OGS
Strain_Dependent_Permeability_Test.prj
<
OpenGeoSysProject
>
<
meshes
>
<
mesh
axially_symmetric
="true">domain.vtu</mesh>
<
mesh
axially_symmetric
="true">boundary_bottom.vtu</mesh>
<
mesh
axially_symmetric
="true">boundary_top.vtu</mesh>
<
mesh
axially_symmetric
="true">boundary_right.vtu</mesh>
<
mesh
axially_symmetric
="true">boundary_left.vtu</mesh>
</meshes>
<
processes
>
<
process
>
<
name
>TH2M</name>
<
type
>
TH2M
</type>
<
integration_order
>4</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
="solid_density"
output_name
="solid_density" />
<
secondary_variable
internal_name
="vapour_pressure"
output_name
="vapour_pressure" />
<
secondary_variable
internal_name
="porosity"
output_name
="porosity" />
<
secondary_variable
internal_name
="saturation"
output_name
="saturation" />
<
secondary_variable
internal_name
="mole_fraction_gas"
output_name
="xnCG" />
<
secondary_variable
internal_name
="mass_fraction_gas"
output_name
="xmCG" />
<
secondary_variable
internal_name
="mass_fraction_liquid"
output_name
="xmWL" />
<
secondary_variable
internal_name
="relative_permeability_gas"
output_name
="k_rel_G" />
<
secondary_variable
internal_name
="relative_permeability_liquid"
output_name
="k_rel_L" />
</secondary_variables>
<
mass_lumping
>false</mass_lumping>
<
specific_body_force
>0 0</specific_body_force>
<
initial_stress
>initial_stress</initial_stress>
</process>
</processes>
<
media
>
<
medium
id
="0">
<
phases
>
<
phase
>
<
type
>
Gas
</type>
<
properties
>
<
property
>
<
name
>specific_heat_capacity</name>
<
type
>
Constant
</type>
<
value
>4000</value>
</property>
<
property
>
<
name
>thermal_conductivity</name>
<
type
>
Constant
</type>
<
value
>.5</value>
</property>
<
property
>
<
name
>molar_mass</name>
<
type
>
Constant
</type>
<
value
>.0285</value>
</property>
<
property
>
<
name
>density</name>
<
type
>
IdealGasLaw
</type>
</property>
<
property
>
<
name
>thermal_expansivity</name>
<
type
>
Constant
</type>
<
value
>0.0</value>
</property>
<
property
>
<
name
>viscosity</name>
<
type
>
Constant
</type>
<
value
>1.6e-5</value>
</property>
</properties>
</phase>
<
phase
>
<
type
>
AqueousLiquid
</type>
<
properties
>
<
property
>
<
name
>specific_heat_capacity</name>
<
type
>
Constant
</type>
<
value
>4000.0</value>
</property>
<
property
>
<
name
>thermal_conductivity</name>
<
type
>
Constant
</type>
<
value
>.5</value>
</property>
<
property
>
<
name
>density</name>
<
type
>
Constant
</type>
<
value
>1000</value>
</property>
<
property
>
<
name
>thermal_expansivity</name>
<
type
>
Constant
</type>
<
value
>1.0e-6</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
>2500.0</value>
</property>
<
property
>
<
name
>thermal_conductivity</name>
<
type
>
Constant
</type>
<
value
>5</value>
</property>
<
property
>
<
name
>specific_heat_capacity</name>
<
type
>
Constant
</type>
<
value
>14</value>
</property>
<
property
>
<
name
>thermal_expansivity</name>
<
type
>
Constant
</type>
<
value
>1.0e-8</value>
</property>
</properties>
</phase>
</phases>
<
properties
>
<
property
>
<
name
>permeability</name>
<
type
>
StrainDependentPermeability
</type>
<
initial_permeability
>permeability0</initial_permeability>
<
b1
>4000.0</b1>
<
b2
>300.0</b2>
<
b3
>50.0</b3>
<
minimum_permeability
>1.e-20</minimum_permeability>
<
maximum_permeability
>1.e-12</maximum_permeability>
</property>
<
property
>
<
name
>biot_coefficient</name>
<
type
>
Constant
</type>
<
value
>1.0</value>
</property>
<
property
>
<
name
>saturation</name>
<
type
>
SaturationVanGenuchten
</type>
<
residual_liquid_saturation
>0.1</residual_liquid_saturation>
<
residual_gas_saturation
>0.01</residual_gas_saturation>
<
exponent
>0.5</exponent>
<
p_b
>9.0e04</p_b>
</property>
<
property
>
<
name
>relative_permeability_nonwetting_phase</name>
<
type
>
Constant
</type>
<
value
>1.0</value>
</property>
<
property
>
<
name
>relative_permeability</name>
<
type
>
Constant
</type>
<
value
>1.0</value>
</property>
<
property
>
<
name
>porosity</name>
<
type
>
Constant
</type>
<
value
>0.2</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-6 1e-6 1e-6 1e-6 1e-6</abstols>
</convergence_criterion>
<
time_discretization
>
<
type
>
BackwardEuler
</type>
</time_discretization>
<
time_stepping
>
<
type
>
FixedTimeStepping
</type>
<
t_initial
>0</t_initial>
<
t_end
>10000</t_end>
<
timesteps
>
<
pair
>
<
repeat
>6</repeat>
<
delta_t
>5</delta_t>
</pair>
<
pair
>
<
repeat
>7</repeat>
<
delta_t
>10</delta_t>
</pair>
<
pair
>
<
repeat
>8</repeat>
<
delta_t
>25</delta_t>
</pair>
<
pair
>
<
repeat
>14</repeat>
<
delta_t
>50</delta_t>
</pair>
<
pair
>
<
repeat
>10</repeat>
<
delta_t
>100</delta_t>
</pair>
<
pair
>
<
repeat
>10</repeat>
<
delta_t
>300</delta_t>
</pair>
<
pair
>
<
repeat
>6</repeat>
<
delta_t
>5</delta_t>
</pair>
<
pair
>
<
repeat
>7</repeat>
<
delta_t
>10</delta_t>
</pair>
<
pair
>
<
repeat
>8</repeat>
<
delta_t
>25</delta_t>
</pair>
<
pair
>
<
repeat
>14</repeat>
<
delta_t
>50</delta_t>
</pair>
<
pair
>
<
repeat
>10</repeat>
<
delta_t
>100</delta_t>
</pair>
<
pair
>
<
repeat
>10</repeat>
<
delta_t
>300</delta_t>
</pair>
</timesteps>
</time_stepping>
</process>
</processes>
<
output
>
<
type
>
VTK
</type>
<
prefix
>IfG</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
>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_pressure</variable>
<
variable
>liquid_pressure_interpolated</variable>
<
variable
>liquid_density</variable>
<
variable
>gas_density</variable>
<
variable
>porosity</variable>
<
variable
>saturation</variable>
</variables>
</output>
</time_loop>
<
parameters
>
<
parameter
>
<
name
>permeability0</name>
<
type
>
Constant
</type>
<
value
>1.0e-17</value>
</parameter>
<
parameter
>
<
name
>E</name>
<
type
>
Constant
</type>
<
value
>2.5e09</value>
</parameter>
<
parameter
>
<
name
>initial_stress</name>
<
type
>
Function
</type>
<
expression
>0</expression>
<
expression
>-((1-0.2975)*2.e3+0.2975*1.e3)*9.806*(1.-y) + 101325</expression>
<
expression
>0</expression>
<
expression
>0</expression>
</parameter>
<
parameter
>
<
name
>nu</name>
<
type
>
Constant
</type>
<
value
>0.3</value>
</parameter>
<
parameter
>
<
name
>T0</name>
<
type
>
Constant
</type>
<
value
>293.15</value>
</parameter>
<
parameter
>
<
name
>one</name>
<
type
>
Constant
</type>
<
value
>1.0</value>
</parameter>
<
parameter
>
<
name
>zero</name>
<
type
>
Constant
</type>
<
value
>0.0</value>
</parameter>
<
parameter
>
<
name
>pGR_ic</name>
<
type
>
Constant
</type>
<
value
>0.1013e06</value>
</parameter>
<
parameter
>
<
name
>pCap_ic</name>
<
type
>
Constant
</type>
<
value
>206166.80631</value>
</parameter>
<
parameter
>
<
name
>T_ic</name>
<
type
>
Constant
</type>
<
value
>293.15</value>
</parameter>
<
parameter
>
<
name
>displacement0</name>
<
type
>
Constant
</type>
<
values
>0 0</values>
</parameter>
<
parameter
>
<
name
>pGR_bottom</name>
<
type
>
Constant
</type>
<
value
>0.5e06</value>
</parameter>
<
parameter
>
<
name
>stressRamp</name>
<
type
>
CurveScaled
</type>
<
curve
>time_ramp_stress</curve>
<
parameter
>one</parameter>
</parameter>
</parameters>
<
curves
>
<
curve
>
<
name
>time_ramp_stress</name>
<coords>0 100 5000 5100 10000</coords>
<values>0.0 2e06 2e06 -2e06 -2e06</values>
</curve>
</curves>
<
process_variables
>
<
process_variable
>
<
name
>displacement</name>
<
components
>2</components>
<
order
>2</order>
<
compensate_non_equilibrium_initial_residuum
>true</compensate_non_equilibrium_initial_residuum>
<
initial_condition
>displacement0</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>boundary_left</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>zero</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>boundary_top</mesh>
<
type
>
Dirichlet
</type>
<
component
>1</component>
<
parameter
>zero</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>boundary_bottom</mesh>
<
type
>
Dirichlet
</type>
<
component
>1</component>
<
parameter
>zero</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>boundary_right</mesh>
<
type
>
Neumann
</type>
<
component
>0</component>
<
parameter
>stressRamp</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>gas_pressure</name>
<
components
>1</components>
<
order
>1</order>
<
compensate_non_equilibrium_initial_residuum
>true</compensate_non_equilibrium_initial_residuum>
<
initial_condition
>pGR_ic</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>boundary_bottom</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>pGR_bottom</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>boundary_top</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>pGR_ic</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>capillary_pressure</name>
<
components
>1</components>
<
order
>1</order>
<
compensate_non_equilibrium_initial_residuum
>true</compensate_non_equilibrium_initial_residuum>
<
initial_condition
>pCap_ic</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>boundary_top</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>pCap_ic</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>temperature</name>
<
components
>1</components>
<
order
>1</order>
<
compensate_non_equilibrium_initial_residuum
>true</compensate_non_equilibrium_initial_residuum>
<
initial_condition
>T_ic</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>domain</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>T_ic</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-14 -maxiter 10000</lis>
<
eigen
>
<
solver_type
>BiCGSTAB</solver_type>
<
precon_type
>ILUT</precon_type>
<
max_iteration_step
>5000</max_iteration_step>
<
error_tolerance
>1e-18</error_tolerance>
</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
H2M
StrainDependentPermeability
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