OGS
Padilla_NaCl6.prj
<
OpenGeoSysProject
>
<
mesh
>Padilla_NaCl6.vtu</mesh>
<
geometry
>Padilla.gml</geometry>
<
processes
>
<
process
>
<
name
>HusC</name>
<
type
>
RichardsComponentTransport
</type>
<
integration_order
>2</integration_order>
<
process_variables
>
<
concentration
>concentration</concentration>
<
pressure
>pressure</pressure>
</process_variables>
<
specific_body_force
>-9.81</specific_body_force>
<
secondary_variables
>
<
secondary_variable
internal_name
="saturation"
output_name
="saturation" />
<
secondary_variable
internal_name
="darcy_velocity"
output_name
="darcy_velocity" />
</secondary_variables>
</process>
</processes>
<
media
>
<
medium
id
="0">
<
phases
>
<
phase
>
<
type
>
AqueousLiquid
</type>
<
components
>
<
component
>
<
name
>concentration</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Parameter
</type>
<parameter_name>Dm</parameter_name>
</property>
<property>
<name>retardation_factor</name>
<type>
Parameter
</type>
<parameter_name>retardation_factor</parameter_name>
</property>
<property>
<name>decay_rate</name>
<type>
Parameter
</type>
<parameter_name>decay_rate</parameter_name>
</property>
</properties>
</component>
</components>
<
properties
>
<
property
>
<
name
>density</name>
<
type
>
Constant
</type>
<
value
>1e3</value>
</property>
<
property
>
<
name
>viscosity</name>
<
type
>
Constant
</type>
<
value
>1e-3</value>
</property>
</properties>
</phase>
</phases>
<
properties
>
<
property
>
<
name
>permeability</name>
<
type
>
Parameter
</type>
<
parameter_name
>kappa1</parameter_name>
</property>
<
property
>
<
name
>porosity</name>
<
type
>
Parameter
</type>
<
parameter_name
>constant_porosity_parameter</parameter_name>
</property>
<
property
>
<
name
>storage</name>
<
type
>
Constant
</type>
<
value
>0</value>
</property>
<
property
>
<
name
>capillary_pressure</name>
<
type
>
CapillaryPressureVanGenuchten
</type>
<
residual_liquid_saturation
>0.1689</residual_liquid_saturation>
<
residual_gas_saturation
>0</residual_gas_saturation>
<
exponent
>0.789029535864979</exponent>
<
p_b
>3633.33</p_b>
<
maximum_capillary_pressure
>36333.30</maximum_capillary_pressure>
</property>
<
property
>
<
name
>relative_permeability</name>
<
type
>
RelativePermeabilityVanGenuchten
</type>
<
residual_liquid_saturation
>0.1689</residual_liquid_saturation>
<
residual_gas_saturation
>0</residual_gas_saturation>
<
minimum_relative_permeability_liquid
>1e-12</minimum_relative_permeability_liquid>
<
exponent
>0.789029535864979</exponent>
</property>
<
property
>
<
name
>saturation</name>
<
type
>
SaturationVanGenuchten
</type>
<
residual_liquid_saturation
>0.1689</residual_liquid_saturation>
<
residual_gas_saturation
>0</residual_gas_saturation>
<
exponent
>0.789029535864979</exponent>
<
p_b
>3633.33</p_b>
</property>
<
property
>
<
name
>longitudinal_dispersivity</name>
<
type
>
Parameter
</type>
<
parameter_name
>alpha_l</parameter_name>
</property>
<
property
>
<
name
>transversal_dispersivity</name>
<
type
>
Parameter
</type>
<
parameter_name
>alpha_l</parameter_name>
</property>
</properties>
</medium>
</media>
<
time_loop
>
<
processes
>
<
process
ref
="HusC">
<
nonlinear_solver
>basic_picard</nonlinear_solver>
<
convergence_criterion
>
<
type
>
PerComponentDeltaX
</type>
<
norm_type
>NORM2</norm_type>
<
reltols
>1e-3 1e-3</reltols>
</convergence_criterion>
<
time_discretization
>
<
type
>
BackwardEuler
</type>
</time_discretization>
<
time_stepping
>
<
type
>
FixedTimeStepping
</type>
<
t_initial
>0.0</t_initial>
<
t_end
>40000</t_end>
<
timesteps
>
<
pair
>
<
repeat
>10</repeat>
<
delta_t
>1</delta_t>
</pair>
<
pair
>
<
repeat
>20</repeat>
<
delta_t
>2</delta_t>
</pair>
</timesteps>
</time_stepping>
</process>
</processes>
<
output
>
<
type
>
VTK
</type>
<
prefix
>Padilla_NaCl6</prefix>
<
timesteps
>
<
pair
>
<
repeat
>4</repeat>
<
each_steps
>1000</each_steps>
</pair>
<
pair
>
<
repeat
>20</repeat>
<
each_steps
>500</each_steps>
</pair>
<
pair
>
<
repeat
>1</repeat>
<
each_steps
>1000</each_steps>
</pair>
</timesteps>
<
variables
>
<
variable
>concentration</variable>
<
variable
>pressure</variable>
<
variable
>saturation</variable>
<
variable
>darcy_velocity</variable>
</variables>
<
suffix
>
ts
{:timestep}_t_{:time}</suffix>
</output>
</time_loop>
<
parameters
>
<
parameter
>
<
name
>rho_fluid</name>
<
type
>
Constant
</type>
<
value
>1000</value>
</parameter>
<
parameter
>
<
name
>decay_rate</name>
<
type
>
Constant
</type>
<
value
>0.0</value>
</parameter>
<
parameter
>
<
name
>retardation_factor</name>
<
type
>
Constant
</type>
<
value
>1</value>
</parameter>
<
parameter
>
<
name
>alpha_l</name>
<
type
>
Constant
</type>
<
value
>4.6916E-03</value>
</parameter>
<
parameter
>
<
name
>Dm</name>
<
type
>
Constant
</type>
<
value
>1e-9</value>
</parameter>
<
parameter
>
<
name
>c_ini</name>
<
type
>
Constant
</type>
<
value
>0</value>
</parameter>
<
parameter
>
<
name
>c1</name>
<
type
>
Constant
</type>
<
value
>1</value>
</parameter>
<
parameter
>
<
name
>p0_mesh</name>
<
type
>
MeshNode
</type>
<
field_name
>pressure</field_name>
</parameter>
<
parameter
>
<
name
>p0</name>
<
type
>
Constant
</type>
<
value
>0</value>
</parameter>
<
parameter
>
<
name
>p_bottom_NaCl6</name>
<
type
>
Constant
</type>
<
value
>-4800</value>
</parameter>
<
parameter
>
<
name
>q_top_NaCl6</name>
<
type
>
Constant
</type>
<
value
>6.46004E-06</value>
</parameter>
<
parameter
>
<
name
>constant_porosity_parameter</name>
<
type
>
Constant
</type>
<
value
>0.45</value>
</parameter>
<
parameter
>
<
name
>kappa1</name>
<
type
>
Constant
</type>
<
values
>1.17420446658343E-10</values>
</parameter>
</parameters>
<
process_variables
>
<
process_variable
>
<
name
>concentration</name>
<
components
>1</components>
<
order
>1</order>
<
initial_condition
>c_ini</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
geometrical_set
>h_us_mesh</geometrical_set>
<
geometry
>top</geometry>
<
type
>
Dirichlet
</type>
<
parameter
>c1</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>pressure</name>
<
components
>1</components>
<
order
>1</order>
<
initial_condition
>p0_mesh</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
geometrical_set
>h_us_mesh</geometrical_set>
<
geometry
>top</geometry>
<
type
>
Neumann
</type>
<
parameter
>q_top_NaCl6</parameter>
</boundary_condition>
<
boundary_condition
>
<
geometrical_set
>h_us_mesh</geometrical_set>
<
geometry
>bottom</geometry>
<
type
>
Dirichlet
</type>
<
parameter
>p_bottom_NaCl6</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
</process_variables>
<
nonlinear_solvers
>
<
nonlinear_solver
>
<
name
>basic_picard</name>
<
type
>
Picard
</type>
<
max_iter
>100</max_iter>
<
linear_solver
>general_linear_solver</linear_solver>
</nonlinear_solver>
<
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
>BiCGSTAB</solver_type>
<
precon_type
>DIAGONAL</precon_type>
<
max_iteration_step
>10000</max_iteration_step>
<
error_tolerance
>1e-10</error_tolerance>
</eigen>
</linear_solver>
</linear_solvers>
<
test_definition
>
<
vtkdiff
>
<
regex
>Padilla_NaCl6_ts_.*.vtu</regex>
<
field
>concentration</field>
<
absolute_tolerance
>1e-13</absolute_tolerance>
<
relative_tolerance
>0</relative_tolerance>
</vtkdiff>
<
vtkdiff
>
<
regex
>Padilla_NaCl6_ts_.*.vtu</regex>
<
field
>pressure</field>
<
absolute_tolerance
>1e-10</absolute_tolerance>
<
relative_tolerance
>0</relative_tolerance>
</vtkdiff>
</test_definition>
</OpenGeoSysProject>
OGS CTests—Project Files
Parabolic
RichardsComponentTransport
Padilla
Padilla_NaCl6
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