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OGS
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OGS
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<OpenGeoSysProject>
<meshes>
<mesh>HeatPipe_2D.vtu</mesh>
<mesh>left.vtu</mesh>
<mesh>right.vtu</mesh>
</meshes>
<processes>
<process>
<name>TP23</name>
<type>THERMAL_TWOPHASE_WITH_PP</type>
<integration_order>2</integration_order>
<process_variables>
<gas_pressure>gas_pressure</gas_pressure>
<capillary_pressure>capillary_pressure</capillary_pressure>
<temperature>temperature</temperature>
<total_molar_fraction_contaminant>Xc</total_molar_fraction_contaminant>
</process_variables>
<jacobian_assembler>
<type>CentralDifferences</type>
<component_magnitudes>1e6 1e6 1e-10 300</component_magnitudes>
<relative_epsilons>1e-8 1e-8 1e-8 1e-8</relative_epsilons>
</jacobian_assembler>
<secondary_variables>
<secondary_variable internal_name="saturation" output_name="saturation" />
<secondary_variable internal_name="pressure_wetting" output_name="pressure_wetting" />
<secondary_variable internal_name="gas_molar_fraction_water" output_name="xwG" />
<secondary_variable internal_name="liquid_molar_fraction_contaminant" output_name="xcL" />
<secondary_variable internal_name="gas_molar_fraction_contaminant" output_name="xcG" />
</secondary_variables>
<specific_body_force>0</specific_body_force>
<mass_lumping>true</mass_lumping>
</process>
</processes>
<media>
<medium id="0">
<phases>
<phase>
<type>Gas</type>
<components>
<component>
<name>w</name>
<properties>
<property>
<name>molar_mass</name>
<type>Constant</type>
<value>0.018016</value>
</property>
<property>
<name>pore_diffusion</name>
<type>Constant</type>
<value>2.6e-6</value>
</property>
<property>
<name>specific_heat_capacity</name>
<type>Constant</type>
<value>4187</value>
</property>
<property>
<name>specific_latent_heat</name>
<type>Constant</type>
<value>2258000</value>
</property>
<property>
<name>vapour_pressure</name>
<type>ClausiusClapeyron</type>
<triple_temperature>273.16</triple_temperature>
<triple_pressure>611.66</triple_pressure>
<critical_temperature>647.096</critical_temperature>
<critical_pressure>22.064e6</critical_pressure>
<reference_temperature>373.15</reference_temperature>
<reference_pressure>101325</reference_pressure>
</property>
</properties>
</component>
<component>
<name>a</name>
<properties>
<property>
<name>molar_mass</name>
<type>Constant</type>
<value>0.02897</value>
</property>
<property>
<name>specific_heat_capacity</name>
<type>Constant</type>
<value>733</value>
</property>
</properties>
</component>
<component>
<name>c</name>
<properties>
<property>
<name>molar_mass</name>
<type>Constant</type>
<value>1.</value>
</property>
<property>
<name>pore_diffusion</name>
<type>Constant</type>
<value>1.</value>
</property>
<property>
<name>specific_heat_capacity</name>
<type>Constant</type>
<value>1.</value>
</property>
<property>
<name>henry_coefficient</name>
<type>Constant</type>
<value>1</value>
</property>
</properties>
</component>
</components>
<properties>
<property>
<name>viscosity</name>
<type>Constant</type>
<value>1.8e-5</value>
</property>
<property>
<name>density</name>
<type>IdealGasLaw</type>
</property>
</properties>
</phase>
<phase>
<type>AqueousLiquid</type>
<components>
<component>
<name>c</name>
<properties>
<property>
<name>pore_diffusion</name>
<type>Constant</type>
<value>1.</value>
</property>
</properties>
</component>
</components>
<properties>
<property>
<name>viscosity</name>
<type>Constant</type>
<value>2.938e-4</value>
</property>
<property>
<name>specific_heat_capacity</name>
<type>Constant</type>
<value>4187</value>
</property>
<property>
<name>density</name>
<type>Constant</type>
<value>1.e3</value>
</property>
</properties>
</phase>
<phase>
<type>Solid</type>
<properties>
<property>
<name>specific_heat_capacity</name>
<type>Constant</type>
<value>700</value>
</property>
<property>
<name>density</name>
<type>Constant</type>
<value>2650</value>
</property>
</properties>
</phase>
</phases>
<properties>
<property>
<name>porosity</name>
<type>Constant</type>
<value>0.4</value>
</property>
<property>
<name>permeability</name>
<type>Constant</type>
<value>1e-12</value>
</property>
<property>
<name>saturation</name>
<type>Curve</type>
<curve>saturation_curve</curve>
<independent_variable>capillary_pressure</independent_variable>
</property>
<property>
<name>relative_permeability</name>
<type>RelativePermeabilityUdell</type>
<residual_liquid_saturation>0.0</residual_liquid_saturation>
<residual_gas_saturation>0.0</residual_gas_saturation>
<min_relative_permeability>0.</min_relative_permeability>
</property>
<property>
<name>relative_permeability_nonwetting_phase</name>
<type>RelativePermeabilityUdellNonwettingPhase</type>
<residual_liquid_saturation>0.0</residual_liquid_saturation>
<residual_gas_saturation>0.0</residual_gas_saturation>
<min_relative_permeability>0.</min_relative_permeability>
</property>
<property>
<name>thermal_conductivity</name>
<type>SaturationWeightedThermalConductivity</type>
<mean_type>arithmetic_squareroot</mean_type>
<dry_thermal_conductivity>k_T_dry</dry_thermal_conductivity>
<wet_thermal_conductivity>k_T_wet</wet_thermal_conductivity>
</property>
<property>
<name>longitudinal_dispersivity</name>
<type>Constant</type>
<value>0</value>
</property>
<property>
<name>transversal_dispersivity</name>
<type>Constant</type>
<value>0</value>
</property>
</properties>
</medium>
</media>
<parameters>
<parameter>
<name>pc_Dirichlet_left</name>
<type>Constant</type>
<value>1.736416339569494e+03</value>
</parameter>
<parameter>
<name>T_Dirichlet_left</name>
<type>Constant</type>
<value>343</value>
</parameter>
<parameter>
<name>pg_Dirichlet_left</name>
<type>Constant</type>
<value>101934</value>
</parameter>
<parameter>
<name>Xc_0</name>
<type>Constant</type>
<values>0</values>
</parameter>
<parameter>
<name>T_0</name>
<type>Constant</type>
<values>343.15</values>
</parameter>
<parameter>
<name>pc_0</name>
<type>Constant</type>
<values>1.327316794077718e+04</values>
</parameter>
<parameter>
<name>pg_0</name>
<type>Constant</type>
<value>114578</value>
</parameter>
<parameter>
<name>T_neumann</name>
<type>Constant</type>
<value>100</value>
</parameter>
<parameter>
<name>k_T_dry</name>
<type>Constant</type>
<value>0.582</value>
</parameter>
<parameter>
<name>k_T_wet</name>
<type>Constant</type>
<value>1.14</value>
</parameter>
</parameters>
<time_loop>
<processes>
<process ref="TP23">
<nonlinear_solver>basic_newton</nonlinear_solver>
<convergence_criterion>
<type>DeltaX</type>
<norm_type>NORM2</norm_type>
<abstol>1.e-5</abstol>
</convergence_criterion>
<time_discretization>
<type>BackwardEuler</type>
</time_discretization>
<time_stepping>
<type>FixedTimeStepping</type>
<t_initial>0</t_initial>
<t_end>10000.0</t_end>
<timesteps>
<pair>
<repeat>1000</repeat>
<delta_t>100</delta_t>
</pair>
</timesteps>
</time_stepping>
</process>
</processes>
<output>
<type>VTK</type>
<prefix>thermaltwophaseflow_small</prefix>
<timesteps>
<pair>
<repeat>1</repeat>
<each_steps>500000</each_steps>
</pair>
</timesteps>
<output_iteration_results>false</output_iteration_results>
<variables>
<variable>capillary_pressure</variable>
<variable>gas_pressure</variable>
<variable>Xc</variable>
<variable>saturation</variable>
<variable>pressure_wetting</variable>
<variable>temperature</variable>
<variable>xwG</variable>
<variable>xcG</variable>
<variable>xcL</variable>
</variables>
<suffix>ts{:timestep}_t_{:time}</suffix>
</output>
</time_loop>
<process_variables>
<process_variable>
<name>gas_pressure</name>
<components>1</components>
<order>1</order>
<initial_condition>pg_0</initial_condition>
<boundary_conditions>
<boundary_condition>
<mesh>left</mesh>
<type>Dirichlet</type>
<parameter>pg_Dirichlet_left</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<process_variable>
<name>capillary_pressure</name>
<components>1</components>
<order>1</order>
<initial_condition>pc_0</initial_condition>
<boundary_conditions>
<boundary_condition>
<mesh>left</mesh>
<type>Dirichlet</type>
<parameter>pc_Dirichlet_left</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<process_variable>
<name>Xc</name>
<components>1</components>
<order>1</order>
<initial_condition>Xc_0</initial_condition>
<boundary_conditions>
<boundary_condition>
<mesh>HeatPipe_2D</mesh>
<type>Dirichlet</type>
<parameter>Xc_0</parameter>
</boundary_condition>
</boundary_conditions>
<source_terms />
</process_variable>
<process_variable>
<name>temperature</name>
<components>1</components>
<order>1</order>
<initial_condition>T_0</initial_condition>
<boundary_conditions>
<boundary_condition>
<mesh>left</mesh>
<type>Dirichlet</type>
<parameter>T_Dirichlet_left</parameter>
</boundary_condition>
<boundary_condition>
<mesh>right</mesh>
<type>Neumann</type>
<parameter>T_neumann</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
</process_variables>
<nonlinear_solvers>
<nonlinear_solver>
<name>basic_newton</name>
<type>Newton</type>
<max_iter>50</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-18 -maxiter 10000</lis>
<eigen>
<solver_type>BiCGSTAB</solver_type>
<precon_type>ILUT</precon_type>
<scaling>true</scaling>
<max_iteration_step>10000</max_iteration_step>
<error_tolerance>1e-18</error_tolerance>
</eigen>
<petsc>
<prefix>tp</prefix>
<parameters>-tp_ksp_type bicg -tp_pc_type bjacobi -tp_ksp_rtol 1e-12 -tp_ksp_max_it 10000</parameters>
</petsc>
</linear_solver>
</linear_solvers>
<curves>
<curve>
<name>saturation_curve</name>
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