCNSFVImplicitMomentumPressureBC
momentum_component = 'y'
boundary = 'left right'
variable = sup_mom_y
[]
# Use these to help create more accurate cell centered gradients for cells adjacent to boundaries
[T_bottom]
type = FVDirichletBC
variable = T_fluid
value = ${T}
boundary = 'bottom'
[]
[sup_mom_x_bottom_and_walls]
type = FVDirichletBC
variable = sup_mom_x
value = 0
boundary = 'bottom left right'
[]
[sup_mom_y_walls]
type = FVDirichletBC
variable = sup_mom_y
value = 0
boundary = 'left right'
[]
[sup_mom_y_bottom]
type = FVDirichletBC
variable = sup_mom_y
value = ${sup_mom_y_in}
boundary = 'bottom'
[]
[p_top]
type = FVDirichletBC
variable = pressure
value = ${p_initial}
boundary = 'top'
[]
[]
[Functions]
[ud_in]
type = ParsedVectorFunction
expression_x = '0'
expression_y = '${sup_mom_y_in}'
[]
[eps]
type = ParsedFunction
expression = 'if(y < 2.8, 1,
if(y < 3.2, 1 - .5 / .4 * (y - 2.8),
if(y < 6.8, .5,
if(y < 7.2, .5 - .25 / .4 * (y - 6.8),
if(y < 10.8, .25,
if(y < 11.2, .25 + .25 / .4 * (y - 10.8),
if(y < 14.8, .5,
if(y < 15.2, .5 + .5 / .4 * (y - 14.8),
1))))))))'
[]
[]
[Materials]
[var_mat]
type = PorousMixedVarMaterial
pressure = pressure
T_fluid = T_fluid
superficial_rhou = sup_mom_x
superficial_rhov = sup_mom_y
porosity = porosity
[]
[porosity]
type = GenericFunctionMaterial
prop_names = 'porosity'
prop_values = 'eps'
[]
[ad_generic]
type = ADGenericConstantVectorMaterial
prop_names = 'cl'
prop_values = '${friction_coeff} ${friction_coeff} ${friction_coeff}'
[]
[]
[Preconditioning]
[smp]
type = SMP
full = true
[]
[]
[Executioner]
solve_type = NEWTON
line_search = 'bt'
type = Transient
nl_max_its = 20
[TimeStepper]
type = IterationAdaptiveDT
dt = 5e-5
optimal_iterations = 6
growth_factor = 1.2
[]
num_steps = 10
nl_abs_tol = 1e-8
automatic_scaling = true
compute_scaling_once = false
resid_vs_jac_scaling_param = 0.5
verbose = true
steady_state_detection = true
steady_state_tolerance = 1e-8
normalize_solution_diff_norm_by_dt = false
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
[]
[Outputs]
[out]
type = Exodus
[]
[]
[Debug]
show_var_residual_norms = true
[]
[Postprocessors]
active = ''
[num_nl]
type = NumNonlinearIterations
[]
[total_nl]
type = CumulativeValuePostprocessor
postprocessor = num_nl
[]
[]
(modules/fluid_properties/test/tests/fp_interrogator/2ph_ncg_partial_pressure_p_T.i)
[FluidPropertiesInterrogator]
fp = fp_2phase_ncg_partial_pressure
p = 1e5
T = 372.7559289
[]
[FluidProperties]
[fp_water]
type = StiffenedGasFluidProperties
gamma = 2.35
cv = 1816.0
q = -1.167e6
p_inf = 1.0e9
q_prime = 0
k = 0.5
mu = 281.8e-6
M = 0.01801488
[]
[fp_steam]
type = IdealGasFluidProperties
gamma = 1.43
molar_mass = 0.01801488
[]
[fp_2phase]
type = TestTwoPhaseFluidProperties
fp_liquid = fp_water
fp_vapor = fp_steam
[]
[fp_air]
type = IdealGasFluidProperties
[]
[fp_2phase_ncg_partial_pressure]
type = TwoPhaseNCGPartialPressureFluidProperties
fp_2phase = fp_2phase
fp_ncg = fp_air
[]
[]
(modules/fluid_properties/test/tests/materials/fluid_properties_material/test_ph.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 2
ny = 2
elem_type = QUAD4
[]
[Functions]
[fn_1]
type = ParsedFunction
expression = '2e5 * (1 + x)'
[]
[fn_2]
type = ParsedFunction
expression = '2000 * (1 + x*x+y*y)'
[]
[]
[AuxVariables]
[p]
[InitialCondition]
type = FunctionIC
function = fn_1
[]
[]
[h]
[InitialCondition]
type = FunctionIC
function = fn_2
[]
[]
[T]
family = MONOMIAL
order = CONSTANT
[]
[s]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[T]
type = MaterialRealAux
variable = T
property = T
[]
[s]
type = MaterialRealAux
variable = s
property = s
[]
[]
[FluidProperties]
[ideal_gas]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 1.000536678700361
[]
[]
[Materials]
[fp_mat]
type = FluidPropertiesMaterialPH
pressure = p
h = h
fp = ideal_gas
[]
[]
[Executioner]
type = Steady
solve_type = NEWTON
[]
[Problem]
solve = false
[]
[Outputs]
exodus = true
[]
(modules/fluid_properties/test/tests/functions/saturation_density_function/saturation_density_function.i)
# Tests SaturationDensityFunction.
# The gold values are computed as follows:
# T = 5
# p_sat = 3 T = 15
# liquid: rho(p_sat, T) = 0.01046369844
# vapor: rho(p_sat, T) = 0.01804085937
[Mesh]
type = GeneratedMesh
dim = 1
nx = 1
[]
[FluidProperties]
[fp_liquid]
type = IdealGasFluidProperties
[]
[fp_vapor]
type = IdealGasFluidProperties
molar_mass = 0.05
[]
[fp_2phase]
type = TestTwoPhaseFluidProperties
fp_liquid = fp_liquid
fp_vapor = fp_vapor
[]
[]
[Functions]
[T]
type = ConstantFunction
value = 5
[]
[rho_sat_fn]
type = SaturationDensityFunction
T = T
fp_2phase = fp_2phase
use_liquid = true
[]
[]
[Postprocessors]
[rho_sat_pp]
type = FunctionValuePostprocessor
function = rho_sat_fn
execute_on = 'INITIAL'
[]
[]
[Problem]
solve = false
[]
[Executioner]
type = Steady
[]
[Outputs]
csv = true
file_base = liquid
execute_on = 'INITIAL'
[]
(modules/navier_stokes/test/tests/finite_volume/cns/mms/1d-with-bcs/pwcnsfv.i)
rho='rho'
advected_interp_method='upwind'
velocity_interp_method='rc'
gamma=1.4
R=8.3145
molar_mass=29.0e-3
R_specific=${fparse R/molar_mass}
cp=${fparse gamma*R_specific/(gamma-1)}
[GlobalParams]
two_term_boundary_expansion = true
rhie_chow_user_object = 'rc'
[]
[UserObjects]
[rc]
type = PINSFVRhieChowInterpolator
u = sup_vel_x
pressure = pressure
porosity = porosity
[]
[]
[Mesh]
[cartesian]
type = GeneratedMeshGenerator
dim = 1
xmin = .1
xmax = .6
nx = 2
[]
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Problem]
fv_bcs_integrity_check = false
[]
[Variables]
[pressure]
type = INSFVPressureVariable
[]
[sup_vel_x]
type = PINSFVSuperficialVelocityVariable
[]
[]
[AuxVariables]
[porosity]
type = MooseVariableFVReal
[]
[T_fluid]
type = INSFVEnergyVariable
[]
[]
[ICs]
[pressure]
type = FunctionIC
variable = pressure
function = 'exact_p'
[]
[sup_vel_x]
type = FunctionIC
variable = sup_vel_x
function = 'exact_sup_vel_x'
[]
[T_fluid]
type = FunctionIC
variable = T_fluid
function = 'exact_T'
[]
[eps]
type = FunctionIC
variable = porosity
function = 'eps'
[]
[]
[FVKernels]
[mass_advection]
type = PINSFVMassAdvection
variable = pressure
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = ${rho}
[]
[mass_fn]
type = FVBodyForce
variable = pressure
function = 'forcing_rho'
[]
[u_advection]
type = PINSFVMomentumAdvection
variable = sup_vel_x
advected_interp_method = ${advected_interp_method}
velocity_interp_method = ${velocity_interp_method}
rho = ${rho}
porosity = porosity
momentum_component = 'x'
[]
[u_pressure]
type = PINSFVMomentumPressureFlux
variable = sup_vel_x
pressure = pressure
porosity = porosity
momentum_component = 'x'
force_boundary_execution = false
[]
[momentum_fn]
type = INSFVBodyForce
variable = sup_vel_x
functor = 'forcing_rho_ud'
momentum_component = 'x'
[]
[]
[FVBCs]
[mass]
variable = pressure
type = PINSFVFunctorBC
boundary = 'left right'
superficial_vel_x = sup_vel_x
pressure = pressure
eqn = 'mass'
porosity = porosity
[]
[momentum]
variable = sup_vel_x
type = PINSFVFunctorBC
boundary = 'left right'
superficial_vel_x = sup_vel_x
pressure = pressure
eqn = 'momentum'
momentum_component = 'x'
porosity = porosity
[]
# help gradient reconstruction *and* create Dirichlet values for use in PINSFVFunctorBC
[pressure_right]
type = FVFunctionDirichletBC
variable = pressure
function = exact_p
boundary = 'right'
[]
[sup_vel_x_left]
type = FVFunctionDirichletBC
variable = sup_vel_x
function = exact_sup_vel_x
boundary = 'left'
[]
[T_fluid_left]
type = FVFunctionDirichletBC
variable = T_fluid
function = exact_T
boundary = 'left'
[]
[]
[FunctorMaterials]
[const_functor]
type = ADGenericFunctorMaterial
prop_names = 'cp'
prop_values = '${cp}'
[]
[rho]
type = RhoFromPTFunctorMaterial
fp = fp
temperature = T_fluid
pressure = pressure
[]
[ins_fv]
type = INSFVEnthalpyFunctorMaterial
temperature = T_fluid
rho = ${rho}
[]
[]
[Functions]
[forcing_rho]
type = ParsedFunction
expression = '-3.45300378856215*sin(1.1*x)'
[]
[forcing_rho_ud]
type = ParsedFunction
expression = '-0.9*(10.6975765229419*cos(1.2*x)/cos(x) - 0.697576522941849*cos(1.1*x)^2/cos(x)^2)*sin(x) + 0.9*(10.6975765229419*sin(x)*cos(1.2*x)/cos(x)^2 - 1.3951530458837*sin(x)*cos(1.1*x)^2/cos(x)^3 + 1.53466835047207*sin(1.1*x)*cos(1.1*x)/cos(x)^2 - 12.8370918275302*sin(1.2*x)/cos(x))*cos(x) + 3.13909435323832*sin(x)*cos(1.1*x)^2/cos(x)^2 - 6.9060075771243*sin(1.1*x)*cos(1.1*x)/cos(x)'
[]
[exact_T]
type = ParsedFunction
expression = '0.0106975765229418*cos(1.2*x)/cos(x) - 0.000697576522941848*cos(1.1*x)^2/cos(x)^2'
[]
[exact_p]
type = ParsedFunction
expression = '3.48788261470924*(3.06706896551724*cos(1.2*x)/cos(x) - 0.2*cos(1.1*x)^2/cos(x)^2)*cos(x)'
[]
[exact_sup_vel_x]
type = ParsedFunction
expression = '0.9*cos(1.1*x)/cos(x)'
[]
[eps]
type = ParsedFunction
expression = '0.9'
[]
[]
[Executioner]
solve_type = NEWTON
type = Transient
num_steps = 1
dtmin = 1
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_max_its = 50
line_search = bt
nl_rel_tol = 1e-12
nl_abs_tol = 1e-12
[]
[Outputs]
exodus = true
csv = true
[]
[Debug]
show_var_residual_norms = true
[]
[Postprocessors]
[h]
type = AverageElementSize
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2pressure]
type = ElementL2FunctorError
approximate = pressure
exact = exact_p
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[L2sup_vel_x]
approximate = sup_vel_x
exact = exact_sup_vel_x
type = ElementL2FunctorError
outputs = 'console csv'
execute_on = 'timestep_end'
[]
[]
(modules/navier_stokes/test/tests/finite_volume/cns/shock_tube_2D_cavity/hllc_sod_shocktube_2D.i)
rho_left = 1
E_left = 2.501505578
u_left = 1e-15
rho_right = 0.125
E_right = 1.999770935
u_right = 1e-15
x_sep = 35
[GlobalParams]
fp = fp
[]
[Mesh]
[./cartesian]
type = CartesianMeshGenerator
dim = 2
dx = '40 20'
ix = '200 100'
dy = '1 20 2 20 1'
iy = '4 100 10 100 4'
subdomain_id = '0 0
0 1
1 1
0 1
0 0'
[../]
[./wall]
type = SideSetsBetweenSubdomainsGenerator
input = cartesian
primary_block = 1
paired_block = 0
new_boundary = 'wall'
[../]
[./delete]
type = BlockDeletionGenerator
input = wall
block = 0
[../]
[]
[FluidProperties]
[./fp]
type = IdealGasFluidProperties
allow_imperfect_jacobians = true
[../]
[]
[Variables]
[./rho]
order = CONSTANT
family = MONOMIAL
fv = true
[../]
[./rho_u]
order = CONSTANT
family = MONOMIAL
fv = true
[../]
[./rho_v]
order = CONSTANT
family = MONOMIAL
fv = true
[../]
[./rho_E]
order = CONSTANT
family = MONOMIAL
fv = true
[../]
[]
[AuxVariables]
[./Ma]
order = CONSTANT
family = MONOMIAL
[../]
[./p]
order = CONSTANT
family = MONOMIAL
[../]
[./v_norm]
order = CONSTANT
family = MONOMIAL
[../]
[./temperature]
order = CONSTANT
family = MONOMIAL
[../]
[]
[AuxKernels]
[./Ma_aux]
type = NSMachAux
variable = Ma
fluid_properties = fp
use_material_properties = true
[../]
[./p_aux]
type = ADMaterialRealAux
variable = p
property = pressure
[../]
[./v_norm_aux]
type = ADMaterialRealAux
variable = v_norm
property = speed
[../]
[./temperature_aux]
type = ADMaterialRealAux
variable = temperature
property = T_fluid
[../]
[]
[FVKernels]
[./mass_time]
type = FVTimeKernel
variable = rho
[../]
[./mass_advection]
type = CNSFVMassHLLC
variable = rho
[../]
[./momentum_x_time]
type = FVTimeKernel
variable = rho_u
[../]
[./momentum_x_advection]
type = CNSFVMomentumHLLC
variable = rho_u
momentum_component = x
[../]
[./momentum_y_time]
type = FVTimeKernel
variable = rho_v
[../]
[./momentum_y_advection]
type = CNSFVMomentumHLLC
variable = rho_v
momentum_component = y
[../]
[./fluid_energy_time]
type = FVTimeKernel
variable = rho_E
[../]
[./fluid_energy_advection]
type = CNSFVFluidEnergyHLLC
variable = rho_E
[../]
[]
[FVBCs]
[./mom_x_pressure]
type = CNSFVMomImplicitPressureBC
variable = rho_u
momentum_component = x
boundary = 'left right wall'
[../]
[./mom_y_pressure]
type = CNSFVMomImplicitPressureBC
variable = rho_v
momentum_component = y
boundary = 'wall'
[../]
[]
[ICs]
[./rho_ic]
type = FunctionIC
variable = rho
function = 'if (x < ${x_sep}, ${rho_left}, ${rho_right})'
[../]
[./rho_u_ic]
type = FunctionIC
variable = rho_u
function = 'if (x < ${x_sep}, ${fparse rho_left * u_left}, ${fparse rho_right * u_right})'
[../]
[./rho_E_ic]
type = FunctionIC
variable = rho_E
function = 'if (x < ${x_sep}, ${fparse E_left * rho_left}, ${fparse E_right * rho_right})'
[../]
[]
[Materials]
[./var_mat]
type = ConservedVarValuesMaterial
rho = rho
rhou = rho_u
rhov = rho_v
rho_et = rho_E
fp = fp
[../]
[./sound_speed]
type = SoundspeedMat
fp = fp
[../]
[]
[Preconditioning]
[./smp]
type = SMP
full = true
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
[../]
[]
[Postprocessors]
[./cfl_dt]
type = ADCFLTimeStepSize
c_names = 'sound_speed'
vel_names = 'speed'
[../]
[]
[Executioner]
type = Transient
end_time = 100
[TimeIntegrator]
type = ExplicitSSPRungeKutta
order = 2
[]
l_tol = 1e-8
[./TimeStepper]
type = PostprocessorDT
postprocessor = cfl_dt
[../]
[]
(modules/thermal_hydraulics/test/tests/components/heat_transfer_from_heat_structure_1phase/phy.heat_structure_multiple_3eqn.i)
# Tests that energy conservation is satisfied in 1-phase flow when there are
# multiple heat structures are connected to the same pipe.
#
# This problem has 2 heat structures with different material properties and
# initial conditions connected to the same flow channel, which has solid wall
# boundary conditions at both ends. An ideal gas equation of state is used for
# the fluid:
# e(T) = cv * T
# From energy conservation, an analytic expression for the steady-state
# temperature results:
# (rho(p,T)*e(T)*V)_fluid + (rho*cp*T*V)_hs1 + (rho*cp*T*V)_hs2 = constant
# The following are constant:
# V_i domain volumes for flow channel and heat structures
# rho_fluid fluid density (due to conservation of mass)
# rho_hsi heat structure densities
# cp_hsi heat structure specific heats
# Furthermore, all volumes are set equal to 1. Therefore the expression for the
# steady-state temperature is the following:
# T = E0 / C0
# where
# E0 = (rho(p0,T0)*e(T0))_fluid + (rho*cp*T0)_hs1 + (rho*cp*T0)_hs2
# C0 = (rho(p0,T0)*cv)_fluid + (rho*cp)_hs1 + (rho*cp)_hs2
#
# An ideal gas is defined by (gamma, R), and the relation between R and cv is as
# follows:
# cp = gamma * R / (gamma - 1)
# cv = cp / gamma = R / (gamma - 1)
# For the EOS parameters
# gamma = 1.0001
# R = 100 J/kg-K
# the relevant specific heat is
# cv = 1e6 J/kg-K
#
# For the initial conditions
# p = 100 kPa
# T = 300 K
# the density and specific internal energy should be
# rho = 3.3333333333333 kg/m^3
# e = 300000000 J/kg
#
# The following heat structure parameters are used:
# T0_hs1 = 290 K T0_hs2 = 310 K
# rho_hs1 = 8000 kg/m^3 rho_hs2 = 6000 kg/m^3
# cp_hs1 = 500 J/kg-K cp_hs2 = 600 J/kg-K
#
# E0 = 1e9 + 8000 * 500 * 290 + 6000 * 600 * 310
# = 3276000000 J
# C0 = 3.3333333333333e6 + 8000 * 500 + 6000 * 600
# = 10933333.3333333 J/K
# T = E0 / C0
# = 3276000000 / 10933333.3333333
# = 299.6341463414643 K
#
T1 = 290
k1 = 50
rho1 = 8000
cp1 = 500
T2 = 310
k2 = 100
rho2 = 6000
cp2 = 600
[GlobalParams]
gravity_vector = '0 0 0'
initial_T = 300
initial_p = 100e3
initial_vel = 0
scaling_factor_1phase = '1e-3 1e-3 1e-8'
closures = simple_closures
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
gamma = 1.0001
molar_mass = 0.083144598
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[SolidProperties]
[hs1_mat]
type = ThermalFunctionSolidProperties
k = ${k1}
rho = ${rho1}
cp = ${cp1}
[]
[hs2_mat]
type = ThermalFunctionSolidProperties
k = ${k2}
rho = ${rho2}
cp = ${cp2}
[]
[]
[Components]
[pipe]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = 1
n_elems = 10
A = 1
f = 0
fp = fp
[]
[hs1]
type = HeatStructurePlate
position = '0 -1 0'
orientation = '1 0 0'
length = 1
depth = 1
n_elems = 10
solid_properties = 'hs1_mat'
solid_properties_T_ref = '300'
n_part_elems = '5'
widths = '1'
names = 'solid'
initial_T = ${T1}
[]
[hs2]
type = HeatStructurePlate
position = '0 -1 0'
orientation = '1 0 0'
length = 1
depth = 1
n_elems = 10
solid_properties = 'hs2_mat'
solid_properties_T_ref = '300'
n_part_elems = '5'
widths = '1'
names = 'solid'
initial_T = ${T2}
[]
[ht1]
type = HeatTransferFromHeatStructure1Phase
hs = hs1
hs_side = outer
flow_channel = pipe
Hw = 1e5
P_hf = 0.5
[]
[ht2]
type = HeatTransferFromHeatStructure1Phase
hs = hs2
hs_side = outer
flow_channel = pipe
Hw = 1e5
P_hf = 0.5
[]
[left]
type = SolidWall1Phase
input = 'pipe:in'
[]
[right]
type = SolidWall1Phase
input = 'pipe:out'
[]
[]
[Preconditioning]
[preconditioner]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'bdf2'
start_time = 0
end_time = 4e5
dt = 1e4
abort_on_solve_fail = true
solve_type = 'newton'
line_search = 'basic'
nl_rel_tol = 0
nl_abs_tol = 1e-6
nl_max_its = 10
l_tol = 1e-3
l_max_its = 100
[Quadrature]
type = GAUSS
order = SECOND
[]
petsc_options_iname = '-pc_type'
petsc_options_value = ' lu'
[]
[Postprocessors]
[T_steady_state_predicted]
type = FunctionValuePostprocessor
# This value is computed in the input file description
function = 299.6341463414643
[]
[T_fluid_average]
type = ElementAverageValue
variable = T
block = pipe
[]
[relative_error]
type = RelativeDifferencePostprocessor
value1 = T_steady_state_predicted
value2 = T_fluid_average
[]
[]
[Outputs]
[out]
type = CSV
show = 'relative_error'
execute_on = 'final'
[]
[]
(modules/thermal_hydraulics/test/tests/problems/william_louis/4pipes_closed.i)
# Junction of 4 pipes:
#
# 4
# |
# 1 -----*----- 3
# |
# 2
#
# The left end of Pipe 1 is a high-pressure region, and the rest of the system
# is at a low pressure.
#
# All pipes are closed.
end_time = 0.07
D_pipe = 0.01
A_pipe = ${fparse 0.25 * pi * D_pipe^2}
length_pipe1_HP = 0.53
length_pipe1_LP = 3.10
length_pipe2 = 2.595
length_pipe3 = 1.725
length_pipe4 = 0.845
x_junction = ${fparse length_pipe1_HP + length_pipe1_LP}
# Numbers of elements correspond to dx ~ 1/3 cm
n_elems_pipe1_HP = 159
n_elems_pipe1_LP = 930
n_elems_pipe2 = 779
n_elems_pipe3 = 518
n_elems_pipe4 = 254
S_junction = ${fparse 4 * A_pipe}
r_junction = ${fparse sqrt(S_junction / (4 * pi))}
V_junction = ${fparse 4/3 * pi * r_junction^3}
p_low = 1e5
p_high = 1.15e5
T_initial = 283.5690633 # at p = 1e5 Pa, rho = 1.23 kg/m^3
cfl = 0.95
[GlobalParams]
# common FlowChannel1Phase parameters
A = ${A_pipe}
initial_T = ${T_initial}
initial_vel = 0
fp = fp_air
closures = closures
f = 0
gravity_vector = '0 0 0'
scaling_factor_1phase = '1 1 1e-5'
[]
[FluidProperties]
[fp_air]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 0.029
[]
[]
[Closures]
[closures]
type = Closures1PhaseSimple
[]
[]
[Functions]
[initial_p_pipe1_fn]
type = PiecewiseConstant
axis = x
x = '0 ${length_pipe1_HP}'
y = '${p_high} ${p_low}'
[]
[]
[Components]
[pipe1_wall]
type = SolidWall1Phase
input = 'pipe1:in'
[]
[pipe1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 0 0'
length = '${length_pipe1_HP} ${length_pipe1_LP}'
n_elems = '${n_elems_pipe1_HP} ${n_elems_pipe1_LP}'
initial_p = initial_p_pipe1_fn
[]
[junction]
type = VolumeJunction1Phase
position = '${x_junction} 0 0'
connections = 'pipe1:out pipe2:in pipe3:in pipe4:in'
initial_p = ${p_low}
initial_T = ${T_initial}
initial_vel_x = 0
initial_vel_y = 0
initial_vel_z = 0
volume = ${V_junction}
scaling_factor_rhoEV = 1e-5
apply_velocity_scaling = true
[]
[pipe2]
type = FlowChannel1Phase
position = '${x_junction} 0 0'
orientation = '0 -1 0'
length = ${length_pipe2}
n_elems = ${n_elems_pipe2}
initial_p = ${p_low}
[]
[pipe2_wall]
type = SolidWall1Phase
input = 'pipe2:out'
[]
[pipe3]
type = FlowChannel1Phase
position = '${x_junction} 0 0'
orientation = '1 0 0'
length = ${length_pipe3}
n_elems = ${n_elems_pipe3}
initial_p = ${p_low}
[]
[pipe3_wall]
type = SolidWall1Phase
input = 'pipe3:out'
[]
[pipe4]
type = FlowChannel1Phase
position = '${x_junction} 0 0'
orientation = '0 1 0'
length = ${length_pipe4}
n_elems = ${n_elems_pipe4}
initial_p = ${p_low}
[]
[pipe4_wall]
type = SolidWall1Phase
input = 'pipe4:out'
[]
[]
[Postprocessors]
[cfl_dt]
type = ADCFLTimeStepSize
block = 'pipe1 pipe2 pipe3 pipe4'
CFL = ${cfl}
c_names = 'c'
vel_names = 'vel'
[]
[p_pipe1_048]
type = PointValue
variable = p
point = '${fparse x_junction - 0.48} 0 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_pipe2_052]
type = PointValue
variable = p
point = '${fparse x_junction} -0.52 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_pipe3_048]
type = PointValue
variable = p
point = '${fparse x_junction + 0.48} 0 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_pipe4_043]
type = PointValue
variable = p
point = '${fparse x_junction} 0.43 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
end_time = ${end_time}
[TimeIntegrator]
type = ExplicitSSPRungeKutta
order = 1
[]
[TimeStepper]
type = PostprocessorDT
postprocessor = cfl_dt
[]
abort_on_solve_fail = true
solve_type = LINEAR
[]
[Times]
[output_times]
type = TimeIntervalTimes
time_interval = 7e-4
[]
[]
[Outputs]
file_base = '4pipes_closed'
[csv]
type = CSV
show = 'p_pipe1_048 p_pipe2_052 p_pipe3_048 p_pipe4_043'
sync_only = true
sync_times_object = output_times
[]
[console]
type = Console
execute_postprocessors_on = 'NONE'
[]
[]
(modules/thermal_hydraulics/test/tests/functormaterials/conjugate_ht_numbers/conjugate_ht_numbers.i)
p_fluid = 1e5
T_fluid = 300
T_solid = 500
[Mesh]
type = GeneratedMesh
dim = 1
nx = 1
[]
[FluidProperties]
[fp_air]
type = IdealGasFluidProperties
[]
[]
[FunctorMaterials]
[q_fmat]
type = ADConjugateHTNumbersFunctorMaterial
Pr_name = Pr
Gr_name = Gr
p_fluid = ${p_fluid}
T_fluid = ${T_fluid}
T_solid = ${T_solid}
length = 0.01
fluid_properties = fp_air
[]
[]
[Postprocessors]
[Pr]
type = ADElementExtremeFunctorValue
functor = Pr
execute_on = 'INITIAL'
[]
[Gr]
type = ADElementExtremeFunctorValue
functor = Gr
execute_on = 'INITIAL'
[]
[]
[Problem]
solve = false
[]
[Executioner]
type = Steady
[]
[Outputs]
csv = true
execute_on = 'INITIAL'
[]
(modules/thermal_hydraulics/test/tests/output/vector_velocity/test.i)
[GlobalParams]
initial_vel = 0
initial_vel_x = 0
initial_vel_y = 0
initial_vel_z = 0
initial_p = 1e5
initial_T = 300
f = 0.1
closures = simple_closures
fp = fp
[]
[FluidProperties]
[fp]
type = IdealGasFluidProperties
[]
[]
[Closures]
[simple_closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[inlet]
type = InletMassFlowRateTemperature1Phase
input = 'fch1:in'
m_dot = 1
T = 300
[]
[fch1]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '1 1 1'
length = 1.73205
n_elems = 5
A = 1
[]
[junction]
type = VolumeJunction1Phase
position = '1 1 1'
connections = 'fch1:out fch2:out'
volume = 0.1
[]
[fch2]
type = FlowChannel1Phase
position = '2 2 2'
orientation = '-1 -1 -1'
length = 1.73205
n_elems = 5
A = 2
[]
[outlet]
type = Outlet1Phase
input = 'fch2:in'
p = 1e5
[]
[]
[Executioner]
type = Transient
dt = 0.5
num_steps = 50
solve_type = NEWTON
line_search = basic
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_abs_tol = 1e-6
l_tol = 1e-03
automatic_scaling = true
[]
[Outputs]
print_linear_converged_reason = false
print_nonlinear_converged_reason = false
print_linear_residuals = false
[out]
type = Exodus
sync_only = false
sync_times = '0 5 10 15 20 25'
show = 'vel_x vel_y vel_z'
[]
[]
(modules/fluid_properties/test/tests/materials/fluid_properties_material/test_pt.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 2
ny = 2
elem_type = QUAD4
[]
[Functions]
[fn_1]
type = ParsedFunction
expression = '2e5 * (1 + x)'
[]
[fn_2]
type = ParsedFunction
expression = '300 * (1 + x*x+y*y)'
[]
[]
[AuxVariables]
[pressure]
[InitialCondition]
type = FunctionIC
function = fn_1
[]
[]
[temperature]
[InitialCondition]
type = FunctionIC
function = fn_2
[]
[]
[rho]
family = MONOMIAL
order = CONSTANT
[]
[mu]
family = MONOMIAL
order = CONSTANT
[]
[cp]
family = MONOMIAL
order = CONSTANT
[]
[cv]
family = MONOMIAL
order = CONSTANT
[]
[k]
family = MONOMIAL
order = CONSTANT
[]
[h]
family = MONOMIAL
order = CONSTANT
[]
[e]
family = MONOMIAL
order = CONSTANT
[]
[s]
family = MONOMIAL
order = CONSTANT
[]
[c]
family = MONOMIAL
order = CONSTANT
[]
[]
[AuxKernels]
[rho]
type = MaterialRealAux
variable = rho
property = density
[]
[mu]
type = MaterialRealAux
variable = mu
property = viscosity
[]
[cp]
type = MaterialRealAux
variable = cp
property = cp
[]
[cv]
type = MaterialRealAux
variable = cv
property = cv
[]
[k]
type = MaterialRealAux
variable = k
property = k
[]
[h]
type = MaterialRealAux
variable = h
property = h
[]
[e]
type = MaterialRealAux
variable = e
property = e
[]
[s]
type = MaterialRealAux
variable = s
property = s
[]
[c]
type = MaterialRealAux
variable = c
property = c
[]
[]
[FluidProperties]
[ideal_gas]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 1.000536678700361
[]
[]
[Materials]
[fp_mat]
type = FluidPropertiesMaterialPT
pressure = pressure
temperature = temperature
fp = ideal_gas
[]
[]
[Executioner]
type = Steady
solve_type = NEWTON
[]
[Problem]
solve = false
[]
[Outputs]
exodus = true
[]
(modules/thermal_hydraulics/test/tests/problems/brayton_cycle/open_brayton_cycle.i)
# This input file is used to demonstrate a simple open-air Brayton cycle using
# a compressor, turbine, shaft, motor, and generator.
# The flow length is divided into 5 segments as illustrated below, where
# - "(I)" denotes the inlet
# - "(C)" denotes the compressor
# - "(T)" denotes the turbine
# - "(O)" denotes the outlet
# - "*" denotes a fictitious junction
#
# Heated section
# (I)-----(C)-----*--------------*-----(T)-----(O)
# 1 2 3 4 5
#
# Initially the fluid is at rest at ambient conditions, the shaft speed is zero,
# and no heat transfer occurs with the system.
# The transient is controlled as follows:
# * 0 - 100 s: motor ramps up torque linearly from zero
# * 100 - 200 s: motor ramps down torque linearly to zero, HTC ramps up linearly from zero.
# * 200 - 300 s: (no changes; should approach steady condition)
I_motor = 1.0
motor_torque_max = 400.0
I_generator = 1.0
generator_torque_per_shaft_speed = -0.00025
motor_ramp_up_duration = 100.0
motor_ramp_down_duration = 100.0
post_motor_time = 100.0
t1 = ${motor_ramp_up_duration}
t2 = ${fparse t1 + motor_ramp_down_duration}
t3 = ${fparse t2 + post_motor_time}
D1 = 0.15
D2 = ${D1}
D3 = ${D1}
D4 = ${D1}
D5 = ${D1}
A1 = ${fparse 0.25 * pi * D1^2}
A2 = ${fparse 0.25 * pi * D2^2}
A3 = ${fparse 0.25 * pi * D3^2}
A4 = ${fparse 0.25 * pi * D4^2}
A5 = ${fparse 0.25 * pi * D5^2}
L1 = 10.0
L2 = ${L1}
L3 = ${L1}
L4 = ${L1}
L5 = ${L1}
x1 = 0.0
x2 = ${fparse x1 + L1}
x3 = ${fparse x2 + L2}
x4 = ${fparse x3 + L3}
x5 = ${fparse x4 + L4}
x2_minus = ${fparse x2 - 0.001}
x2_plus = ${fparse x2 + 0.001}
x5_minus = ${fparse x5 - 0.001}
x5_plus = ${fparse x5 + 0.001}
n_elems1 = 10
n_elems2 = ${n_elems1}
n_elems3 = ${n_elems1}
n_elems4 = ${n_elems1}
n_elems5 = ${n_elems1}
A_ref_comp = ${fparse 0.5 * (A1 + A2)}
V_comp = ${fparse A_ref_comp * 1.0}
I_comp = 1.0
A_ref_turb = ${fparse 0.5 * (A4 + A5)}
V_turb = ${fparse A_ref_turb * 1.0}
I_turb = 1.0
c0_rated_comp = 351.6925137
rho0_rated_comp = 1.146881112
rated_mfr = 0.25
speed_rated_rpm = 96000
speed_rated = ${fparse speed_rated_rpm * 2 * pi / 60.0}
speed_initial = 0
eff_comp = 0.79
eff_turb = 0.843
T_hot = 1000
T_ambient = 300
p_ambient = 1e5
[GlobalParams]
orientation = '1 0 0'
gravity_vector = '0 0 0'
initial_p = ${p_ambient}
initial_T = ${T_ambient}
initial_vel = 0
initial_vel_x = 0
initial_vel_y = 0
initial_vel_z = 0
fp = fp_air
closures = closures
f = 0
scaling_factor_1phase = '1 1 1e-5'
scaling_factor_rhoV = 1
scaling_factor_rhouV = 1
scaling_factor_rhovV = 1
scaling_factor_rhowV = 1
scaling_factor_rhoEV = 1e-5
rdg_slope_reconstruction = none
[]
[Functions]
[motor_torque_fn]
type = PiecewiseLinear
x = '0 ${t1} ${t2}'
y = '0 ${motor_torque_max} 0'
[]
[motor_power_fn]
type = ParsedFunction
expression = 'torque * speed'
symbol_names = 'torque speed'
symbol_values = 'motor_torque shaft:omega'
[]
[generator_torque_fn]
type = ParsedFunction
expression = 'slope * t'
symbol_names = 'slope'
symbol_values = '${generator_torque_per_shaft_speed}'
[]
[generator_power_fn]
type = ParsedFunction
expression = 'torque * speed'
symbol_names = 'torque speed'
symbol_values = 'generator_torque shaft:omega'
[]
[htc_wall_fn]
type = PiecewiseLinear
x = '0 ${t1} ${t2}'
y = '0 0 1e3'
[]
[]
[FluidProperties]
[fp_air]
type = IdealGasFluidProperties
emit_on_nan = none
[]
[]
[Closures]
[closures]
type = Closures1PhaseSimple
[]
[]
[Components]
[shaft]
type = Shaft
connected_components = 'motor compressor turbine generator'
initial_speed = ${speed_initial}
[]
[motor]
type = ShaftConnectedMotor
inertia = ${I_motor}
torque = 0 # controlled
[]
[generator]
type = ShaftConnectedMotor
inertia = ${I_generator}
torque = generator_torque_fn
[]
[inlet]
type = InletStagnationPressureTemperature1Phase
input = 'pipe1:in'
p0 = ${p_ambient}
T0 = ${T_ambient}
[]
[pipe1]
type = FlowChannel1Phase
position = '${x1} 0 0'
length = ${L1}
n_elems = ${n_elems1}
A = ${A1}
[]
[compressor]
type = ShaftConnectedCompressor1Phase
position = '${x2} 0 0'
inlet = 'pipe1:out'
outlet = 'pipe2:in'
A_ref = ${A_ref_comp}
volume = ${V_comp}
omega_rated = ${speed_rated}
mdot_rated = ${rated_mfr}
c0_rated = ${c0_rated_comp}
rho0_rated = ${rho0_rated_comp}
speeds = '0.5208 0.6250 0.7292 0.8333 0.9375'
Rp_functions = 'rp_comp1 rp_comp2 rp_comp3 rp_comp4 rp_comp5'
eff_functions = 'eff_comp1 eff_comp2 eff_comp3 eff_comp4 eff_comp5'
min_pressure_ratio = 1.0
speed_cr_I = 0
inertia_const = ${I_comp}
inertia_coeff = '${I_comp} 0 0 0'
# assume no shaft friction
speed_cr_fr = 0
tau_fr_const = 0
tau_fr_coeff = '0 0 0 0'
[]
[pipe2]
type = FlowChannel1Phase
position = '${x2} 0 0'
length = ${L2}
n_elems = ${n_elems2}
A = ${A2}
[]
[junction2_3]
type = JunctionOneToOne1Phase
connections = 'pipe2:out pipe3:in'
[]
[pipe3]
type = FlowChannel1Phase
position = '${x3} 0 0'
length = ${L3}
n_elems = ${n_elems3}
A = ${A3}
[]
[junction3_4]
type = JunctionOneToOne1Phase
connections = 'pipe3:out pipe4:in'
[]
[pipe4]
type = FlowChannel1Phase
position = '${x4} 0 0'
length = ${L4}
n_elems = ${n_elems4}
A = ${A4}
[]
[turbine]
type = ShaftConnectedCompressor1Phase
position = '${x5} 0 0'
inlet = 'pipe4:out'
outlet = 'pipe5:in'
A_ref = ${A_ref_turb}
volume = ${V_turb}
treat_as_turbine = true
omega_rated = ${speed_rated}
mdot_rated = ${rated_mfr}
c0_rated = ${c0_rated_comp}
rho0_rated = ${rho0_rated_comp}
speeds = '0 0.5208 0.6250 0.7292 0.8333 0.9375'
Rp_functions = 'rp_turb0 rp_turb1 rp_turb2 rp_turb3 rp_turb4 rp_turb5'
eff_functions = 'eff_turb1 eff_turb1 eff_turb2 eff_turb3 eff_turb4 eff_turb5'
min_pressure_ratio = 1.0
speed_cr_I = 0
inertia_const = ${I_turb}
inertia_coeff = '${I_turb} 0 0 0'
# assume no shaft friction
speed_cr_fr = 0
tau_fr_const = 0
tau_fr_coeff = '0 0 0 0'
[]
[pipe5]
type = FlowChannel1Phase
position = '${x5} 0 0'
length = ${L5}
n_elems = ${n_elems5}
A = ${A5}
[]
[outlet]
type = Outlet1Phase
input = 'pipe5:out'
p = ${p_ambient}
[]
[heating]
type = HeatTransferFromSpecifiedTemperature1Phase
flow_channel = pipe3
T_wall = ${T_hot}
Hw = htc_wall_fn
[]
[]
[ControlLogic]
[motor_ctrl]
type = TimeFunctionComponentControl
component = motor
parameter = torque
function = motor_torque_fn
[]
[]
[Postprocessors]
[heating_rate]
type = ADHeatRateConvection1Phase
block = 'pipe3'
T = T
T_wall = T_wall
Hw = Hw
P_hf = P_hf
execute_on = 'INITIAL TIMESTEP_END'
[]
[motor_torque]
type = RealComponentParameterValuePostprocessor
component = motor
parameter = torque
execute_on = 'INITIAL TIMESTEP_END'
[]
[motor_power]
type = FunctionValuePostprocessor
function = motor_power_fn
execute_on = 'INITIAL TIMESTEP_END'
indirect_dependencies = 'motor_torque shaft:omega'
[]
[generator_torque]
type = ShaftConnectedComponentPostprocessor
quantity = torque
shaft_connected_component_uo = generator:shaftconnected_uo
execute_on = 'INITIAL TIMESTEP_END'
[]
[generator_power]
type = FunctionValuePostprocessor
function = generator_power_fn
execute_on = 'INITIAL TIMESTEP_END'
indirect_dependencies = 'generator_torque shaft:omega'
[]
[shaft_speed]
type = ScalarVariable
variable = 'shaft:omega'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_in_comp]
type = PointValue
variable = p
point = '${x2_minus} 0 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_out_comp]
type = PointValue
variable = p
point = '${x2_plus} 0 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_ratio_comp]
type = ParsedPostprocessor
pp_names = 'p_in_comp p_out_comp'
expression = 'p_out_comp / p_in_comp'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_in_turb]
type = PointValue
variable = p
point = '${x5_minus} 0 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_out_turb]
type = PointValue
variable = p
point = '${x5_plus} 0 0'
execute_on = 'INITIAL TIMESTEP_END'
[]
[p_ratio_turb]
type = ParsedPostprocessor
pp_names = 'p_in_turb p_out_turb'
expression = 'p_in_turb / p_out_turb'
execute_on = 'INITIAL TIMESTEP_END'
[]
[mfr_comp]
type = ADFlowJunctionFlux1Phase
boundary = pipe1:out
connection_index = 0
equation = mass
junction = compressor
[]
[mfr_turb]
type = ADFlowJunctionFlux1Phase
boundary = pipe4:out
connection_index = 0
equation = mass
junction = turbine
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = 'bdf2'
end_time = ${t3}
dt = 0.1
abort_on_solve_fail = true
solve_type = NEWTON
nl_rel_tol = 1e-50
nl_abs_tol = 1e-11
nl_max_its = 15
l_tol = 1e-4
l_max_its = 10
[]
[Outputs]
[csv]
type = CSV
file_base = 'open_brayton_cycle'
execute_vector_postprocessors_on = 'INITIAL'
[]
[console]
type = Console
show = 'shaft_speed p_ratio_comp p_ratio_turb compressor:pressure_ratio turbine:pressure_ratio'
[]
[]
[Functions]
# compressor pressure ratio
[rp_comp1]
type = PiecewiseLinear
data_file = 'rp_comp1.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_comp2]
type = PiecewiseLinear
data_file = 'rp_comp2.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_comp3]
type = PiecewiseLinear
data_file = 'rp_comp3.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_comp4]
type = PiecewiseLinear
data_file = 'rp_comp4.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_comp5]
type = PiecewiseLinear
data_file = 'rp_comp5.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
# compressor efficiency
[eff_comp1]
type = ConstantFunction
value = ${eff_comp}
[]
[eff_comp2]
type = ConstantFunction
value = ${eff_comp}
[]
[eff_comp3]
type = ConstantFunction
value = ${eff_comp}
[]
[eff_comp4]
type = ConstantFunction
value = ${eff_comp}
[]
[eff_comp5]
type = ConstantFunction
value = ${eff_comp}
[]
# turbine pressure ratio
[rp_turb0]
type = ConstantFunction
value = 1
[]
[rp_turb1]
type = PiecewiseLinear
data_file = 'rp_turb1.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_turb2]
type = PiecewiseLinear
data_file = 'rp_turb2.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_turb3]
type = PiecewiseLinear
data_file = 'rp_turb3.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_turb4]
type = PiecewiseLinear
data_file = 'rp_turb4.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
[rp_turb5]
type = PiecewiseLinear
data_file = 'rp_turb5.csv'
x_index_in_file = 0
y_index_in_file = 1
format = columns
extrap = true
[]
# turbine efficiency
[eff_turb1]
type = ConstantFunction
value = ${eff_turb}
[]
[eff_turb2]
type = ConstantFunction
value = ${eff_turb}
[]
[eff_turb3]
type = ConstantFunction
value = ${eff_turb}
[]
[eff_turb4]
type = ConstantFunction
value = ${eff_turb}
[]
[eff_turb5]
type = ConstantFunction
value = ${eff_turb}
[]
[]
(modules/fluid_properties/test/tests/ics/rho_vapor_mixture_from_pressure_temperature/test.i)
# Tests the initial condition for mixture density from pressure and temperature.
# This test uses the general vapor mixture fluid properties with steam, air,
# and helium with mass fractions 0.5, 0.3, and 0.2, respectively. The individual
# specific volumes (in m^3/kg) at p = 100 kPa, T = 500 K are:
# steam: 2.298113001
# air: 1.43525
# helium: 10.3855
# For the general vapor mixture, the mixture specific volume is computed as
# v = \sum\limits_i x_i v_i ,
# where x_i is the mass fraction of component i, and v_i is the specific volume
# of component i. Therefore, the correct value for specific volume of the mixture is
# v = 3.65673150050 m^3/kg
# and thus density is
# rho = 0.27346825980066236 kg/m^3
[Mesh]
type = GeneratedMesh
dim = 1
nx = 1
allow_renumbering = false
[]
[FluidProperties]
[fp_steam]
type = StiffenedGasFluidProperties
gamma = 1.43
cv = 1040.0
q = 2.03e6
p_inf = 0.0
q_prime = -2.3e4
k = 0.026
mu = 134.4e-7
M = 0.01801488
rho_c = 322.0
[]
[fp_air]
type = IdealGasFluidProperties
gamma = 1.4
molar_mass = 28.965197004e-3
[]
[fp_helium]
type = IdealGasFluidProperties
gamma = 1.66
molar_mass = 4.002917432959e-3
[]
[fp_vapor_mixture]
type = IdealRealGasMixtureFluidProperties
fp_primary = fp_steam
fp_secondary = 'fp_air fp_helium'
[]
[]
[AuxVariables]
[rho]
[]
[p]
[]
[T]
[]
[x_air]
[]
[x_helium]
[]
[]
[ICs]
[rho_ic]
type = RhoVaporMixtureFromPressureTemperatureIC
variable = rho
p = p
T = T
x_secondary_vapors = 'x_air x_helium'
fp_vapor_mixture = fp_vapor_mixture
[]
[p_ic]
type = ConstantIC
variable = p
value = 100e3
[]
[T_ic]
type = ConstantIC
variable = T
value = 500
[]
[x_air_ic]
type = ConstantIC
variable = x_air
value = 0.3
[]
[x_helium_ic]
type = ConstantIC
variable = x_helium
value = 0.2
[]
[]
[Executioner]
type = Steady
[]
[Postprocessors]
[rho_test]
type = ElementalVariableValue
elementid = 0
variable = rho
execute_on = 'INITIAL TIMESTEP_END'
[]
[]
[Outputs]
csv = true
execute_on = 'INITIAL'
[]
[Problem]
solve = false
[]
(modules/fluid_properties/test/tests/functions/saturation_temperature_function/saturation_temperature_function.i)
# TestTwoPhaseFluidProperties has the following saturation temperature function:
# T_sat(p) = 2 p
# Thus for p = 5, T_sat should be 10.
[Mesh]
type = GeneratedMesh
dim = 1
nx = 1
[]
[FluidProperties]
[./fp_liquid]
type = IdealGasFluidProperties
[../]
[./fp_vapor]
type = IdealGasFluidProperties
[../]
[./fp_2phase]
type = TestTwoPhaseFluidProperties
fp_liquid = fp_liquid
fp_vapor = fp_vapor
[../]
[]
[Functions]
[./p]
type = ConstantFunction
value = 5
[../]
[./T_sat]
type = SaturationTemperatureFunction
p = p
fp_2phase = fp_2phase
[../]
[]
[Postprocessors]
[./T_sat_pp]
type = FunctionValuePostprocessor
function = T_sat
execute_on = 'INITIAL'
[../]
[]
[Problem]
solve = false
[]
[Executioner]
type = Steady
[]
[Outputs]
csv = true
[]
(modules/navier_stokes/test/include/userobjects/TestConservedVarFluidProperties.h)
// This file is part of the MOOSE framework
// https://mooseframework.inl.gov
//
// All rights reserved, see COPYRIGHT for full restrictions
// https://github.com/idaholab/moose/blob/master/COPYRIGHT
//
// Licensed under LGPL 2.1, please see LICENSE for details
// https://www.gnu.org/licenses/lgpl-2.1.html
#pragma once
#include "IdealGasFluidProperties.h"
#pragma GCC diagnostic push
#pragma GCC diagnostic ignored "-Woverloaded-virtual"
class TestConservedVarFluidProperties : public IdealGasFluidProperties
{
public:
static InputParameters validParams();
TestConservedVarFluidProperties(const InputParameters & parameters);
ADReal p_from_v_e(const ADReal & v, const ADReal & /*e*/) const override;
ADReal T_from_v_e(const ADReal & /*v*/, const ADReal & /*e*/) const override;
};
#pragma GCC diagnostic pop