OGS
TwoPhase_mcwt_line.prj
<
OpenGeoSysProject
>
<
mesh
>mcwt.vtu</mesh>
<
geometry
>mcwt.gml</geometry>
<
processes
>
<
process
>
<
name
>GW23</name>
<
type
>
TWOPHASE_FLOW_PP
</type>
<
integration_order
>2</integration_order>
<
jacobian_assembler
>
<
type
>
CentralDifferences
</type>
<
component_magnitudes
>1e4 1e+5</component_magnitudes>
<
relative_epsilons
>1e-7 1e-7</relative_epsilons>
</jacobian_assembler>
<
process_variables
>
<
capillary_pressure
>capillary_pressure</capillary_pressure>
<
gas_pressure
>gas_pressure</gas_pressure>
</process_variables>
<
secondary_variables
>
<
secondary_variable
internal_name
="saturation"
output_name
="saturation" />
</secondary_variables>
<
specific_body_force
>0 0</specific_body_force>
<
mass_lumping
>true</mass_lumping>
<
temperature
>temp</temperature>
</process>
</processes>
<
media
>
<
medium
id
="0">
<
phases
>
<
phase
>
<
type
>
AqueousLiquid
</type>
<
properties
>
<
property
>
<
name
>density</name>
<
type
>
Constant
</type>
<
value
>1.0e3</value>
</property>
<
property
>
<
name
>viscosity</name>
<
type
>
Constant
</type>
<
value
>1e-3</value>
</property>
</properties>
</phase>
<
phase
>
<
type
>
Gas
</type>
<
properties
>
<
property
>
<
name
>density</name>
<
type
>
Constant
</type>
<
value
>1.0e3</value>
</property>
<
property
>
<
name
>viscosity</name>
<
type
>
Constant
</type>
<
value
>1.e-3</value>
</property>
<
property
>
<
name
>molar_mass</name>
<
type
>
Constant
</type>
<
value
>0.0289</value>
</property>
</properties>
</phase>
</phases>
<
properties
>
<
property
>
<
name
>permeability</name>
<
type
>
Constant
</type>
<
value
>1.0e-10</value>
</property>
<
property
>
<
name
>saturation</name>
<
type
>
SaturationBrooksCorey
</type>
<
residual_liquid_saturation
>0.0</residual_liquid_saturation>
<
residual_gas_saturation
>0.0</residual_gas_saturation>
<
lambda
>2.0</lambda>
<
entry_pressure
>5000</entry_pressure>
</property>
<
property
>
<
name
>relative_permeability</name>
<
type
>
RelPermBrooksCorey
</type>
<
residual_liquid_saturation
>0.0</residual_liquid_saturation>
<
residual_gas_saturation
>0.0</residual_gas_saturation>
<
lambda
>2</lambda>
<
min_relative_permeability
>0</min_relative_permeability>
</property>
<
property
>
<
name
>relative_permeability_nonwetting_phase</name>
<
type
>
RelPermBrooksCoreyNonwettingPhase
</type>
<
residual_liquid_saturation
>0.0</residual_liquid_saturation>
<
residual_gas_saturation
>0.0</residual_gas_saturation>
<
lambda
>2</lambda>
<
min_relative_permeability
>1e-9</min_relative_permeability>
</property>
<
property
>
<
name
>porosity</name>
<
type
>
Constant
</type>
<
value
>0.3</value>
</property>
</properties>
</medium>
</media>
<
parameters
>
<
parameter
>
<
name
>pc_Dirichlet_left</name>
<
type
>
Constant
</type>
<
value
>5000.0</value>
</parameter>
<
parameter
>
<
name
>pg_Dirichlet_left</name>
<
type
>
Constant
</type>
<
value
>2.e5</value>
</parameter>
<
parameter
>
<
name
>pc_0</name>
<
type
>
Constant
</type>
<
values
>5.e4</values>
</parameter>
<
parameter
>
<
name
>pg_0</name>
<
type
>
Constant
</type>
<
values
>0.0</values>
</parameter>
<
parameter
>
<
name
>temp</name>
<
type
>
Constant
</type>
<
value
>293.15</value>
</parameter>
<
parameter
>
<
name
>constant_porosity_parameter</name>
<
type
>
Constant
</type>
<
value
>0.3</value>
</parameter>
<
parameter
>
<
name
>kappa1</name>
<
type
>
Constant
</type>
<
values
>1.0e-10</values>
</parameter>
</parameters>
<
time_loop
>
<
processes
>
<
process
ref
="GW23">
<
nonlinear_solver
>basic_newton</nonlinear_solver>
<
convergence_criterion
>
<
type
>
PerComponentDeltaX
</type>
<
norm_type
>NORM2</norm_type>
<
abstols
>1e-05 1e-05</abstols>
<
reltols
>1e-08 1e-08</reltols>
</convergence_criterion>
<
time_discretization
>
<
type
>
BackwardEuler
</type>
</time_discretization>
<
time_stepping
>
<
type
>
FixedTimeStepping
</type>
<
t_initial
>0</t_initial>
<
t_end
>1000</t_end>
<
timesteps
>
<
pair
>
<
repeat
>100</repeat>
<
delta_t
>0.05</delta_t>
</pair>
<
pair
>
<
repeat
>100</repeat>
<
delta_t
>0.1</delta_t>
</pair>
<
pair
>
<
repeat
>100</repeat>
<
delta_t
>0.5</delta_t>
</pair>
<
pair
>
<
repeat
>100</repeat>
<
delta_t
>1</delta_t>
</pair>
<
pair
>
<
repeat
>100</repeat>
<
delta_t
>2</delta_t>
</pair>
<
pair
>
<
repeat
>100</repeat>
<
delta_t
>5</delta_t>
</pair>
</timesteps>
</time_stepping>
</process>
</processes>
<
output
>
<
type
>
VTK
</type>
<
prefix
>twophaseflow</prefix>
<
timesteps
>
<
pair
>
<
repeat
>1</repeat>
<
each_steps
>10000</each_steps>
</pair>
</timesteps>
<
output_iteration_results
>false</output_iteration_results>
<
variables
>
<
variable
>capillary_pressure</variable>
<
variable
>gas_pressure</variable>
<
variable
>saturation</variable>
</variables>
<
suffix
>
ts
{:timestep}_t_{:time}</suffix>
</output>
</time_loop>
<
process_variables
>
<
process_variable
>
<
name
>capillary_pressure</name>
<
components
>1</components>
<
order
>1</order>
<
initial_condition
>pc_0</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
geometrical_set
>mcwt</geometrical_set>
<
geometry
>POINT0</geometry>
<
type
>
Dirichlet
</type>
<
parameter
>pc_Dirichlet_left</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>gas_pressure</name>
<
components
>1</components>
<
order
>1</order>
<
initial_condition
>pg_0</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
geometrical_set
>mcwt</geometrical_set>
<
geometry
>POINT0</geometry>
<
type
>
Dirichlet
</type>
<
parameter
>pg_Dirichlet_left</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
</process_variables>
<
nonlinear_solvers
>
<
nonlinear_solver
>
<
name
>basic_newton</name>
<
type
>
Newton
</type>
<
max_iter
>60</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 ilut -tol 1e-18 -maxiter 10000</lis>
<
eigen
>
<
solver_type
>BiCGSTAB</solver_type>
<
precon_type
>ILUT</precon_type>
<
max_iteration_step
>10000</max_iteration_step>
<
error_tolerance
>1e-18</error_tolerance>
</eigen>
</linear_solver>
</linear_solvers>
</OpenGeoSysProject>
OGS CTests—Project Files
Parabolic
TwoPhaseFlowPP
McWhorter
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