OGS
TRuni_unsaturated.prj
<
OpenGeoSysProject
>
<
meshes
>
<
mesh
>single_cube_bulk.vtu</mesh>
<
mesh
>single_cube_x0_surface.vtu</mesh>
<
mesh
>single_cube_x10_surface.vtu</mesh>
<
mesh
>single_cube_y0_surface.vtu</mesh>
<
mesh
>single_cube_y10_surface.vtu</mesh>
<
mesh
>single_cube_z0_surface.vtu</mesh>
<
mesh
>single_cube_z10_surface.vtu</mesh>
</meshes>
<
processes
>
<
process
>
<
name
>TRF</name>
<
type
>
THERMO_RICHARDS_FLOW
</type>
<
integration_order
>4</integration_order>
<
process_variables
>
<
pressure
>pressure</pressure>
<
temperature
>temperature</temperature>
</process_variables>
<
secondary_variables
>
<
secondary_variable
internal_name
="velocity"
output_name
="velocity" />
<
secondary_variable
internal_name
="saturation"
output_name
="saturation" />
</secondary_variables>
<
specific_body_force
>0 0 0</specific_body_force>
<
simplified_elasticity
>uniaxial</simplified_elasticity>
</process>
</processes>
<
media
>
<
medium
id
="0">
<
phases
>
<
phase
>
<
type
>
AqueousLiquid
</type>
<
properties
>
<
property
>
<
name
>specific_heat_capacity</name>
<
type
>
Constant
</type>
<
value
>4065.12</value>
</property>
<
property
>
<
name
>thermal_conductivity</name>
<
type
>
Constant
</type>
<
value
>0.63</value>
</property>
<
property
>
<
name
>density</name>
<
type
>
Linear
</type>
<
reference_value
>999.1</reference_value>
<
independent_variable
>
<
variable_name
>temperature</variable_name>
<
reference_condition
>293.15</reference_condition>
<
slope
>-3.98e-4</slope>
</independent_variable>
<
independent_variable
>
<
variable_name
>liquid_phase_pressure</variable_name>
<
reference_condition
>1e5</reference_condition>
<
slope
>4.5999999999999996e-10</slope>
</independent_variable>
</property>
<
property
>
<
name
>thermal_expansivity</name>
<
type
>
Constant
</type>
<
value
>3.98e-4</value>
</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
>2768.5</value>
</property>
<
property
>
<
name
>thermal_conductivity</name>
<
type
>
Constant
</type>
<
value
>1.7</value>
</property>
<
property
>
<
name
>specific_heat_capacity</name>
<
type
>
Constant
</type>
<
value
>860.0</value>
</property>
<
property
>
<
name
>thermal_expansivity</name>
<
type
>
Constant
</type>
<
value
>1.4e-6</value>
</property>
<
property
>
<
name
>youngs_modulus</name>
<
type
>
Constant
</type>
<
value
>2.7e9</value>
</property>
<
property
>
<
name
>poissons_ratio</name>
<
type
>
Constant
</type>
<
value
>0.33</value>
</property>
</properties>
</phase>
</phases>
<
properties
>
<
property
>
<
name
>permeability</name>
<
type
>
Constant
</type>
<
value
>3e-20 0 0 0 3e-20 0 0 0 3e-20</value>
</property>
<
property
>
<
name
>biot_coefficient</name>
<
type
>
Constant
</type>
<
value
>0.3</value>
</property>
<
property
>
<
name
>porosity</name>
<
type
>
Constant
</type>
<
value
>0.183</value>
</property>
<
property
>
<
name
>relative_permeability</name>
<
type
>
RelativePermeabilityVanGenuchten
</type>
<
residual_liquid_saturation
>0.1689</residual_liquid_saturation>
<
residual_gas_saturation
>0.05</residual_gas_saturation>
<
exponent
>0.789029535864979</exponent>
<
minimum_relative_permeability_liquid
>1e-12</minimum_relative_permeability_liquid>
</property>
<
property
>
<
name
>saturation</name>
<
type
>
SaturationVanGenuchten
</type>
<
residual_liquid_saturation
>0.1689</residual_liquid_saturation>
<
residual_gas_saturation
>0.05</residual_gas_saturation>
<
exponent
>0.789029535864979</exponent>
<
p_b
>3633.33</p_b>
</property>
<
property
>
<
name
>thermal_conductivity</name>
<
type
>
EffectiveThermalConductivityPorosityMixing
</type>
</property>
</properties>
</medium>
</media>
<
time_loop
>
<
processes
>
<
process
ref
="TRF">
<
nonlinear_solver
>basic_newton</nonlinear_solver>
<
convergence_criterion
>
<
type
>
PerComponentDeltaX
</type>
<
norm_type
>NORM2</norm_type>
<
abstols
>1e-5 1e-2</abstols>
</convergence_criterion>
<
time_discretization
>
<
type
>
BackwardEuler
</type>
</time_discretization>
<
time_stepping
>
<
type
>
FixedTimeStepping
</type>
<
t_initial
>0</t_initial>
<
t_end
>1</t_end>
<
timesteps
>
<
pair
>
<
repeat
>10</repeat>
<
delta_t
>0.1</delta_t>
</pair>
</timesteps>
</time_stepping>
</process>
</processes>
<
output
>
<
type
>
VTK
</type>
<
prefix
>TRuni_unsat</prefix>
<
timesteps
>
<
pair
>
<
repeat
>100</repeat>
<
each_steps
>1</each_steps>
</pair>
</timesteps>
<
variables
>
<
variable
>pressure</variable>
<
variable
>temperature</variable>
<
variable
>velocity</variable>
<
variable
>saturation</variable>
</variables>
</output>
</time_loop>
<
parameters
>
<
parameter
>
<
name
>E</name>
<
type
>
Constant
</type>
<
value
>2.7e9</value>
</parameter>
<
parameter
>
<
name
>nu</name>
<
type
>
Constant
</type>
<
value
>0.33</value>
</parameter>
<
parameter
>
<
name
>displacement0</name>
<
type
>
Constant
</type>
<
values
>0 0 0</values>
</parameter>
<
parameter
>
<
name
>pressure_ic</name>
<
type
>
Constant
</type>
<
values
>-1.e4</values>
</parameter>
<
parameter
>
<
name
>dirichlet0</name>
<
type
>
Constant
</type>
<
value
>0</value>
</parameter>
<
parameter
>
<
name
>neumann0</name>
<
type
>
Constant
</type>
<
value
>0</value>
</parameter>
<
parameter
>
<
name
>pressure_bc_left</name>
<
type
>
Constant
</type>
<
value
>0</value>
</parameter>
<
parameter
>
<
name
>temperature0</name>
<
type
>
Constant
</type>
<
value
>293.15</value>
</parameter>
<
parameter
>
<
name
>Tvalue</name>
<
type
>
Constant
</type>
<
value
>293.15</value>
</parameter>
<
parameter
>
<
name
>temperature1</name>
<
type
>
CurveScaled
</type>
<
parameter
>Tvalue</parameter>
<
curve
>Tcurve</curve>
</parameter>
</parameters>
<
curves
>
<
curve
>
<
name
>Tcurve</name>
<coords>0 1</coords>
<values>1 1.5</values>
</curve>
</curves>
<
process_variables
>
<
process_variable
>
<
name
>pressure</name>
<
components
>1</components>
<
order
>1</order>
<
initial_condition
>pressure_ic</initial_condition>
<
boundary_conditions
/>
</process_variable>
<
process_variable
>
<
name
>temperature</name>
<
components
>1</components>
<
order
>1</order>
<
initial_condition
>temperature0</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>single_cube_x10_surface</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>temperature1</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>single_cube_y10_surface</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>temperature1</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>single_cube_z10_surface</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>temperature1</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>single_cube_x0_surface</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>temperature1</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>single_cube_y0_surface</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>temperature1</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>single_cube_z0_surface</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>temperature1</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>
<
eigen
>
<
solver_type
>SparseLU</solver_type>
<
scaling
>1</scaling>
</eigen>
<
petsc
>
<
parameters
>-ksp_type bcgs
-pc_type jacobi
-ksp_rtol 1.e-14 -ksp_atol 1.e-14
-ksp_max_it 4000</parameters>
</petsc>
</linear_solver>
</linear_solvers>
</OpenGeoSysProject>
OGS CTests—Project Files
ThermoRichardsFlow
SimplifiedMechanics
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