OGS
base.prj
<
OpenGeoSysProject
>
<
meshes
>
<
mesh
axially_symmetric
="false">domain.vtu</mesh>
<
mesh
axially_symmetric
="false">surface_x_min.vtu</mesh>
<
mesh
axially_symmetric
="false">surface_x_max.vtu</mesh>
<
mesh
axially_symmetric
="false">surface_y_min.vtu</mesh>
<
mesh
axially_symmetric
="false">submesh_0.vtu</mesh>
<
mesh
axially_symmetric
="false">submesh_1.vtu</mesh>
<
mesh
axially_symmetric
="false">submesh_2.vtu</mesh>
<
mesh
axially_symmetric
="false">submesh_3.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
>1e5 1e5 1e5 1e5
1e5 1e5 1e5 1e5
1e2 1e2 1e2 1e2
1e-2 1e-2 1e-2 1e-2
1e-2 1e-2 1e-2 1e-2
1e-2 1e-2 1e-2 1e-2
1e-2 1e-2 1e-2 1e-2</component_magnitudes>
<
relative_epsilons
>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
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
>temperature_ic</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
name="velocity_gas" />
<
secondary_variable
name="velocity_liquid" />
<
secondary_variable
name="sigma" />
<
secondary_variable
name="epsilon" />
<
secondary_variable
name="liquid_density" />
<
secondary_variable
name="gas_density" />
<
secondary_variable
name="porosity" />
<
secondary_variable
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
>4019.0</value>
</property>
<
property
>
<
name
>thermal_conductivity</name>
<
type
>
Constant
</type>
<
value
>1</value>
</property>
<
property
>
<
name
>density</name>
<
type
>
Constant
</type>
<
value
>1000</value>
</property>
<
property
>
<
name
>molar_mass</name>
<
type
>
Constant
</type>
<
value
>0.018</value>
</property>
<
property
>
<
name
>thermal_expansivity</name>
<
type
>
Constant
</type>
<
value
>0.2</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
>
Constant
</type>
<
value
>1</value>
</property>
<
property
>
<
name
>viscosity</name>
<
type
>
Constant
</type>
<
value
>1.e-5</value>
</property>
</properties>
</phase>
<
phase
>
<
type
>
Solid
</type>
<
properties
>
<
property
>
<
name
>density</name>
<
type
>
Constant
</type>
<
value
>2e3</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
>1.e-12</value>
</property>
<
property
>
<
name
>biot_coefficient</name>
<
type
>
Constant
</type>
<
value
>1.0</value>
</property>
<
property
>
<
name
>saturation</name>
<
type
>
Constant
</type>
<
value
>0.5</value>
</property>
<
property
>
<
name
>relative_permeability</name>
<
type
>
Constant
</type>
<
value
>1</value>
</property>
<
property
>
<
name
>relative_permeability_nonwetting_phase</name>
<
type
>
Constant
</type>
<
value
>1</value>
</property>
<
property
>
<
name
>thermal_conductivity</name>
<
type
>
EffectiveThermalConductivityPorosityMixing
</type>
</property>
<
property
>
<
name
>porosity</name>
<
type
>
Constant
</type>
<
value
>0.4</value>
</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
>INFINITY_N</norm_type>
<
abstols
>1e-10 1e-9 1e-16 1e-16 1e-16</abstols>
</convergence_criterion>
<
time_discretization
>
<
type
>
BackwardEuler
</type>
</time_discretization>
<
time_stepping
>
<
type
>
FixedTimeStepping
</type>
<
t_initial
>0</t_initial>
<
t_end
>4</t_end>
<
timesteps
>
<
pair
>
<
repeat
>1</repeat>
<
delta_t
>1</delta_t>
</pair>
</timesteps>
</time_stepping>
</process>
</processes>
<
output
>
<
type
>
VTK
</type>
<
timesteps
>
<
pair
>
<
repeat
>1</repeat>
<
each_steps
>1</each_steps>
</pair>
</timesteps>
<
variables
>
<
variable
>gas_pressure_interpolated</variable>
<
variable
>capillary_pressure_interpolated</variable>
<
variable
>temperature_interpolated</variable>
<
variable
>displacement</variable>
<
variable
>liquid_pressure_interpolated</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>
<
submesh_residuum_output
>
<type>
VTK
</type>
<timesteps>
<pair>
<repeat>1</repeat>
<each_steps>1</each_steps>
</pair>
</timesteps>
<variables>
<variable>gas_pressure_interpolated</variable>
<variable>capillary_pressure_interpolated</variable>
<variable>temperature_interpolated</variable>
<variable>displacement</variable>
<variable>liquid_pressure_interpolated</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>
<meshes>
<mesh>submesh_0</mesh>
<mesh>submesh_1</mesh>
<mesh>submesh_2</mesh>
<mesh>submesh_3</mesh>
</meshes>
</submesh_residuum_output>
</time_loop>
<
parameters
>
<
parameter
>
<
name
>E</name>
<
type
>
Constant
</type>
<
value
>1e9</value>
</parameter>
<
parameter
>
<
name
>nu</name>
<
type
>
Constant
</type>
<
value
>0.1</value>
</parameter>
<
parameter
>
<
name
>displacement0</name>
<
type
>
Constant
</type>
<
values
>0 0</values>
</parameter>
<
parameter
>
<
name
>zero</name>
<
type
>
Constant
</type>
<
value
>0</value>
</parameter>
<
parameter
>
<
name
>temperature_ic</name>
<
type
>
Constant
</type>
<
value
>0</value>
</parameter>
</parameters>
<
process_variables
>
<
process_variable
>
<
name
>displacement</name>
<
components
>2</components>
<
order
>2</order>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>surface_y_min</mesh>
<
type
>
Dirichlet
</type>
<
component
>1</component>
<
parameter
>zero</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>surface_x_min</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>zero</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>gas_pressure</name>
<
components
>1</components>
<
order
>1</order>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>surface_x_min</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>zero</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>capillary_pressure</name>
<
components
>1</components>
<
order
>1</order>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>surface_x_min</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>zero</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>temperature</name>
<
components
>1</components>
<
order
>1</order>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>surface_x_min</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>zero</parameter>
</boundary_condition>
</boundary_conditions>
</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>
OGS CTests—Project Files
TH2M
submesh_residuum_assembly
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