- from_postprocessorThe name of the Postprocessor in the Master to transfer the value from.
C++ Type:PostprocessorName
Unit:(no unit assumed)
Controllable:No
Description:The name of the Postprocessor in the Master to transfer the value from.
- to_postprocessorThe name of the Postprocessor in the MultiApp to transfer the value to. This should most likely be a Reporter Postprocessor.
C++ Type:PostprocessorName
Unit:(no unit assumed)
Controllable:No
Description:The name of the Postprocessor in the MultiApp to transfer the value to. This should most likely be a Reporter Postprocessor.
MultiAppPostprocessorTransfer
Transfers postprocessor data between the master application and sub-application(s).
Siblings transfer behavior
This transfer supports sending data from a multiapp to a multiapp. There are two supported configurations:
only one subapp in the source multiapp, the source postprocessor value is sent to all target multiapps.
the same number of subapps in the source and target multiapp, the source postprocessor is matched to a target postprocessor based on a matching subapp index.
Example Input File Syntax
The MultiAppPostprocessorTransfer allows for a Postprocessor value to be transfer between the parent application and sub-application(s). For example, the input file snippet below sets up a transfer of a Postprocessor value from the parent application to a Postprocessor on each of the sub-applications.
[Transfers<<<{"href": "../../syntax/Transfers/index.html"}>>>]
[pp_transfer]
type = MultiAppPostprocessorTransfer<<<{"description": "Transfers postprocessor data between the master application and sub-application(s).", "href": "MultiAppPostprocessorTransfer.html"}>>>
to_multi_app<<<{"description": "The name of the MultiApp to transfer the data to"}>>> = pp_sub
from_postprocessor<<<{"description": "The name of the Postprocessor in the Master to transfer the value from."}>>> = average
to_postprocessor<<<{"description": "The name of the Postprocessor in the MultiApp to transfer the value to. This should most likely be a Reporter Postprocessor."}>>> = from_parent
[]
[]Input Parameters
- check_multiapp_execute_onTrueWhen false the check between the multiapp and transfer execute on flags is not performed.
Default:True
C++ Type:bool
Controllable:No
Description:When false the check between the multiapp and transfer execute on flags is not performed.
- displaced_source_meshFalseWhether or not to use the displaced mesh for the source mesh.
Default:False
C++ Type:bool
Controllable:No
Description:Whether or not to use the displaced mesh for the source mesh.
- displaced_target_meshFalseWhether or not to use the displaced mesh for the target mesh.
Default:False
C++ Type:bool
Controllable:No
Description:Whether or not to use the displaced mesh for the target mesh.
- execute_onSAME_AS_MULTIAPPThe list of flag(s) indicating when this object should be executed. For a description of each flag, see https://mooseframework.inl.gov/source/interfaces/SetupInterface.html.
Default:SAME_AS_MULTIAPP
C++ Type:ExecFlagEnum
Options:XFEM_MARK, FORWARD, ADJOINT, HOMOGENEOUS_FORWARD, ADJOINT_TIMESTEP_BEGIN, ADJOINT_TIMESTEP_END, NONE, INITIAL, LINEAR, LINEAR_CONVERGENCE, NONLINEAR, NONLINEAR_CONVERGENCE, POSTCHECK, TIMESTEP_END, TIMESTEP_BEGIN, MULTIAPP_FIXED_POINT_END, MULTIAPP_FIXED_POINT_BEGIN, MULTIAPP_FIXED_POINT_CONVERGENCE, FINAL, CUSTOM, SAME_AS_MULTIAPP, POST_ADAPTIVITY
Controllable:No
Description:The list of flag(s) indicating when this object should be executed. For a description of each flag, see https://mooseframework.inl.gov/source/interfaces/SetupInterface.html.
- from_multi_appThe name of the MultiApp to receive data from
C++ Type:MultiAppName
Controllable:No
Description:The name of the MultiApp to receive data from
- reduction_typeThe type of reduction to perform to reduce postprocessor values from multiple SubApps to a single value
C++ Type:MooseEnum
Options:average, sum, maximum, minimum
Controllable:No
Description:The type of reduction to perform to reduce postprocessor values from multiple SubApps to a single value
- to_multi_appThe name of the MultiApp to transfer the data to
C++ Type:MultiAppName
Controllable:No
Description:The name of the MultiApp to transfer the data to
Optional Parameters
- _called_legacy_paramsTrue
Default:True
C++ Type:bool
Controllable:No
- 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.
- skip_coordinate_collapsingTrueWhether to skip coordinate collapsing (translation and rotation are still performed, only XYZ, RZ etc collapsing is skipped) when performing mapping and inverse mapping coordinate transformation operations. This parameter should only be set by users who really know what they're doing.
Default:True
C++ Type:bool
Controllable:No
Description:Whether to skip coordinate collapsing (translation and rotation are still performed, only XYZ, RZ etc collapsing is skipped) when performing mapping and inverse mapping coordinate transformation operations. This parameter should only be set by users who really know what they're doing.
- use_displaced_meshFalseWhether or not this object should use the displaced mesh for computation. Note that in the case this is true but no displacements are provided in the Mesh block the undisplaced mesh will still be used.
Default:False
C++ Type:bool
Controllable:No
Description:Whether or not this object should use the displaced mesh for computation. Note that in the case this is true but no displacements are provided in the Mesh block the undisplaced mesh will still be used.
Advanced Parameters
Input Files
- (test/tests/multiapps/secant_postprocessor/steady_main.i)
- (test/tests/transfers/transfer_once_per_fixed_point/parent.i)
- (test/tests/multiapps/secant_postprocessor/transient_main.i)
- (modules/thermal_hydraulics/test/tests/misc/coupling_mD_flow/parent_non_overlapping.i)
- (test/tests/multiapps/steffensen_postprocessor/steady_main.i)
- (test/tests/transfers/multiapp_postprocessor_transfer/parent_from_multiapp.i)
- (test/tests/multiapps/steffensen_postprocessor/transient_main.i)
- (test/tests/multiapps/initial_transfer/parent.i)
- (modules/combined/test/tests/subchannel_thm_coupling/THM_SCM_coupling_pump.i)
- (test/tests/multiapps/picard_multilevel/multilevel_dt_rejection/parent.i)
- (test/tests/transfers/multiapp_postprocessor_transfer/parent.i)
- (modules/combined/test/tests/subchannel_thm_coupling/THM_SCM_coupling.i)
- (test/tests/transfers/multiapp_postprocessor_transfer/between_multiapp/main.i)
- (test/tests/multiapps/picard_postprocessor/transient_main.i)
- (test/tests/transfers/multiapp_postprocessor_transfer/from_one_sub_parent.i)
- (test/tests/multiapps/picard_multilevel/multilevel_dt_rejection/picard_sub.i)
- (test/tests/multiapps/picard_postprocessor/steady_main.i)
- (modules/thermal_hydraulics/test/tests/components/hs_boundary_external_app_heat_flux/main.i)
(test/tests/transfers/multiapp_postprocessor_transfer/parent.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 10
ny = 10
[]
[Variables]
[u]
[]
[]
[Kernels]
[diff]
type = CoefDiffusion
variable = u
coef = 0.01
[]
[td]
type = TimeDerivative
variable = u
[]
[]
[BCs]
[left]
type = DirichletBC
variable = u
boundary = left
value = 0
[]
[right]
type = DirichletBC
variable = u
boundary = right
value = 1
[]
[]
[Postprocessors]
[average]
type = ElementAverageValue
variable = u
execute_on = 'TRANSFER'
[]
[]
[Executioner]
type = Transient
num_steps = 5
solve_type = 'PJFNK'
petsc_options_iname = '-pc_type -pc_hypre_type'
petsc_options_value = 'hypre boomeramg'
nl_rel_tol = 1e-12
[]
[Outputs]
exodus = true
[]
[MultiApps]
[pp_sub]
app_type = MooseTestApp
positions = '0.5 0.5 0 0.7 0.7 0'
execute_on = timestep_end
type = TransientMultiApp
input_files = sub.i
[]
[]
[Transfers]
[pp_transfer]
type = MultiAppPostprocessorTransfer
to_multi_app = pp_sub
from_postprocessor = average
to_postprocessor = from_parent
[]
[]
(test/tests/multiapps/secant_postprocessor/steady_main.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 5
ny = 5
parallel_type = replicated
uniform_refine = 1
[]
[Variables]
[u]
[]
[]
[Kernels]
[diff]
type = Diffusion
variable = u
[]
[source]
type = BodyForce
variable = u
value = 1
[]
[]
[BCs]
[left]
type = PostprocessorDirichletBC
variable = u
boundary = left
postprocessor = 'from_sub'
[]
[]
[Postprocessors]
[from_sub]
type = Receiver
default = 0
[]
[to_sub]
type = SideAverageValue
variable = u
boundary = right
[]
[average]
type = ElementAverageValue
variable = u
[]
[]
[Executioner]
type = Steady
# Solve parameters
solve_type = PJFNK
petsc_options_iname = '-pc_type -pc_hypre_type'
petsc_options_value = 'hypre boomeramg'
nl_abs_tol = 1e-14
# App coupling parameters
fixed_point_algorithm = 'secant'
fixed_point_max_its = 100
transformed_postprocessors = 'from_sub'
[]
[Outputs]
csv = true
exodus = false
[]
[MultiApps]
[sub]
type = FullSolveMultiApp
app_type = MooseTestApp
positions = '0 0 0'
input_files = steady_sub.i
clone_parent_mesh = true
execute_on = 'timestep_begin'
# we keep the full postprocessor output history of the subapp
keep_full_output_history = true
transformed_postprocessors = 'from_main'
[]
[]
[Transfers]
[left_from_sub]
type = MultiAppPostprocessorTransfer
from_multi_app = sub
from_postprocessor = 'to_main'
to_postprocessor = 'from_sub'
reduction_type = 'average'
[]
[right_to_sub]
type = MultiAppPostprocessorTransfer
to_multi_app = sub
from_postprocessor = 'to_sub'
to_postprocessor = 'from_main'
[]
[]
(test/tests/transfers/transfer_once_per_fixed_point/parent.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 10
ny = 10
[]
[Problem]
type = FEProblem
solve = false
verbose_multiapps = true
[]
[Executioner]
type = Transient
num_steps = 4
solve_type = 'PJFNK'
petsc_options_iname = '-pc_type -pc_hypre_type'
petsc_options_value = 'hypre boomeramg'
fixed_point_min_its = 4
fixed_point_max_its = 20
verbose = true
[]
[MultiApps]
# This app is used to trigger fixed point iteration when sub is executed on MULTIAPP_FIXED_POINT_BEGIN/END
[side_app]
type = TransientMultiApp
input_files = sub.i
cli_args = "MultiApps/active='';Outputs/active=''"
execute_on = 'INITIAL TIMESTEP_END'
# The input was originally created with effectively no restore
# see the changes made for #5554 then reverted in #28115
no_restore = true
[]
# This app is used to test the fixed point begin/end execute_on for transfers and multiapps
[sub]
type = TransientMultiApp
input_files = sub.i
execute_on = 'INITIAL TIMESTEP_END'
# The input was originally created with effectively no restore
# see the changes made for #5554 then reverted in #28115
no_restore = true
[]
[]
[Transfers]
[to_sub]
type = MultiAppPostprocessorTransfer
from_postprocessor = num_fixed_point_total
to_postprocessor = parent_fp_its
to_multi_app = sub
check_multiapp_execute_on = false
execute_on = 'MULTIAPP_FIXED_POINT_BEGIN'
[]
[from_sub]
type = MultiAppPostprocessorTransfer
from_postprocessor = num_fixed_point_its
to_postprocessor = subapp_fp_its
from_multi_app = sub
check_multiapp_execute_on = false
execute_on = 'MULTIAPP_FIXED_POINT_BEGIN'
reduction_type = 'sum'
[]
[]
[Postprocessors]
[num_fixed_point_total]
type = TestPostprocessor
test_type = 'grow'
execute_on = 'INITIAL TIMESTEP_END'
[]
[num_fixed_point_begin]
type = TestPostprocessor
test_type = 'grow'
execute_on = 'MULTIAPP_FIXED_POINT_BEGIN'
[]
[num_fixed_point_end]
type = TestPostprocessor
test_type = 'grow'
execute_on = 'MULTIAPP_FIXED_POINT_END'
[]
[subapp_fp_its]
type = Receiver
[]
[]
[Outputs]
[fp_begin]
type = CSV
execute_on = 'MULTIAPP_FIXED_POINT_BEGIN'
[]
[fp_end]
type = CSV
file_base = 'fp_end'
execute_on = 'MULTIAPP_FIXED_POINT_END'
[]
[]
(test/tests/multiapps/secant_postprocessor/transient_main.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 5
ny = 5
parallel_type = replicated
uniform_refine = 1
[]
[Variables]
[u]
[]
[]
[Kernels]
[diff]
type = Diffusion
variable = u
[]
[time]
type = TimeDerivative
variable = u
[]
[source]
type = BodyForce
variable = u
value = 1
[]
[]
[BCs]
[left]
type = PostprocessorDirichletBC
variable = u
boundary = left
postprocessor = 'from_sub'
[]
[]
[Postprocessors]
[coupling_its]
type = NumFixedPointIterations
execute_on = 'initial timestep_end'
[]
[from_sub]
type = Receiver
default = 0
[]
[to_sub]
type = SideAverageValue
variable = u
boundary = right
[]
[average]
type = ElementAverageValue
variable = u
[]
[]
[Executioner]
type = Transient
num_steps = 10
dt = 0.1
solve_type = PJFNK
petsc_options_iname = '-pc_type -pc_hypre_type'
petsc_options_value = 'hypre boomeramg'
nl_abs_tol = 1e-14
# App coupling parameters
fixed_point_algorithm = 'secant'
fixed_point_max_its = 30
transformed_postprocessors = 'from_sub'
[]
[Outputs]
csv = true
exodus = false
[]
[MultiApps]
[sub]
type = TransientMultiApp
app_type = MooseTestApp
positions = '0 0 0'
input_files = 'transient_sub.i'
clone_parent_mesh = true
execute_on = 'timestep_begin'
# The input was originally created with effectively no restore
# see the changes made for #5554 then reverted in #28115
no_restore = true
[]
[]
[Transfers]
[left_from_sub]
type = MultiAppPostprocessorTransfer
from_multi_app = sub
from_postprocessor = 'to_main'
to_postprocessor = 'from_sub'
reduction_type = 'average'
[]
[right_to_sub]
type = MultiAppPostprocessorTransfer
to_multi_app = sub
from_postprocessor = 'to_sub'
to_postprocessor = 'from_main'
[]
[]
(modules/thermal_hydraulics/test/tests/misc/coupling_mD_flow/parent_non_overlapping.i)
# inlet temperature
T_in = 523.0
mdot = 10
pout = 7e6
[Mesh]
type = GeneratedMesh
dim = 3
xmin = -1.5
xmax = 1.5
ymin = -1.5
ymax = 1.5
zmin = 0
zmax = 10
nx = 3
ny = 3
nz = 10
[]
[Problem]
kernel_coverage_check = false
[]
[Variables]
[u]
[]
[]
[Postprocessors]
[core_outlet_pressure]
type = Receiver
default = ${pout}
[]
[core_inlet_mdot]
type = Receiver
default = ${mdot}
[]
[core_inlet_temperature]
type = Receiver
default = ${T_in}
[]
[core_inlet_pressure]
type = FunctionValuePostprocessor
function = compute_inlet_pressure_fn
execute_on = 'INITIAL LINEAR TIMESTEP_END'
[]
[core_outlet_mdot]
type = ScalePostprocessor
value = core_inlet_mdot
execute_on = 'INITIAL LINEAR TIMESTEP_END'
[]
[bypass_mdot]
type = Receiver
[]
[inlet_mdot]
type = Receiver
[]
[outlet_mdot]
type = Receiver
[]
[core_outlet_temperature]
type = FunctionValuePostprocessor
function = compute_outlet_temperature_fn
execute_on = 'INITIAL LINEAR TIMESTEP_END'
[]
[core_pressure_drop]
type = DifferencePostprocessor
value1 = core_inlet_pressure
value2 = core_outlet_pressure
[]
[]
[Functions]
[compute_outlet_temperature_fn]
type = ParsedFunction
symbol_values = 'core_inlet_mdot core_inlet_temperature 1000'
symbol_names = 'mdot Tin Q'
expression = 'Tin + Q / mdot'
[]
[compute_inlet_pressure_fn]
type = ParsedFunction
symbol_values = 'core_inlet_mdot core_outlet_pressure 5000'
symbol_names = 'mdot pout C'
expression = 'pout + C * mdot'
[]
[]
[MultiApps]
[thm]
type = TransientMultiApp
input_files = thm_non_overlapping.i
sub_cycling = true
max_procs_per_app = 1
print_sub_cycles = false
[]
[]
[Transfers]
#### thm Transfers ####
## transfers from thm
[core_inlet_mdot]
type = MultiAppPostprocessorTransfer
from_postprocessor = core_inlet_mdot
to_postprocessor = core_inlet_mdot
reduction_type = maximum
from_multi_app = thm
[]
[core_inlet_temperature]
type = MultiAppPostprocessorTransfer
to_postprocessor = core_inlet_temperature
from_postprocessor = core_inlet_temperature
reduction_type = maximum
from_multi_app = thm
[]
[core_outlet_pressure]
type = MultiAppPostprocessorTransfer
to_postprocessor = core_outlet_pressure
from_postprocessor = core_outlet_pressure
reduction_type = maximum
from_multi_app = thm
[]
[bypass_mdot]
type = MultiAppPostprocessorTransfer
to_postprocessor = bypass_mdot
from_postprocessor = bypass_mdot
reduction_type = maximum
from_multi_app = thm
[]
[inlet_mdot]
type = MultiAppPostprocessorTransfer
to_postprocessor = inlet_mdot
from_postprocessor = inlet_mdot
reduction_type = maximum
from_multi_app = thm
[]
[outlet_mdot]
type = MultiAppPostprocessorTransfer
to_postprocessor = outlet_mdot
from_postprocessor = outlet_mdot
reduction_type = maximum
from_multi_app = thm
[]
## transfers to thm
[core_outlet_mdot]
type = MultiAppPostprocessorTransfer
from_postprocessor = core_outlet_mdot
to_postprocessor = core_outlet_mdot
to_multi_app = thm
[]
[core_outlet_temperature]
type = MultiAppPostprocessorTransfer
from_postprocessor = core_outlet_temperature
to_postprocessor = core_outlet_temperature
to_multi_app = thm
[]
[core_inlet_pressure]
type = MultiAppPostprocessorTransfer
from_postprocessor = core_inlet_pressure
to_postprocessor = core_inlet_pressure
to_multi_app = thm
[]
[]
[Executioner]
type = Transient
dt = 0.1
num_steps = 1
abort_on_solve_fail = true
[]
[Outputs]
exodus = true
[]
(test/tests/multiapps/steffensen_postprocessor/steady_main.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 5
ny = 5
parallel_type = replicated
uniform_refine = 1
[]
[Variables]
[u]
[]
[]
[Kernels]
[diff]
type = Diffusion
variable = u
[]
[source]
type = BodyForce
variable = u
value = 1
[]
[]
[BCs]
[left]
type = PostprocessorDirichletBC
variable = u
boundary = left
postprocessor = 'from_sub'
[]
[]
[Postprocessors]
[from_sub]
type = Receiver
default = 0
[]
[to_sub]
type = SideAverageValue
variable = u
boundary = right
[]
[average]
type = ElementAverageValue
variable = u
[]
[]
[Executioner]
type = Steady
# Solve parameters
solve_type = PJFNK
petsc_options_iname = '-pc_type -pc_hypre_type'
petsc_options_value = 'hypre boomeramg'
nl_abs_tol = 1e-14
# App coupling parameters
fixed_point_algorithm = 'steffensen'
fixed_point_max_its = 100
transformed_postprocessors = 'from_sub'
[]
[Outputs]
csv = true
exodus = false
[]
[MultiApps]
[sub]
type = FullSolveMultiApp
app_type = MooseTestApp
positions = '0 0 0'
input_files = steady_sub.i
clone_parent_mesh = true
execute_on = 'timestep_begin'
# we keep the full postprocessor output history of the subapp
keep_full_output_history = true
transformed_postprocessors = 'from_main'
[]
[]
[Transfers]
[left_from_sub]
type = MultiAppPostprocessorTransfer
from_multi_app = sub
from_postprocessor = 'to_main'
to_postprocessor = 'from_sub'
reduction_type = 'average'
[]
[right_to_sub]
type = MultiAppPostprocessorTransfer
to_multi_app = sub
from_postprocessor = 'to_sub'
to_postprocessor = 'from_main'
[]
[]
(test/tests/transfers/multiapp_postprocessor_transfer/parent_from_multiapp.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 10
ny = 10
[]
[Variables]
[./u]
[../]
[]
[AuxVariables]
[./from_sub]
[../]
[]
[Kernels]
[./diff]
type = Diffusion
variable = u
[../]
[]
[BCs]
[./left]
type = DirichletBC
variable = u
boundary = left
value = 0
[../]
[./right]
type = DirichletBC
variable = u
boundary = right
value = 1
[../]
[]
[Postprocessors]
[./sub_average]
type = Receiver
[../]
[./sub_sum]
type = Receiver
[../]
[./sub_maximum]
type = Receiver
[../]
[./sub_minimum]
type = Receiver
[../]
[]
[Executioner]
type = Transient
num_steps = 1
dt = 1
solve_type = 'PJFNK'
petsc_options_iname = '-pc_type -pc_hypre_type'
petsc_options_value = 'hypre boomeramg'
[]
[Outputs]
exodus = true
[]
[MultiApps]
[./sub]
positions = '0.2 0.2 0 0.7 0.7 0'
type = TransientMultiApp
app_type = MooseTestApp
input_files = 'sub0.i sub1.i'
[../]
[]
[Transfers]
[./pp_transfer_ave]
type = MultiAppPostprocessorTransfer
reduction_type = average
from_multi_app = sub
from_postprocessor = average
to_postprocessor = sub_average
[../]
[./pp_transfer_sum]
type = MultiAppPostprocessorTransfer
reduction_type = sum
from_multi_app = sub
from_postprocessor = average
to_postprocessor = sub_sum
[../]
[./pp_transfer_min]
type = MultiAppPostprocessorTransfer
reduction_type = minimum
from_multi_app = sub
from_postprocessor = average
to_postprocessor = sub_minimum
[../]
[./pp_transfer_max]
type = MultiAppPostprocessorTransfer
reduction_type = maximum
from_multi_app = sub
from_postprocessor = average
to_postprocessor = sub_maximum
[../]
[]
(test/tests/multiapps/steffensen_postprocessor/transient_main.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 5
ny = 5
parallel_type = replicated
uniform_refine = 1
[]
[Variables]
[u]
[]
[]
[Kernels]
[diff]
type = Diffusion
variable = u
[]
[time]
type = TimeDerivative
variable = u
[]
[source]
type = BodyForce
variable = u
value = 1
[]
[]
[BCs]
[left]
type = PostprocessorDirichletBC
variable = u
boundary = left
postprocessor = 'from_sub'
[]
[]
[Postprocessors]
[coupling_its]
type = NumFixedPointIterations
execute_on = 'initial timestep_end'
[]
[from_sub]
type = Receiver
default = 0
[]
[to_sub]
type = SideAverageValue
variable = u
boundary = right
[]
[average]
type = ElementAverageValue
variable = u
[]
[]
[Executioner]
type = Transient
num_steps = 10
dt = 0.1
solve_type = PJFNK
petsc_options_iname = '-pc_type -pc_hypre_type'
petsc_options_value = 'hypre boomeramg'
nl_abs_tol = 1e-14
# App coupling parameters
fixed_point_algorithm = 'steffensen'
fixed_point_max_its = 30
transformed_postprocessors = 'from_sub'
[]
[Outputs]
csv = true
exodus = false
[]
[MultiApps]
[sub]
type = TransientMultiApp
app_type = MooseTestApp
positions = '0 0 0'
input_files = 'transient_sub.i'
clone_parent_mesh = true
execute_on = 'timestep_begin'
# The input was originally created with effectively no restore
# see the changes made for #5554 then reverted in #28115
no_restore = true
[]
[]
[Transfers]
[left_from_sub]
type = MultiAppPostprocessorTransfer
from_multi_app = sub
from_postprocessor = 'to_main'
to_postprocessor = 'from_sub'
reduction_type = 'average'
[]
[right_to_sub]
type = MultiAppPostprocessorTransfer
to_multi_app = sub
from_postprocessor = 'to_sub'
to_postprocessor = 'from_main'
[]
[]
(test/tests/multiapps/initial_transfer/parent.i)
[Mesh]
type = GeneratedMesh
dim = 2
xmin = 0
xmax = 1
ymin = 0
ymax = 1
nx = 2
ny = 2
[]
[Problem]
kernel_coverage_check = false
[]
[Variables][dummy][][]
[Functions]
[func]
type = ConstantFunction
value = 1
[]
[]
[Postprocessors]
[c]
type = FunctionValuePostprocessor
function = func
execute_on = initial
# this will force this postprocessor to be evaluated before transfer on initial
force_preic = true
[]
[]
[Executioner]
type = Steady
[]
[MultiApps]
[sub]
type = FullSolveMultiApp
input_files = sub.i
execute_on = initial
[../]
[]
[Transfers]
[to_sub]
type = MultiAppPostprocessorTransfer
to_multi_app = sub
from_postprocessor = c
to_postprocessor = receiver
[]
[]
(modules/combined/test/tests/subchannel_thm_coupling/THM_SCM_coupling_pump.i)
# THM file based on https://mooseframework.inl.gov/modules/thermal_hydraulics/tutorials/single_phase_flow/step05.html
# Used to loosely couple THM with SCM
# This is a simple closed loop with a pump providing pressure head, core, pressurizer and HX.
# THM sends massflux and temperature at the inlet of the core, and pressure at the outlet of the core
# to subchannel. Subchannel returns total pressure drop of the assembly and total power to THM and THM calculates an
# average friction factor for the core region.
T_in = 583.0 # K
press = 2e5 # Pa
SC_core = 0.0004980799633447909 #m2
# core parameters
core_length = 1. # m
core_n_elems = 1
A_core = 0.005 #dummy
# pipe parameters
pipe_dia = '${units 10. cm -> m}'
A_pipe = '${fparse 0.25 * pi * pipe_dia^2}'
# heat exchanger parameters
hx_dia_inner = '${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 = sodium_eos
[]
[Functions]
[q_wall_fn]
type = ParsedFunction
symbol_names = 'core_power length'
symbol_values = 'core_power ${core_length}'
expression = 'core_power/length'
[]
[]
[FluidProperties]
[water]
type = StiffenedGasFluidProperties
gamma = 2.35
cv = 1816.0
q = -1.167e6
p_inf = 1.0e9
q_prime = 0
[]
[sodium_eos]
type = StiffenedGasFluidProperties
gamma = 1.24
cv = 1052.8
q = -2.6292e+05
p_inf = 1.1564e+08
q_prime = 0
mu = 3.222e-04
k = 73.82
[]
[]
[Closures]
[thm_closures]
type = Closures1PhaseTHM
[]
[none_closures]
type = Closures1PhaseNone
[]
[]
[Materials]
[f_mat]
type = ADParsedMaterial
property_name = f_D
postprocessor_names = 'core_f'
expression = 'core_f'
block = 'core_chan'
[]
[]
[HeatStructureMaterials]
[steel]
type = SolidMaterialProperties
rho = 8050
k = 45
cp = 466
[]
[]
[Components]
[up_pipe_1]
type = FlowChannel1Phase
position = '0 0 -0.5'
orientation = '0 0 1'
length = 0.5
n_elems = 15
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct1]
type = JunctionParallelChannels1Phase
position = '0 0 0'
connections = 'up_pipe_1:out core_chan:in'
volume = 1e-5
[]
[core_chan]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '0 0 1'
length = ${core_length}
n_elems = ${core_n_elems}
A = ${A_core}
closures = none_closures
[]
[core_ht]
type = HeatTransferFromHeatFlux1Phase
flow_channel = core_chan
q_wall = q_wall_fn
P_hf = 1
[]
[jct2]
type = JunctionParallelChannels1Phase
position = '0 0 1'
connections = 'core_chan:out up_pipe_2:in'
volume = 1e-5
[]
[up_pipe_2]
type = FlowChannel1Phase
position = '0 0 1'
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 1.5'
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 1.5'
orientation = '1 0 0'
length = 0.5
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct4]
type = VolumeJunction1Phase
position = '0.5 0 1.5'
volume = 1e-5
connections = 'top_pipe_1:out top_pipe_2:in press_pipe:in'
[]
[press_pipe]
type = FlowChannel1Phase
position = '0.5 0 1.5'
orientation = '0 1 0'
length = 0.2
n_elems = 5
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[pressurizer]
type = InletStagnationPressureTemperature1Phase
p0 = ${press}
T0 = 580
input = press_pipe:out
[]
[jct5]
type = JunctionOneToOne1Phase
connections = 'top_pipe_2:out down_pipe_1:in'
[]
[down_pipe_1]
type = FlowChannel1Phase
position = '1 0 1.5'
orientation = '0 0 -1'
length = 0.25
A = ${A_pipe}
n_elems = 5
[]
[jct6]
type = JunctionParallelChannels1Phase
position = '1 0 1.25'
connections = 'down_pipe_1:out hx/pri:in'
volume = 1e-5
[]
[hx]
[pri]
type = FlowChannel1Phase
position = '1 0 1.25'
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 1.25'
orientation = '0 0 -1'
length = ${hx_length}
n_elems = ${hx_n_elems}
widths = '${hx_wall_thickness}'
n_part_elems = '3'
materials = 'steel'
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 -0.25'
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 -0.5'
orientation = '-1 0 0'
length = 0.5
n_elems = 5
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[pump]
type = Pump1Phase
position = '0.5 0 -0.5'
connections = 'bottom_1:out bottom_2:in'
volume = 1e-4
A_ref = ${A_pipe}
head = 3.56
[]
[bottom_2]
type = FlowChannel1Phase
position = '0.5 0 -0.5'
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 = ${m_dot_sec_in}
T = 300
[]
[outlet_sec]
type = Outlet1Phase
input = 'hx/sec:out'
p = 1e5
[]
[]
[Postprocessors]
[power_to_coolant]
type = ADHeatRateDirectFlowChannel
q_wall_prop = q_wall
block = core_chan
P_hf = 1
[]
[core_T_out]
type = SideAverageValue
boundary = core_chan:out
variable = T
[]
[T_out]
type = SideAverageValue
boundary = bottom_1:out
variable = T
[]
[core_p_in]
type = SideAverageValue
boundary = up_pipe_1:out
variable = p
[]
[core_p_out]
type = SideAverageValue
boundary = up_pipe_2:in
variable = p
[]
[core_delta_p]
type = ParsedPostprocessor
pp_names = 'core_p_in core_p_out'
function = '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
[]
############## Friction Factor Calculation #############
[av_rhouA]
type = ElementAverageValue
variable = 'rhouA'
block = 'core_chan'
[]
[av_rho]
type = ElementAverageValue
variable = 'rho'
block = 'core_chan'
[]
[Kloss]
type = ParsedPostprocessor
pp_names = 'core_delta_p_tgt av_rhouA av_rho'
function = '2.0 * core_delta_p_tgt * av_rho * ${A_core} * ${A_core} / (av_rhouA * av_rhouA)'
[]
[Dh]
type = ADElementAverageMaterialProperty
mat_prop = D_h
block = core_chan
[]
[core_f]
type = ParsedPostprocessor
pp_names = 'Kloss Dh'
function = 'Kloss * Dh / ${core_length}'
[]
### INFO to send to SC
[outlet_pressure]
type = SideAverageValue
boundary = up_pipe_2:in
variable = p
[]
[inlet_mass_flow_rate]
type = ADFlowJunctionFlux1Phase
boundary = up_pipe_1:out
connection_index = 0
equation = mass
junction = jct1
[]
[inlet_temperature]
type = SideAverageValue
boundary = up_pipe_1:out
variable = T
[]
[inlet_mass_flux]
type = ParsedPostprocessor
pp_names = 'inlet_mass_flow_rate'
function = 'abs(inlet_mass_flow_rate/${SC_core})'
[]
#####
##### Info received from subchannel
[core_delta_p_tgt]
type = Receiver
default = 100
[]
[core_power]
type = Receiver
default = 100
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
start_time = 0
[TimeStepper]
type = IterationAdaptiveDT
dt = 2
[]
dtmax = 50
end_time = 10
line_search = basic
solve_type = NEWTON
petsc_options_iname = '-pc_type'
petsc_options_value = 'lu'
nl_rel_tol = 1e-7
nl_abs_tol = 1e-7
nl_max_its = 25
fixed_point_min_its = 1
fixed_point_max_its = 5
accept_on_max_fixed_point_iteration = true
auto_advance = true
relaxation_factor = 0.5
[]
[Outputs]
csv = true
[console]
type = Console
max_rows = 1
outlier_variable_norms = false
[]
print_linear_residuals = false
[]
################################################################################
# A multiapp that couples THM to subchannel
################################################################################
[MultiApps]
# active = ''
[subchannel]
type = FullSolveMultiApp
input_files = 'subchannel.i'
execute_on = 'timestep_end'
positions = '0 0 0'
max_procs_per_app = 1
output_in_position = true
bounding_box_padding = '0 0 0.1'
[]
[]
[Transfers]
# active = ''
[pressure_drop_transfer] # Get pressure drop to THM from subchannel
type = MultiAppPostprocessorTransfer
from_multi_app = subchannel
from_postprocessor = total_pressure_drop_SC
to_postprocessor = core_delta_p_tgt
reduction_type = average
execute_on = 'timestep_end'
[]
[power_transfer] # Get Total power to THM from subchannel
type = MultiAppPostprocessorTransfer
from_multi_app = subchannel
from_postprocessor = Total_power
to_postprocessor = core_power
reduction_type = average
execute_on = 'timestep_end'
[]
[mass_flux_tranfer] # Send mass_flux at the inlet of THM core to subchannel
type = MultiAppPostprocessorTransfer
to_multi_app = subchannel
from_postprocessor = inlet_mass_flux
to_postprocessor = report_mass_flux_inlet
execute_on = 'timestep_end'
[]
[outlet_pressure_tranfer] # Send pressure at the outlet of THM core to subchannel
type = MultiAppPostprocessorTransfer
to_multi_app = subchannel
from_postprocessor = outlet_pressure
to_postprocessor = report_pressure_outlet
execute_on = 'timestep_end'
[]
[inlet_temperature_transfer]
type = MultiAppPostprocessorTransfer
to_multi_app = subchannel
from_postprocessor = inlet_temperature
to_postprocessor = report_temperature_inlet
execute_on = 'timestep_end'
[]
[]
(test/tests/multiapps/picard_multilevel/multilevel_dt_rejection/parent.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 10
ny = 10
parallel_type = replicated
[]
[Variables]
[u]
[]
[]
[AuxVariables]
[v]
[]
[]
[AuxKernels]
[set_v]
type = FunctionAux
variable = v
function = 't'
[]
[]
[Kernels]
[diff]
type = CoefDiffusion
variable = u
coef = 0.1
[]
[coupled_force]
type = CoupledForce
variable = u
v = v
[]
[time]
type = TimeDerivative
variable = u
[]
[]
[BCs]
[left]
type = DirichletBC
variable = u
boundary = left
value = 0
[]
[right]
type = DirichletBC
variable = u
boundary = right
value = 1
[]
[]
[Executioner]
type = Transient
solve_type = PJFNK
num_steps = 2
petsc_options_iname = '-pc_type -pc_hypre_type'
petsc_options_value = 'hypre boomeramg'
fixed_point_max_its = 1
auto_advance = false
[]
[MultiApps]
[sub1]
type = TransientMultiApp
positions = '0 0 0'
input_files = picard_sub.i
execute_on = 'timestep_end'
[]
[]
[Transfers]
[u_to_v2]
type = MultiAppGeneralFieldNearestLocationTransfer
to_multi_app = sub1
source_variable = u
variable = v2
[]
[time_to_sub]
type = MultiAppPostprocessorTransfer
from_postprocessor = time
to_postprocessor = parent_time
to_multi_app = sub1
[]
[dt_to_sub]
type = MultiAppPostprocessorTransfer
from_postprocessor = dt
to_postprocessor = parent_dt
to_multi_app = sub1
[]
[]
[Postprocessors]
[time]
type = TimePostprocessor
execute_on = 'timestep_end'
[]
[dt]
type = TimestepSize
execute_on = 'timestep_end'
[]
[]
(test/tests/transfers/multiapp_postprocessor_transfer/parent.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 10
ny = 10
[]
[Variables]
[u]
[]
[]
[Kernels]
[diff]
type = CoefDiffusion
variable = u
coef = 0.01
[]
[td]
type = TimeDerivative
variable = u
[]
[]
[BCs]
[left]
type = DirichletBC
variable = u
boundary = left
value = 0
[]
[right]
type = DirichletBC
variable = u
boundary = right
value = 1
[]
[]
[Postprocessors]
[average]
type = ElementAverageValue
variable = u
execute_on = 'TRANSFER'
[]
[]
[Executioner]
type = Transient
num_steps = 5
solve_type = 'PJFNK'
petsc_options_iname = '-pc_type -pc_hypre_type'
petsc_options_value = 'hypre boomeramg'
nl_rel_tol = 1e-12
[]
[Outputs]
exodus = true
[]
[MultiApps]
[pp_sub]
app_type = MooseTestApp
positions = '0.5 0.5 0 0.7 0.7 0'
execute_on = timestep_end
type = TransientMultiApp
input_files = sub.i
[]
[]
[Transfers]
[pp_transfer]
type = MultiAppPostprocessorTransfer
to_multi_app = pp_sub
from_postprocessor = average
to_postprocessor = from_parent
[]
[]
(modules/combined/test/tests/subchannel_thm_coupling/THM_SCM_coupling.i)
# THM file based on https://mooseframework.inl.gov/modules/thermal_hydraulics/tutorials/single_phase_flow/step05.html
# Used to loosely couple THM with SCM
# This is a simple open loop with fixed massflow at the inlet and pressure at the outlet.
# THM sends massflux and temperature at the inlet of the core, and pressure at the outlet of the core
# to subchannel. Subchannel returns total pressure drop of the assembly and total power to THM and THM calculates an
# average friction factor for the core region.
T_in = 583.0 # K
m_dot_in = 1 # kg/s
press = 2e5 # Pa
SC_core = 0.0004980799633447909 #m2
# core parameters
core_length = 1. # m
core_n_elems = 1
A_core = 0.005 #dummy
# pipe parameters
pipe_dia = '${units 10. cm -> m}'
A_pipe = '${fparse 0.25 * pi * pipe_dia^2}'
# 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 = sodium_eos
[]
[Functions]
[q_wall_fn]
type = ParsedFunction
symbol_names = 'core_power length'
symbol_values = 'core_power ${core_length}'
expression = 'core_power/length'
[]
[]
[FluidProperties]
[water]
type = StiffenedGasFluidProperties
gamma = 2.35
cv = 1816.0
q = -1.167e6
p_inf = 1.0e9
q_prime = 0
[]
[sodium_eos]
type = StiffenedGasFluidProperties
gamma = 1.24
cv = 1052.8
q = -2.6292e+05
p_inf = 1.1564e+08
q_prime = 0
mu = 3.222e-04
k = 73.82
[]
[]
[Closures]
[thm_closures]
type = Closures1PhaseTHM
[]
[none_closures]
type = Closures1PhaseNone
[]
[]
[Materials]
[f_mat]
type = ADParsedMaterial
property_name = f_D
postprocessor_names = 'core_f'
expression = 'core_f'
block = 'core_chan'
[]
[]
[HeatStructureMaterials]
[steel]
type = SolidMaterialProperties
rho = 8050
k = 45
cp = 466
[]
[]
[Components]
[inlet]
type = InletMassFlowRateTemperature1Phase
input = 'bottom_2:in'
m_dot = ${m_dot_in}
T = ${T_in}
[]
[outlet]
type = Outlet1Phase
input = 'bottom_1:out'
p = ${press}
[]
[up_pipe_1]
type = FlowChannel1Phase
position = '0 0 -0.5'
orientation = '0 0 1'
length = 0.5
n_elems = 15
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct1]
type = JunctionParallelChannels1Phase
position = '0 0 0'
connections = 'up_pipe_1:out core_chan:in'
volume = 1e-5
[]
[core_chan]
type = FlowChannel1Phase
position = '0 0 0'
orientation = '0 0 1'
length = ${core_length}
n_elems = ${core_n_elems}
A = ${A_core}
closures = none_closures
[]
[core_ht]
type = HeatTransferFromHeatFlux1Phase
flow_channel = core_chan
q_wall = q_wall_fn
P_hf = 1
[]
[jct2]
type = JunctionParallelChannels1Phase
position = '0 0 1'
connections = 'core_chan:out up_pipe_2:in'
volume = 1e-5
[]
[up_pipe_2]
type = FlowChannel1Phase
position = '0 0 1'
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 1.5'
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 1.5'
orientation = '1 0 0'
length = 0.5
n_elems = 10
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[jct4]
type = VolumeJunction1Phase
position = '0.5 0 1.5'
volume = 1e-5
connections = 'top_pipe_1:out top_pipe_2:in'
[]
[jct5]
type = JunctionOneToOne1Phase
connections = 'top_pipe_2:out down_pipe_1:in'
[]
[down_pipe_1]
type = FlowChannel1Phase
position = '1 0 1.5'
orientation = '0 0 -1'
length = 0.25
A = ${A_pipe}
n_elems = 5
[]
[jct6]
type = JunctionParallelChannels1Phase
position = '1 0 1.25'
connections = 'down_pipe_1:out hx/pri:in'
volume = 1e-5
[]
[hx]
[pri]
type = FlowChannel1Phase
position = '1 0 1.25'
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 1.25'
orientation = '0 0 -1'
length = ${hx_length}
n_elems = ${hx_n_elems}
widths = '${hx_wall_thickness}'
n_part_elems = '3'
materials = 'steel'
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 -0.25'
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 -0.5'
orientation = '-1 0 0'
length = 0.5
n_elems = 5
A = ${A_pipe}
D_h = ${pipe_dia}
[]
[bottom_2]
type = FlowChannel1Phase
position = '0.5 0 -0.5'
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 = ${m_dot_sec_in}
T = 300
[]
[outlet_sec]
type = Outlet1Phase
input = 'hx/sec:out'
p = 1e5
[]
[]
[Postprocessors]
[power_to_coolant]
type = ADHeatRateDirectFlowChannel
q_wall_prop = q_wall
block = core_chan
P_hf = 1
[]
[core_T_out]
type = SideAverageValue
boundary = core_chan:out
variable = T
[]
[T_out]
type = SideAverageValue
boundary = bottom_1:out
variable = T
[]
[core_p_in]
type = SideAverageValue
boundary = up_pipe_1:out
variable = p
[]
[core_p_out]
type = SideAverageValue
boundary = up_pipe_2:in
variable = p
[]
[core_delta_p]
type = ParsedPostprocessor
pp_names = 'core_p_in core_p_out'
function = '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
[]
############## Friction Factor Calculation #############
[av_rhouA]
type = ElementAverageValue
variable = 'rhouA'
block = 'core_chan'
[]
[av_rho]
type = ElementAverageValue
variable = 'rho'
block = 'core_chan'
[]
[Kloss]
type = ParsedPostprocessor
pp_names = 'core_delta_p_tgt av_rhouA av_rho'
function = '2.0 * core_delta_p_tgt * av_rho * ${A_core} * ${A_core} / (av_rhouA * av_rhouA)'
[]
[Dh]
type = ADElementAverageMaterialProperty
mat_prop = D_h
block = core_chan
[]
[core_f]
type = ParsedPostprocessor
pp_names = 'Kloss Dh'
function = 'Kloss * Dh / ${core_length}'
[]
### INFO to send to SC
[outlet_pressure]
type = SideAverageValue
boundary = up_pipe_2:in
variable = p
[]
[inlet_mass_flow_rate]
type = ADFlowJunctionFlux1Phase
boundary = up_pipe_1:out
connection_index = 0
equation = mass
junction = jct1
[]
[inlet_temperature]
type = SideAverageValue
boundary = up_pipe_1:out
variable = T
[]
[inlet_mass_flux]
type = ParsedPostprocessor
pp_names = 'inlet_mass_flow_rate'
function = 'abs(inlet_mass_flow_rate/${SC_core})'
[]
#####
##### Info received from subchannel
[core_delta_p_tgt]
type = Receiver
default = 100
[]
[core_power]
type = Receiver
default = 100
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
start_time = 0
[TimeStepper]
type = IterationAdaptiveDT
dt = 0.01
[]
# dtmax = 5
end_time = 5
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]
csv = true
[console]
type = Console
max_rows = 1
outlier_variable_norms = false
[]
print_linear_residuals = false
[]
################################################################################
# A multiapp that couples THM to subchannel
################################################################################
[MultiApps]
[subchannel]
type = FullSolveMultiApp
input_files = 'subchannel.i'
execute_on = 'timestep_end'
positions = '0 0 0'
max_procs_per_app = 1
output_in_position = true
bounding_box_padding = '0 0 0.1'
[]
[]
[Transfers]
[pressure_drop_transfer] # Get pressure drop to THM from subchannel
type = MultiAppPostprocessorTransfer
from_multi_app = subchannel
from_postprocessor = total_pressure_drop_SC
to_postprocessor = core_delta_p_tgt
reduction_type = average
execute_on = 'timestep_end'
[]
[power_transfer] # Get Total power to THM from subchannel
type = MultiAppPostprocessorTransfer
from_multi_app = subchannel
from_postprocessor = Total_power
to_postprocessor = core_power
reduction_type = average
execute_on = 'timestep_end'
[]
[mass_flux_tranfer] # Send mass_flux at the inlet of THM core to subchannel
type = MultiAppPostprocessorTransfer
to_multi_app = subchannel
from_postprocessor = inlet_mass_flux
to_postprocessor = report_mass_flux_inlet
execute_on = 'timestep_end'
[]
[outlet_pressure_tranfer] # Send pressure at the outlet of THM core to subchannel
type = MultiAppPostprocessorTransfer
to_multi_app = subchannel
from_postprocessor = outlet_pressure
to_postprocessor = report_pressure_outlet
execute_on = 'timestep_end'
[]
[inlet_temperature_transfer]
type = MultiAppPostprocessorTransfer
to_multi_app = subchannel
from_postprocessor = inlet_temperature
to_postprocessor = report_temperature_inlet
execute_on = 'timestep_end'
[]
[]
(test/tests/transfers/multiapp_postprocessor_transfer/between_multiapp/main.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 10
ny = 10
[]
[Variables]
[u]
[]
[]
[Kernels]
[diff]
type = CoefDiffusion
variable = u
coef = 0.01
[]
[td]
type = TimeDerivative
variable = u
[]
[]
[BCs]
[left]
type = DirichletBC
variable = u
boundary = left
value = 0
[]
[right]
type = DirichletBC
variable = u
boundary = right
value = 1
[]
[]
[Executioner]
type = Transient
num_steps = 5
solve_type = 'PJFNK'
petsc_options_iname = '-pc_type -pc_hypre_type'
petsc_options_value = 'hypre boomeramg'
nl_rel_tol = 1e-12
[]
[MultiApps]
[pp_sub_0]
app_type = MooseTestApp
positions = '0.5 0.5 0 0.7 0.7 0'
execute_on = timestep_end
type = TransientMultiApp
input_files = sub0.i
[]
[pp_sub_1]
app_type = MooseTestApp
positions = '0.5 0.5 0 0.7 0.7 0'
execute_on = timestep_end
type = TransientMultiApp
input_files = sub1.i
[]
[]
[Transfers]
[pp_transfer_1]
type = MultiAppPostprocessorTransfer
from_multi_app = pp_sub_0
to_multi_app = pp_sub_1
from_postprocessor = average_0
to_postprocessor = from_0
[]
[pp_transfer_2]
type = MultiAppPostprocessorTransfer
from_multi_app = pp_sub_1
to_multi_app = pp_sub_0
from_postprocessor = average_1
to_postprocessor = from_1
[]
[]
(test/tests/multiapps/picard_postprocessor/transient_main.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 5
ny = 5
parallel_type = replicated
uniform_refine = 1
[]
[Variables]
[u]
[]
[]
[Kernels]
[diff]
type = Diffusion
variable = u
[]
[time]
type = TimeDerivative
variable = u
[]
[source]
type = BodyForce
variable = u
value = 1
[]
[]
[BCs]
[left]
type = PostprocessorDirichletBC
variable = u
boundary = left
postprocessor = 'from_sub'
[]
[]
[Postprocessors]
[coupling_its]
type = NumFixedPointIterations
execute_on = 'initial timestep_end'
[]
[from_sub]
type = Receiver
default = 0
[]
[to_sub]
type = SideAverageValue
variable = u
boundary = right
[]
[average]
type = ElementAverageValue
variable = u
[]
[]
[Executioner]
type = Transient
num_steps = 10
dt = 0.1
solve_type = PJFNK
petsc_options_iname = '-pc_type -pc_hypre_type'
petsc_options_value = 'hypre boomeramg'
nl_abs_tol = 1e-14
# App coupling parameters
fixed_point_max_its = 30
relaxation_factor = 0.8
transformed_postprocessors = 'from_sub'
[]
[Outputs]
csv = true
exodus = false
[]
[MultiApps]
[sub]
type = TransientMultiApp
app_type = MooseTestApp
positions = '0 0 0'
input_files = 'transient_sub.i'
clone_parent_mesh = true
execute_on = 'timestep_begin'
# The input was originally created with effectively no restore
# see the changes made for #5554 then reverted in #28115
no_restore = true
[]
[]
[Transfers]
[left_from_sub]
type = MultiAppPostprocessorTransfer
from_multi_app = sub
from_postprocessor = 'to_main'
to_postprocessor = 'from_sub'
reduction_type = 'average'
[]
[right_to_sub]
type = MultiAppPostprocessorTransfer
to_multi_app = sub
from_postprocessor = 'to_sub'
to_postprocessor = 'from_main'
[]
[]
(test/tests/transfers/multiapp_postprocessor_transfer/from_one_sub_parent.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 10
ny = 10
[]
[Variables]
[./u]
[../]
[]
[AuxVariables]
[./from_sub]
[../]
[]
[Kernels]
[./diff]
type = Diffusion
variable = u
[../]
[]
[BCs]
[./left]
type = DirichletBC
variable = u
boundary = left
value = 0
[../]
[./right]
type = DirichletBC
variable = u
boundary = right
value = 1
[../]
[]
[Postprocessors]
[./sub_average]
type = Receiver
[../]
[./sub_sum]
type = Receiver
[../]
[./sub_maximum]
type = Receiver
[../]
[./sub_minimum]
type = Receiver
[../]
[]
[Executioner]
type = Transient
num_steps = 1
dt = 1
solve_type = 'PJFNK'
petsc_options_iname = '-pc_type -pc_hypre_type'
petsc_options_value = 'hypre boomeramg'
[]
[Outputs]
exodus = true
[]
[MultiApps]
[./sub]
positions = '0.2 0.2 0'
type = TransientMultiApp
app_type = MooseTestApp
input_files = 'sub0.i'
[../]
[]
[Transfers]
[./pp_transfer_ave]
type = MultiAppPostprocessorTransfer
reduction_type = average
from_multi_app = sub
from_postprocessor = average
to_postprocessor = sub_average
[../]
[./pp_transfer_sum]
type = MultiAppPostprocessorTransfer
reduction_type = sum
from_multi_app = sub
from_postprocessor = average
to_postprocessor = sub_sum
[../]
[./pp_transfer_min]
type = MultiAppPostprocessorTransfer
reduction_type = minimum
from_multi_app = sub
from_postprocessor = average
to_postprocessor = sub_minimum
[../]
[./pp_transfer_max]
type = MultiAppPostprocessorTransfer
reduction_type = maximum
from_multi_app = sub
from_postprocessor = average
to_postprocessor = sub_maximum
[../]
[]
(test/tests/multiapps/picard_multilevel/multilevel_dt_rejection/picard_sub.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 10
ny = 10
[]
[Variables]
[v]
[]
[]
[AuxVariables]
[v2]
[]
[v3]
[]
[w]
[]
[]
[AuxKernels]
[set_w]
type = NormalizationAux
variable = w
source_variable = v
normal_factor = 0.1
[]
[]
[Kernels]
[diff_v]
type = Diffusion
variable = v
[]
[coupled_force]
type = CoupledForce
variable = v
v = v2
[]
[coupled_force2]
type = CoupledForce
variable = v
v = v3
[]
[td_v]
type = TimeDerivative
variable = v
[]
[]
[BCs]
[left_v]
type = FunctionDirichletBC
variable = v
boundary = left
function = func
[]
[right_v]
type = DirichletBC
variable = v
boundary = right
value = 0
[]
[]
[Functions]
[func]
type = ParsedFunction
expression = 'if(t < 2.5, 1, 1 / t)'
[]
[]
[Postprocessors]
[picard_its]
type = NumFixedPointIterations
execute_on = 'initial timestep_end'
[]
[parent_time]
type = Receiver
execute_on = 'timestep_end'
[]
[parent_dt]
type = Receiver
execute_on = 'timestep_end'
[]
[time]
type = TimePostprocessor
execute_on = 'timestep_end'
[]
[dt]
type = TimestepSize
execute_on = 'timestep_end'
[]
[]
[Executioner]
type = Transient
solve_type = PJFNK
petsc_options_iname = '-pc_type -pc_hypre_type'
petsc_options_value = 'hypre boomeramg'
fixed_point_max_its = 2 # deliberately make it fail at 2 to test the time step rejection behavior
nl_rel_tol = 1e-5 # loose enough to force multiple Picard iterations on this example
l_tol = 1e-5 # loose enough to force multiple Picard iterations on this example
fixed_point_rel_tol = 1e-8
num_steps = 2
[]
[MultiApps]
[sub2]
type = TransientMultiApp
positions = '0 0 0'
input_files = picard_sub2.i
execute_on = timestep_end
[]
[]
[Transfers]
[v_to_v3]
type = MultiAppGeneralFieldNearestLocationTransfer
from_multi_app = sub2
source_variable = v
variable = v3
[]
[w]
type = MultiAppGeneralFieldNearestLocationTransfer
to_multi_app = sub2
source_variable = w
variable = w
[]
[time_to_sub]
type = MultiAppPostprocessorTransfer
from_postprocessor = time
to_postprocessor = sub_time
to_multi_app = sub2
[]
[dt_to_sub]
type = MultiAppPostprocessorTransfer
from_postprocessor = dt
to_postprocessor = sub_dt
to_multi_app = sub2
[]
[matser_time_to_sub]
type = MultiAppPostprocessorTransfer
from_postprocessor = time
to_postprocessor = parent_time
to_multi_app = sub2
[]
[parent_dt_to_sub]
type = MultiAppPostprocessorTransfer
from_postprocessor = dt
to_postprocessor = parent_dt
to_multi_app = sub2
[]
[]
(test/tests/multiapps/picard_postprocessor/steady_main.i)
[Mesh]
type = GeneratedMesh
dim = 2
nx = 5
ny = 5
parallel_type = replicated
uniform_refine = 1
[]
[Variables]
[u]
[]
[]
[Kernels]
[diff]
type = Diffusion
variable = u
[]
[source]
type = BodyForce
variable = u
value = 1
[]
[]
[BCs]
[left]
type = PostprocessorDirichletBC
variable = u
boundary = left
postprocessor = 'from_sub'
[]
[]
[Postprocessors]
[from_sub]
type = Receiver
default = 0
[]
[to_sub]
type = SideAverageValue
variable = u
boundary = right
[]
[average]
type = ElementAverageValue
variable = u
[]
[]
[Executioner]
type = Steady
# Solve parameters
solve_type = PJFNK
petsc_options_iname = '-pc_type -pc_hypre_type'
petsc_options_value = 'hypre boomeramg'
nl_abs_tol = 1e-14
# App coupling parameters
fixed_point_max_its = 100
fixed_point_rel_tol = 0.5 # pseudo transient is slow to converge
relaxation_factor = 0.8
transformed_postprocessors = 'from_sub'
[]
[Outputs]
csv = true
exodus = false
[]
[MultiApps]
[sub]
type = FullSolveMultiApp
app_type = MooseTestApp
positions = '0 0 0'
input_files = steady_sub.i
clone_parent_mesh = true
execute_on = 'timestep_begin'
# we keep the full postprocessor output history of the subapp
keep_full_output_history = true
relaxation_factor = 0.8
transformed_postprocessors = 'from_main'
[]
[]
[Transfers]
[left_from_sub]
type = MultiAppPostprocessorTransfer
from_multi_app = sub
from_postprocessor = 'to_main'
to_postprocessor = 'from_sub'
reduction_type = 'average'
[]
[right_to_sub]
type = MultiAppPostprocessorTransfer
to_multi_app = sub
from_postprocessor = 'to_sub'
to_postprocessor = 'from_main'
[]
[]
(modules/thermal_hydraulics/test/tests/components/hs_boundary_external_app_heat_flux/main.i)
# Main input file.
#
# Run mesh.i first to produce a mesh file that this input uses:
#
# thermal_hydraulics-opt -i mesh.i --mesh-only mesh.e
length = 5.0
n_elems_axial = 10
rho_name = density
cp_name = specific_heat
k_name = thermal_conductivity
rho = 8000.0
cp = 500.0
k = 15.0
T_initial = 500.0
power = 1000.0
[Mesh]
type = FileMesh
file = mesh.e
[]
[Variables]
[T_solid]
[]
[]
[ICs]
[T_ic]
type = ConstantIC
variable = T_solid
value = ${T_initial}
[]
[]
[Kernels]
[time_derivative]
type = ADHeatConductionTimeDerivative
variable = T_solid
density_name = ${rho_name}
specific_heat = ${cp_name}
[]
[heat_conduction]
type = ADHeatConduction
variable = T_solid
thermal_conductivity = ${k_name}
[]
[]
[BCs]
[bc]
type = FunctorNeumannBC
variable = T_solid
boundary = 'inner'
functor = heat_flux_fn
flux_is_inward = false
[]
[]
[Materials]
[ad_constant_mat]
type = ADGenericConstantMaterial
prop_names = '${rho_name} ${cp_name} ${k_name}'
prop_values = '${rho} ${cp} ${k}'
[]
[]
[Functions]
[heat_flux_fn]
type = ParsedFunction
symbol_names = 'S'
symbol_values = 'inner_surface_area'
expression = '${power} / S'
[]
[]
[Postprocessors]
[inner_surface_area]
type = AreaPostprocessor
boundary = 'inner'
execute_on = 'INITIAL'
[]
[inner_perimeter]
type = ParsedPostprocessor
pp_names = 'inner_surface_area'
expression = 'inner_surface_area / ${length}'
execute_on = 'INITIAL'
[]
[]
[MultiApps]
[sub]
type = TransientMultiApp
app_type = ThermalHydraulicsApp
input_files = 'sub.i'
positions = '0 0 0'
max_procs_per_app = 1
output_in_position = true
execute_on = 'TIMESTEP_END'
[]
[]
[UserObjects]
[layered_average_heat_flux]
type = NearestPointLayeredSideAverageFunctor
direction = z
points='0 0 0'
num_layers = ${n_elems_axial}
functor = heat_flux_fn
boundary = 'inner'
execute_on = 'TIMESTEP_END'
[]
[]
[Transfers]
[heat_flux_transfer]
type = MultiAppGeneralFieldUserObjectTransfer
to_multi_app = sub
source_user_object = layered_average_heat_flux
variable = q_ext
error_on_miss = true
[]
[perimeter_transfer]
type = MultiAppPostprocessorTransfer
to_multi_app = sub
from_postprocessor = inner_perimeter
to_postprocessor = P_ext
[]
[]
[Preconditioning]
[pc]
type = SMP
full = true
[]
[]
[Executioner]
type = Transient
scheme = bdf2
dt = 10.0
num_steps = 1
abort_on_solve_fail = true
solve_type = NEWTON
nl_abs_tol = 1e-10
nl_rel_tol = 1e-8
nl_max_its = 10
l_tol = 1e-3
l_max_its = 10
[]