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OGS
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OGS
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<OpenGeoSysProject>
<meshes>
<mesh axially_symmetric="false">domain.vtu</mesh>
<mesh axially_symmetric="false">boundary_left.vtu</mesh>
<mesh axially_symmetric="false">boundary_right.vtu</mesh>
<mesh axially_symmetric="false">boundary_bottom.vtu</mesh>
</meshes>
<processes>
<process>
<name>TH2M</name>
<type>TH2M</type>
<integration_order>3</integration_order>
<constitutive_relation>
<type>LinearElasticIsotropic</type>
<youngs_modulus>E</youngs_modulus>
<poissons_ratio>nu</poissons_ratio>
</constitutive_relation>
<jacobian_assembler>
<type>CentralDifferences</type>
<component_magnitudes>1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0</component_magnitudes>
<relative_epsilons>1e-03 1e-03 1e-03 1e-03 1e-03 1e-03 1e-03 1e-03 1e-06 1e-06 1e-06 1e-06 1e-08 1e-08 1e-08 1e-08 1e-08 1e-08 1e-08 1e-08 1e-08 1e-08 1e-08 1e-08 1e-08 1e-08 1e-08 1e-08</relative_epsilons>
</jacobian_assembler>
<reference_temperature>T0</reference_temperature>
<process_variables>
<gas_pressure>gas_pressure</gas_pressure>
<capillary_pressure>capillary_pressure</capillary_pressure>
<temperature>temperature</temperature>
<displacement>displacement</displacement>
</process_variables>
<secondary_variables>
<secondary_variable internal_name="velocity_gas" output_name="velocity_gas" />
<secondary_variable internal_name="velocity_liquid" output_name="velocity_liquid" />
<secondary_variable internal_name="sigma" output_name="sigma" />
<secondary_variable internal_name="epsilon" output_name="epsilon" />
<secondary_variable internal_name="liquid_density" output_name="liquid_density" />
<secondary_variable internal_name="gas_density" output_name="gas_density" />
<secondary_variable internal_name="porosity" output_name="porosity" />
<secondary_variable internal_name="saturation" output_name="saturation" />
</secondary_variables>
<specific_body_force>0 0</specific_body_force>
</process>
</processes>
<media>
<medium id="0">
<phases>
<phase>
<type>AqueousLiquid</type>
<properties>
<property>
<name>specific_heat_capacity</name>
<type>Constant</type>
<value>0.0</value>
</property>
<property>
<name>thermal_conductivity</name>
<type>Constant</type>
<value>0</value>
</property>
<property>
<name>density</name>
<type>Constant</type>
<value>0</value>
</property>
<property>
<name>viscosity</name>
<type>Constant</type>
<value>1</value>
</property>
</properties>
</phase>
<phase>
<type>Gas</type>
<properties>
<property>
<name>specific_heat_capacity</name>
<type>Constant</type>
<value>4280.0</value>
</property>
<property>
<name>molar_mass</name>
<type>Constant</type>
<value>.028949</value>
</property>
<property>
<name>thermal_conductivity</name>
<type>Constant</type>
<value>0.6</value>
</property>
<property>
<name>density</name>
<type>Linear</type>
<reference_value>999.1</reference_value>
<independent_variable>
<variable_name>temperature</variable_name>
<reference_condition>273.15</reference_condition>
<slope>-4.e-4</slope>
</independent_variable>
</property>
<property>
<name>viscosity</name>
<type>Constant</type>
<value>1.e-3</value>
</property>
</properties>
</phase>
<phase>
<type>Solid</type>
<properties>
<property>
<name>density</name>
<type>Constant</type>
<value>2290.0</value>
</property>
<property>
<name>thermal_conductivity</name>
<type>Constant</type>
<value>1.838</value>
</property>
<property>
<name>specific_heat_capacity</name>
<type>Constant</type>
<value>917.654</value>
</property>
<property>
<name>thermal_expansivity</name>
<type>Constant</type>
<value>1.5e-5</value>
</property>
</properties>
</phase>
</phases>
<properties>
<property>
<name>permeability</name>
<type>Constant</type>
<value>2.e-20</value>
</property>
<property>
<name>biot_coefficient</name>
<type>Constant</type>
<value>1.0</value>
</property>
<property>
<name>saturation</name>
<type>Constant</type>
<value>0</value>
</property>
<property>
<name>relative_permeability</name>
<type>Constant</type>
<value>0</value>
</property>
<property>
<name>relative_permeability_nonwetting_phase</name>
<type>Constant</type>
<value>1</value>
</property>
<property>
<name>porosity</name>
<type>Constant</type>
<value>0.16</value>
</property>
<property>
<name>thermal_conductivity</name>
<type>EffectiveThermalConductivityPorosityMixing</type>
</property>
<property>
<name>bishops_effective_stress</name>
<type>BishopsPowerLaw</type>
<exponent>1</exponent>
</property>
</properties>
</medium>
</media>
<time_loop>
<processes>
<process ref="TH2M">
<nonlinear_solver>basic_newton</nonlinear_solver>
<convergence_criterion>
<type>PerComponentDeltaX</type>
<norm_type>NORM2</norm_type>
<abstols>1e-3 1e-3 1e-5 1e-6 1.e-6</abstols>
</convergence_criterion>
<time_discretization>
<type>BackwardEuler</type>
</time_discretization>
<time_stepping>
<type>FixedTimeStepping</type>
<t_initial>0</t_initial>
<t_end>100000</t_end>
<timesteps>
<pair>
<repeat>5</repeat>
<delta_t>20000</delta_t>
</pair>
</timesteps>
</time_stepping>
</process>
</processes>
<output>
<type>VTK</type>
<prefix>result_1d_dirichlet_slab</prefix>
<timesteps>
<pair>
<repeat>1</repeat>
<each_steps>5</each_steps>
</pair>
</timesteps>
<variables>
<variable>gas_pressure</variable>
<variable>gas_pressure_interpolated</variable>
<variable>capillary_pressure</variable>
<variable>capillary_pressure_interpolated</variable>
<variable>liquid_pressure_interpolated</variable>
<variable>temperature</variable>
<variable>temperature_interpolated</variable>
<variable>displacement</variable>
<variable>sigma</variable>
<variable>epsilon</variable>
<variable>velocity_gas</variable>
<variable>velocity_liquid</variable>
<variable>liquid_density</variable>
<variable>gas_density</variable>
<variable>porosity</variable>
<variable>saturation</variable>
</variables>
</output>
</time_loop>
<parameters>
<parameter>
<name>E</name>
<type>Constant</type>
<value>5.e9</value>
</parameter>
<parameter>
<name>nu</name>
<type>Constant</type>
<value>0.3</value>
</parameter>
<parameter>
<name>T0</name>
<type>Constant</type>
<value>273.15</value>
</parameter>
<parameter>
<name>displacement0</name>
<type>Constant</type>
<values>0 0</values>
</parameter>
<parameter>
<name>pressure_ic</name>
<type>Constant</type>
<values>0</values>
</parameter>
<parameter>
<name>dirichlet0</name>
<type>Constant</type>
<value>0</value>
</parameter>
<parameter>
<name>temperature_ic</name>
<type>Constant</type>
<value>273.15</value>
</parameter>
<parameter>
<name>pressure_bc_left</name>
<type>Constant</type>
<value>0</value>
</parameter>
<parameter>
<name>temperature_bc_left</name>
<type>Constant</type>
<value>320</value>
</parameter>
<parameter>
<name>temperature_bc_right</name>
<type>Constant</type>
<value>273.15</value>
</parameter>
</parameters>
<process_variables>
<process_variable>
<name>displacement</name>
<components>2</components>
<order>2</order>
<initial_condition>displacement0</initial_condition>
<boundary_conditions>
<boundary_condition>
<mesh>boundary_bottom</mesh>
<type>Dirichlet</type>
<component>1</component>
<parameter>dirichlet0</parameter>
</boundary_condition>
<boundary_condition>
<mesh>boundary_left</mesh>
<type>Dirichlet</type>
<component>0</component>
<parameter>dirichlet0</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<process_variable>
<name>gas_pressure</name>
<components>1</components>
<order>1</order>
<initial_condition>pressure_ic</initial_condition>
<boundary_conditions>
<boundary_condition>
<mesh>boundary_right</mesh>
<type>Dirichlet</type>
<component>0</component>
<parameter>pressure_bc_left</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<process_variable>
<name>capillary_pressure</name>
<components>1</components>
<order>1</order>
<initial_condition>dirichlet0</initial_condition>
<boundary_conditions>
<boundary_condition>
<mesh>domain</mesh>
<type>Dirichlet</type>
<component>0</component>
<parameter>dirichlet0</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<process_variable>
<name>temperature</name>
<components>1</components>
<order>1</order>
<initial_condition>temperature_ic</initial_condition>
<boundary_conditions>
<boundary_condition>
<mesh>boundary_left</mesh>
<type>Dirichlet</type>
<component>0</component>
<parameter>temperature_bc_left</parameter>
</boundary_condition>
<boundary_condition>
<mesh>boundary_right</mesh>
<type>Dirichlet</type>
<component>0</component>
<parameter>temperature_bc_right</parameter>
</boundary_condition>
</boundary_conditions>
<source_terms />
</process_variable>
</process_variables>
<nonlinear_solvers>
<nonlinear_solver>
<name>basic_newton</name>
<type>Newton</type>
<max_iter>20</max_iter>
<linear_solver>general_linear_solver</linear_solver>
</nonlinear_solver>
</nonlinear_solvers>
<linear_solvers>
<linear_solver>
<name>general_linear_solver</name>
<lis>-i bicgstab -p ilu -tol 1e-16 -maxiter 10000</lis>
<eigen>
<solver_type>SparseLU</solver_type>
<scaling>true</scaling>
</eigen>
<petsc>
<prefix>sd</prefix>
<parameters>-sd_ksp_type cg -sd_pc_type bjacobi -sd_ksp_rtol 1e-16 -sd_ksp_max_it 10000</parameters>
</petsc>
</linear_solver>
</linear_solvers>
</OpenGeoSysProject>
1.12.0