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Commit 1ceef03b authored by Tom Fischer's avatar Tom Fischer
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[T] Test for bulk triangle to line point mapping.

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ProcessLib/LiquidFlow/Tests.cmake
+ 16
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View file @ 1ceef03b
...@@ -381,7 +381,7 @@ AddTest( ...@@ -381,7 +381,7 @@ AddTest(
) )
AddTest( AddTest(
NAME LiquidFlow_Flux_2D NAME LiquidFlow_Flux_2D_Quads
PATH Parabolic/LiquidFlow/Flux/2D PATH Parabolic/LiquidFlow/Flux/2D
EXECUTABLE ogs EXECUTABLE ogs
EXECUTABLE_ARGS square_1e1_calculatesurfaceflux.prj EXECUTABLE_ARGS square_1e1_calculatesurfaceflux.prj
...@@ -395,6 +395,21 @@ AddTest( ...@@ -395,6 +395,21 @@ AddTest(
LF_square_1e1_surfaceflux_pcs_0_ts_2_t_0.864000_expected.vtu LF_square_1e1_surfaceflux_pcs_0_ts_2_t_0.864000.vtu pressure pressure 1e-7 1e-13 LF_square_1e1_surfaceflux_pcs_0_ts_2_t_0.864000_expected.vtu LF_square_1e1_surfaceflux_pcs_0_ts_2_t_0.864000.vtu pressure pressure 1e-7 1e-13
) )
AddTest(
NAME LiquidFlow_Flux_2D_Tris
PATH Parabolic/LiquidFlow/Flux/2D
EXECUTABLE ogs
EXECUTABLE_ARGS square_1.8e1_calculatesurfaceflux.prj
WRAPPER time
TESTER vtkdiff
REQUIREMENTS NOT OGS_USE_MPI
DIFF_DATA
square_1x1_tri_1.8e1_complete_boundary_left_right_dirichlet_specific_flux_t_0.432000_expected.vtu square_1x1_tri_1.8e1_complete_boundary_left_right_dirichlet_specific_flux_t_0.432000.vtu specific_flux specific_flux 1e-7 1e-13
square_1x1_tri_1.8e1_complete_boundary_left_right_dirichlet_specific_flux_t_0.864000_expected.vtu square_1x1_tri_1.8e1_complete_boundary_left_right_dirichlet_specific_flux_t_0.864000.vtu specific_flux specific_flux 1e-7 1e-13
LF_square_1x1_tri_1.8e1_surfaceflux_pcs_0_ts_1_t_0.432000_expected.vtu LF_square_1x1_tri_1.8e1_surfaceflux_pcs_0_ts_1_t_0.432000.vtu pressure pressure 1e-7 1e-13
LF_square_1x1_tri_1.8e1_surfaceflux_pcs_0_ts_2_t_0.864000_expected.vtu LF_square_1x1_tri_1.8e1_surfaceflux_pcs_0_ts_2_t_0.864000.vtu pressure pressure 1e-7 1e-13
)
#AddTest( #AddTest(
# NAME LiquidFlow_SimpleSynthetics_constraint_dirichlet_bc # NAME LiquidFlow_SimpleSynthetics_constraint_dirichlet_bc
# PATH Parabolic/LiquidFlow/SimpleSynthetics # PATH Parabolic/LiquidFlow/SimpleSynthetics
......
Tests/Data/Parabolic/LiquidFlow/Flux/2D/square_1.8e1_calculatesurfaceflux.prj 0 → 100644
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− 0
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<?xml version="1.0" encoding="ISO-8859-1"?>
<OpenGeoSysProject>
<meshes>
<mesh>square_1x1_tri_1.8e1.vtu</mesh>
<mesh>square_1x1_tri_1.8e1_complete_boundary.vtu</mesh>
<mesh>square_1x1_tri_1.8e1_left.vtu</mesh>
<mesh>square_1x1_tri_1.8e1_right.vtu</mesh>
</meshes>
<processes>
<process>
<name>LiquidFlow</name>
<type>LIQUID_FLOW</type>
<integration_order>2</integration_order>
<darcy_gravity>
<!-- axis_id: 0, 1, or the dimension of space minus one -->
<axis_id>0</axis_id>
<!-- g>=0. g=0: non gravity term -->
<g>0.</g>
</darcy_gravity>
<process_variables>
<process_variable>pressure</process_variable>
</process_variables>
<secondary_variables>
<secondary_variable internal_name="darcy_velocity" output_name="v"/>
</secondary_variables>
<calculatesurfaceflux>
<mesh>square_1x1_tri_1.8e1_complete_boundary</mesh>
<property_name>specific_flux</property_name>
<output_mesh>square_1x1_tri_1.8e1_complete_boundary_left_right_dirichlet_specific_flux.vtu</output_mesh>
</calculatesurfaceflux>
</process>
</processes>
<time_loop>
<processes>
<process ref="LiquidFlow">
<nonlinear_solver>basic_picard</nonlinear_solver>
<convergence_criterion>
<type>DeltaX</type>
<norm_type>NORM2</norm_type>
<abstol>1.e-10</abstol>
</convergence_criterion>
<time_discretization>
<type>BackwardEuler</type>
</time_discretization>
<time_stepping>
<type>FixedTimeStepping</type>
<t_initial> 0.0 </t_initial>
<t_end> 0.864 </t_end>
<timesteps>
<pair>
<repeat>2</repeat>
<delta_t>0.432</delta_t>
</pair>
</timesteps>
</time_stepping>
</process>
</processes>
<output>
<type>VTK</type>
<prefix>LF_square_1x1_tri_1.8e1_surfaceflux</prefix>
<timesteps>
<pair>
<repeat> 1 </repeat>
<each_steps> 1 </each_steps>
</pair>
</timesteps>
<variables>
<variable> pressure </variable>
<variable> v </variable>
</variables>
</output>
</time_loop>
<media>
<medium id="0">
<phases>
<phase>
<type>AqueousLiquid</type>
<properties>
<property>
<name>viscosity</name>
<type>Constant</type>
<value> 1.295e-4 </value>
</property>
<property>
<name>density</name>
<type>Constant</type>
<value> 78.68 </value>
</property>
</properties>
</phase>
</phases>
<properties>
<property>
<name>permeability</name>
<type>Constant</type>
<value>9.2e-12 0 0 9.2e-12</value>
</property>
<property>
<name>reference_temperature</name>
<type>Constant</type>
<value>293.15</value>
</property>
<property>
<name>porosity</name>
<type>Constant</type>
<value>1</value>
</property>
<property>
<name>storage</name>
<type>Constant</type>
<value> 8.05e-10 </value>
</property>
</properties>
</medium>
</media>
<parameters>
<parameter>
<name>p0</name>
<type>Constant</type>
<value>5e6</value>
</parameter>
<parameter>
<name>p_Dirichlet_left</name>
<type>Constant</type>
<value>1e7</value>
</parameter>
<parameter>
<name>p_Dirichlet_right</name>
<type>Constant</type>
<value>1e6</value>
</parameter>
<parameter>
<name>constant_porosity_parameter</name>
<type>Constant</type>
<value>1</value>
</parameter>
<parameter>
<name>kappa1</name>
<type>Constant</type>
<values>9.2e-12 0 0 9.2e-12</values>
</parameter>
<parameter>
<name>p_spatial</name>
<type>Constant</type>
<value>1</value>
</parameter>
</parameters>
<process_variables>
<process_variable>
<name>pressure</name>
<components>1</components>
<order>1</order>
<initial_condition>p0</initial_condition>
<boundary_conditions>
<boundary_condition>
<mesh>square_1x1_tri_1.8e1_left</mesh>
<type>Dirichlet</type>
<parameter>p_Dirichlet_left</parameter>
</boundary_condition>
<boundary_condition>
<mesh>square_1x1_tri_1.8e1_right</mesh>
<type>Dirichlet</type>
<parameter>p_Dirichlet_right</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
</process_variables>
<nonlinear_solvers>
<nonlinear_solver>
<name>basic_picard</name>
<type>Picard</type>
<max_iter>10</max_iter>
<linear_solver>general_linear_solver</linear_solver>
</nonlinear_solver>
</nonlinear_solvers>
<linear_solvers>
<linear_solver>
<name>general_linear_solver</name>
<lis>-i cg -p jacobi -tol 1e-16 -maxiter 10000</lis>
<eigen>
<solver_type>CG</solver_type>
<precon_type>DIAGONAL</precon_type>
<max_iteration_step>10000</max_iteration_step>
<error_tolerance>1e-16</error_tolerance>
</eigen>
<petsc>
<prefix>lf</prefix>
<parameters>-lf_ksp_type cg -lf_pc_type bjacobi -lf_ksp_rtol 1e-16 -lf_ksp_max_it 10000</parameters>
</petsc>
</linear_solver>
</linear_solvers>
</OpenGeoSysProject>
Tests/Data/Parabolic/LiquidFlow/Flux/2D/square_1x1_tri_1.8e1.vtu 0 → 100644 LFS
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File added
Tests/Data/Parabolic/LiquidFlow/Flux/2D/square_1x1_tri_1.8e1_complete_boundary.vtu 0 → 100644 LFS
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− 0
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File added
Tests/Data/Parabolic/LiquidFlow/Flux/2D/square_1x1_tri_1.8e1_left.vtu 0 → 100644 LFS
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Tests/Data/Parabolic/LiquidFlow/Flux/2D/square_1x1_tri_1.8e1_right.vtu 0 → 100644 LFS
+ 3
− 0
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File added
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