OGS
excavation_th2m.prj
<
OpenGeoSysProject
>
<
meshes
>
<
mesh
>domain.vtu</mesh>
<
mesh
>left.vtu</mesh>
<
mesh
>right.vtu</mesh>
<
mesh
>top.vtu</mesh>
<
mesh
>bottom.vtu</mesh>
<
mesh
>arc.vtu</mesh>
</meshes>
<
processes
>
<
process
>
<
name
>TH2M</name>
<
type
>
TH2M
</type>
<
integration_order
>4</integration_order>
<constitutive_relation>
<type>
MFront
</type>
<
behaviour
>MohrCoulombAbboSloan</behaviour>
<
material_properties
>
<
material_property
name
="YoungModulus"
parameter
="E" />
<
material_property
name
="PoissonRatio"
parameter
="nu" />
<
material_property
name
="Cohesion"
parameter
="Cohesion" />
<
material_property
name
="FrictionAngle"
parameter
="FrictionAngle" />
<
material_property
name
="DilatancyAngle"
parameter
="DilatancyAngle" />
<
material_property
name
="TransitionAngle"
parameter
="TransitionAngle" />
<
material_property
name
="TensionCutOffParameter"
parameter
="TensionCutOffParameter" />
</material_properties>
</constitutive_relation>
<
jacobian_assembler
>
<
type
>
ForwardDifferences
</type>
<
epsilons
>0.01 0.01 1.0</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
="EquivalentPlasticStrain"
output_name
="epsilon_pls" />
<
secondary_variable
internal_name
="gas_density"
output_name
="gas_density" />
<
secondary_variable
internal_name
="saturation"
output_name
="saturation" />
<
secondary_variable
internal_name
="vapour_pressure"
output_name
="vapour_pressure" />
</secondary_variables>
<
specific_body_force
>0 0.0</specific_body_force>
<
mass_lumping
>true</mass_lumping>
<
initial_stress
type
="total">sigma0</initial_stress>
</process>
</processes>
<
time_loop
>
<
processes
>
<
process
ref
="TH2M">
<
nonlinear_solver
>basic_newton</nonlinear_solver>
<
convergence_criterion
>
<
type
>
PerComponentDeltaX
</type>
<
norm_type
>NORM2</norm_type>
<
abstols
>1.e-06 1.e-06 1.e-04 1.e-05 1.e-05</abstols>
<
reltols
>1.e-06 2.e-05 0.0 1.e-07 1.e-07</reltols>
</convergence_criterion>
<
time_discretization
>
<
type
>
BackwardEuler
</type>
</time_discretization>
<
time_stepping
>
<
type
>
IterationNumberBasedTimeStepping
</type>
<
t_initial
>0.0</t_initial>
<
t_end
>2.16e+5</t_end>
<
initial_dt
>10000</initial_dt>
<
minimum_dt
>1e1</minimum_dt>
<
maximum_dt
>2.16e+5</maximum_dt>
<
number_iterations
>1 4 10 15 20 25 31</number_iterations>
<
multiplier
>1.5 1.3 1.2 1.1 0.8 0.7 0.6</multiplier>
</time_stepping>
</process>
</processes>
<
output
>
<
type
>
VTK
</type>
<
prefix
>excavation_th2m_pls</prefix>
<
suffix
>
ts
{:gtime}</suffix>
<
timesteps
>
<
pair
>
<
repeat
>1</repeat>
<
each_steps
>1</each_steps>
</pair>
</timesteps>
<
variables
>
<
variable
>gas_pressure</variable>
<
variable
>capillary_pressure</variable>
<
variable
>temperature</variable>
<
variable
>displacement</variable>
<
variable
>sigma</variable>
<
variable
>epsilon</variable>
<
variable
>epsilon_pls</variable>
<
variable
>velocity_gas</variable>
<
variable
>velocity_liquid</variable>
<
variable
>liquid_density</variable>
<
variable
>gas_density</variable>
<
variable
>saturation</variable>
<
variable
>vapour_pressure</variable>
<
variable
>gas_pressure_interpolated</variable>
<
variable
>capillary_pressure_interpolated</variable>
<
variable
>liquid_pressure_interpolated</variable>
<
variable
>temperature_interpolated</variable>
<
variable
>MaterialIDs</variable>
</variables>
<
fixed_output_times
>31558
63115
94673
126230
157788
189346
220903
252461
284018
315576
631152
946728
1262304
1577880
1728000</fixed_output_times>
</output>
</time_loop>
<
media
>
<
medium
>
<
phases
>
<
phase
>
<
type
>
AqueousLiquid
</type>
<
components
>
<
component
>
<
name
>A</name>
<
properties
>
<property>
<name>specific_heat_capacity</name>
<type>
Constant
</type>
<value>733</value>
</property>
<property>
<name>henry_coefficient</name>
<type>
Constant
</type>
<value>7.600000000000001e-06</value>
</property>
<property>
<name>diffusion</name>
<type>
Constant
</type>
<value>4.5e-09</value>
</property>
<property>
<name>specific_latent_heat</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>W</name>
<
properties
>
<property>
<name>specific_heat_capacity</name>
<type>
Constant
</type>
<value>4187</value>
</property>
</properties>
</component>
</components>
<
properties
>
<
property
>
<
name
>thermal_conductivity</name>
<
type
>
Constant
</type>
<
value
>0.6</value>
</property>
<
property
>
<
name
>specific_heat_capacity</name>
<
type
>
Constant
</type>
<
value
>4187</value>
</property>
<
property
>
<
name
>density</name>
<
type
>
Linear
</type>
<
reference_value
>1000</reference_value>
<
independent_variable
>
<
variable_name
>liquid_phase_pressure</variable_name>
<
reference_condition
>1e5</reference_condition>
<
slope
>4.e-10</slope>
</independent_variable>
</property>
<
property
>
<
name
>viscosity</name>
<
type
>
Constant
</type>
<
value
>1.e-3</value>
</property>
</properties>
</phase>
<
phase
>
<
type
>
Gas
</type>
<
components
>
<
component
>
<
name
>A</name>
<
properties
>
<property>
<name>molar_mass</name>
<type>
Constant
</type>
<value>0.002016</value>
</property>
<property>
<name>specific_heat_capacity</name>
<type>
Constant
</type>
<value>733</value>
</property>
</properties>
</component>
<
component
>
<
name
>W</name>
<
properties
>
<property>
<name>molar_mass</name>
<type>
Constant
</type>
<value>0.0</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>
Constant
</type>
<value>0.0</value>
</property>
<property>
<name>diffusion</name>
<type>
Constant
</type>
<value>0.0</value>
</property>
</properties>
</component>
</components>
<
properties
>
<
property
>
<
name
>thermal_conductivity</name>
<
type
>
Constant
</type>
<
value
>0.6</value>
</property>
<
property
>
<
name
>density</name>
<
type
>
IdealGasLawBinaryMixture
</type>
</property>
<
property
>
<
name
>viscosity</name>
<
type
>
Constant
</type>
<
value
>9.e-6</value>
</property>
</properties>
</phase>
<
phase
>
<
type
>
Solid
</type>
<
properties
>
<
property
>
<
name
>density</name>
<
type
>
Constant
</type>
<
value
>2.e3</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
>0</value>
</property>
</properties>
</phase>
</phases>
<
properties
>
<
property
>
<
name
>permeability</name>
<
type
>
Constant
</type>
<
value
>1e-21</value>
</property>
<
property
>
<
name
>biot_coefficient</name>
<
type
>
Constant
</type>
<
value
>1.0</value>
</property>
<
property
>
<
name
>saturation</name>
<
type
>
SaturationVanGenuchten
</type>
<
residual_liquid_saturation
>0.01</residual_liquid_saturation>
<
residual_gas_saturation
>0.01</residual_gas_saturation>
<
p_b
>48000000.0</p_b>
<
exponent
>0.2</exponent>
</property>
<
property
>
<
name
>relative_permeability_nonwetting_phase</name>
<
type
>
RelativePermeabilityNonWettingPhaseVanGenuchtenMualem
</type>
<
residual_liquid_saturation
>0.6</residual_liquid_saturation>
<
residual_gas_saturation
>0.0</residual_gas_saturation>
<
exponent
>0.2</exponent>
<
min_relative_permeability
>1e-5</min_relative_permeability>
</property>
<
property
>
<
name
>relative_permeability</name>
<
type
>
RelativePermeabilityVanGenuchten
</type>
<
residual_liquid_saturation
>0.1</residual_liquid_saturation>
<
residual_gas_saturation
>0.1</residual_gas_saturation>
<
exponent
>0.2</exponent>
<
minimum_relative_permeability_liquid
>1e-12</minimum_relative_permeability_liquid>
</property>
<
property
>
<
name
>porosity</name>
<
type
>
Constant
</type>
<
value
>0.1</value>
</property>
<
property
>
<
name
>tortuosity</name>
<
type
>
Constant
</type>
<
value
>1</value>
</property>
<
property
>
<
name
>thermal_conductivity</name>
<
type
>
EffectiveThermalConductivityPorosityMixing
</type>
</property>
<
property
>
<
name
>bishops_effective_stress</name>
<
type
>
BishopsSaturationCutoff
</type>
<
cutoff_value
>0.99</cutoff_value>
</property>
</properties>
</medium>
</media>
<
parameters
>
<
parameter
>
<
name
>E</name>
<
type
>
Constant
</type>
<
value
>6.5e9</value>
</parameter>
<
parameter
>
<
name
>nu</name>
<
type
>
Constant
</type>
<
value
>.3</value>
</parameter>
<
parameter
>
<
name
>Cohesion</name>
<
type
>
Constant
</type>
<
value
>5.0e+6</value>
</parameter>
<
parameter
>
<
name
>FrictionAngle</name>
<
type
>
Constant
</type>
<
value
>25</value>
</parameter>
<
parameter
>
<
name
>DilatancyAngle</name>
<
type
>
Constant
</type>
<
value
>2.0</value>
</parameter>
<
parameter
>
<
name
>TransitionAngle</name>
<
type
>
Constant
</type>
<
value
>25.0</value>
</parameter>
<
parameter
>
<
name
>TensionCutOffParameter</name>
<
type
>
Constant
</type>
<
value
>0.5</value>
</parameter>
<
parameter
>
<
name
>zero</name>
<
type
>
Constant
</type>
<
value
>0.0</value>
</parameter>
<
parameter
>
<
name
>initial_displacement</name>
<
type
>
Constant
</type>
<
values
>0 0</values>
</parameter>
<
parameter
>
<
name
>sigma0</name>
<
type
>
Function
</type>
<
expression
>y*(14.3e+6-1e+5)
/
857-1e+5</expression>
<
expression
>y*(20.4e+6-1e+5)
/
857-1e+5</expression>
<
expression
>y*(22.4e+6-1e+5)
/
857-1e+5</expression>
<
expression
>0</expression>
</parameter>
<
parameter
>
<
name
>sigma_top</name>
<
type
>
Function
</type>
<
expression
>y*(20.4e+6-1e+5)
/
857-1e+5</expression>
</parameter>
<
parameter
>
<
name
>T0</name>
<
type
>
Constant
</type>
<
value
>300</value>
</parameter>
<
parameter
>
<
name
>pg_0_function</name>
<
type
>
Function
</type>
<
expression
>1e+5 - 1000 * 9.81 * y</expression>
</parameter>
<
parameter
>
<
name
>pc_0</name>
<
type
>
Constant
</type>
<
value
>1000</value>
</parameter>
<
parameter
>
<
name
>decay_function</name>
<
type
>
Function
</type>
<
expression
>if (t>1.728e+5) 0.0; else 1 - t
/
1.728e+5;</expression>
</parameter>
</parameters>
<
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
>initial_displacement</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>left</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>zero</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>bottom</mesh>
<
type
>
Dirichlet
</type>
<
component
>1</component>
<
parameter
>zero</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>top</mesh>
<
type
>
Neumann
</type>
<
component
>1</component>
<
parameter
>sigma_top</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>arc</mesh>
<
type
>
ReleaseNodalForce
</type>
<
time_decay_parameter
>decay_function</time_decay_parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>gas_pressure</name>
<
components
>1</components>
<
order
>1</order>
<
initial_condition
>pg_0_function</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>top</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>pg_0_function</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>arc</mesh>
<
type
>
TimeDecayDirichlet
</type>
<
component
>0</component>
<
time_decay_parameter
>decay_function</time_decay_parameter>
<
lower_limit
>1e+5</lower_limit>
</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
>top</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>pc_0</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>arc</mesh>
<
type
>
TimeDecayDirichlet
</type>
<
component
>0</component>
<
time_decay_parameter
>decay_function</time_decay_parameter>
<
lower_limit
>238501051.60885435</lower_limit>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>temperature</name>
<
components
>1</components>
<
order
>1</order>
<
initial_condition
>T0</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>domain</mesh>
<
type
>
Dirichlet
</type>
<
component
>0</component>
<
parameter
>T0</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
</process_variables>
<
nonlinear_solvers
>
<
nonlinear_solver
>
<
name
>basic_newton</name>
<
type
>
Newton
</type>
<
max_iter
>100</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
>true</scaling>
</eigen>
<
petsc
>
<
parameters
>-ksp_type bcgs
-pc_type lu -pc_factor_mat_solver_type mkl_pardiso</parameters>
</petsc>
</linear_solver>
</linear_solvers>
</OpenGeoSysProject>
OGS CTests—Project Files
TH2M
ExcavationTH2M
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