OGS
porosityIncrease_hc.prj
<
OpenGeoSysProject
>
<
meshes
>
<
mesh
>domain.vtu</mesh>
<
mesh
>physical_group_Left.vtu</mesh>
<
mesh
>physical_group_Right.vtu</mesh>
<
mesh
>physical_group_Reactive_domain.vtu</mesh>
</meshes>
<
processes
>
<
process
>
<
name
>hc</name>
<
type
>
ComponentTransport
</type>
<
integration_order
>2</integration_order>
<
coupling_scheme
>staggered</coupling_scheme>
<
process_variables
>
<
concentration
>S(6)</concentration>
<
concentration
>C</concentration>
<
concentration
>Ca</concentration>
<
concentration
>Na</concentration>
<
concentration
>Cl</concentration>
<
concentration
>H</concentration>
<
pressure
>pressure</pressure>
</process_variables>
<
specific_body_force
>0 0</specific_body_force>
<
chemically_induced_porosity_change
>true</chemically_induced_porosity_change>
<
secondary_variables
/>
</process>
</processes>
<
media
>
<
medium
id
="0">
<
phases
>
<
phase
>
<
type
>
AqueousLiquid
</type>
<
components
>
<
component
>
<
name
>S(6)</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>C</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>Ca</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>Na</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>Cl</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>H</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</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>
<
phase
>
<
type
>
Solid
</type>
<
components
>
<
component
>
<
name
>Calcite</name>
<
properties
>
<property>
<name>molar_volume</name>
<type>
Constant
</type>
<value>3.693e-05</value>
</property>
<property>
<name>volume_fraction</name>
<type>
Constant
</type>
<value>.0</value>
</property>
</properties>
</component>
</components>
</phase>
</phases>
<
properties
>
<
property
>
<
name
>permeability</name>
<
type
>
Parameter
</type>
<
parameter_name
>kappa_upstream</parameter_name>
</property>
<
property
>
<
name
>porosity</name>
<
type
>
Parameter
</type>
<
parameter_name
>porosity_upstream</parameter_name>
</property>
<
property
>
<
name
>longitudinal_dispersivity</name>
<
type
>
Constant
</type>
<
value
>1e-4</value>
</property>
<
property
>
<
name
>transversal_dispersivity</name>
<
type
>
Constant
</type>
<
value
>1e-4</value>
</property>
</properties>
</medium>
<
medium
id
="1">
<
phases
>
<
phase
>
<
type
>
AqueousLiquid
</type>
<
components
>
<
component
>
<
name
>S(6)</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>C</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>Ca</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>Na</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>Cl</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>H</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</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>
<
phase
>
<
type
>
Solid
</type>
<
components
>
<
component
>
<
name
>Calcite</name>
<
properties
>
<property>
<name>molar_volume</name>
<type>
Constant
</type>
<value>3.693e-05</value>
</property>
<property>
<name>volume_fraction</name>
<type>
Constant
</type>
<value>0.2185</value>
</property>
</properties>
</component>
</components>
</phase>
</phases>
<
properties
>
<
property
>
<
name
>permeability</name>
<
type
>
KozenyCarman
</type>
<
initial_permeability
>kappa_reactive_init</initial_permeability>
<
initial_porosity
>porosity_reactive</initial_porosity>
</property>
<
property
>
<
name
>porosity</name>
<
type
>
Parameter
</type>
<
parameter_name
>porosity_reactive</parameter_name>
</property>
<
property
>
<
name
>longitudinal_dispersivity</name>
<
type
>
Constant
</type>
<
value
>1e-4</value>
</property>
<
property
>
<
name
>transversal_dispersivity</name>
<
type
>
Constant
</type>
<
value
>1e-4</value>
</property>
</properties>
</medium>
<
medium
id
="2">
<
phases
>
<
phase
>
<
type
>
AqueousLiquid
</type>
<
components
>
<
component
>
<
name
>S(6)</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>C</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>Ca</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>Na</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>Cl</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
<
component
>
<
name
>H</name>
<
properties
>
<property>
<name>pore_diffusion</name>
<type>
Constant
</type>
<value>1.0e-9</value>
</property>
<property>
<name>retardation_factor</name>
<type>
Constant
</type>
<value>1</value>
</property>
<property>
<name>decay_rate</name>
<type>
Constant
</type>
<value>0</value>
</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>
<
phase
>
<
type
>
Solid
</type>
<
components
>
<
component
>
<
name
>Calcite</name>
<
properties
>
<property>
<name>molar_volume</name>
<type>
Constant
</type>
<value>3.693e-05</value>
</property>
<property>
<name>volume_fraction</name>
<type>
Constant
</type>
<value>0</value>
</property>
</properties>
</component>
</components>
</phase>
</phases>
<
properties
>
<
property
>
<
name
>permeability</name>
<
type
>
Parameter
</type>
<
parameter_name
>kappa_downstream</parameter_name>
</property>
<
property
>
<
name
>porosity</name>
<
type
>
Parameter
</type>
<
parameter_name
>porosity_downstream</parameter_name>
</property>
<
property
>
<
name
>longitudinal_dispersivity</name>
<
type
>
Constant
</type>
<
value
>1e-4</value>
</property>
<
property
>
<
name
>transversal_dispersivity</name>
<
type
>
Constant
</type>
<
value
>1e-4</value>
</property>
</properties>
</medium>
</media>
<
time_loop
>
<
global_process_coupling
>
<
max_iter
>100</max_iter>
<
convergence_criteria
>
<
convergence_criterion
>
<type>
DeltaX
</type>
<norm_type>NORM2</norm_type>
<reltol>1e-6</reltol>
</convergence_criterion>
<
convergence_criterion
>
<type>
DeltaX
</type>
<norm_type>NORM2</norm_type>
<reltol>1e-6</reltol>
</convergence_criterion>
<
convergence_criterion
>
<type>
DeltaX
</type>
<norm_type>NORM2</norm_type>
<reltol>1e-6</reltol>
</convergence_criterion>
<
convergence_criterion
>
<type>
DeltaX
</type>
<norm_type>NORM2</norm_type>
<reltol>1e-6</reltol>
</convergence_criterion>
<
convergence_criterion
>
<type>
DeltaX
</type>
<norm_type>NORM2</norm_type>
<reltol>1e-6</reltol>
</convergence_criterion>
<
convergence_criterion
>
<type>
DeltaX
</type>
<norm_type>NORM2</norm_type>
<reltol>1e-6</reltol>
</convergence_criterion>
<
convergence_criterion
>
<type>
DeltaX
</type>
<norm_type>NORM2</norm_type>
<reltol>1e-6</reltol>
</convergence_criterion>
</convergence_criteria>
</global_process_coupling>
<
processes
>
<
process
ref
="hc">
<
nonlinear_solver
>basic_picard</nonlinear_solver>
<
convergence_criterion
>
<
type
>
DeltaX
</type>
<
norm_type
>NORM2</norm_type>
<
reltol
>1e-6</reltol>
</convergence_criterion>
<
time_discretization
>
<
type
>
BackwardEuler
</type>
</time_discretization>
<
time_stepping
>
<
type
>
IterationNumberBasedTimeStepping
</type>
<
t_initial
>0</t_initial>
<
t_end
>1440000</t_end>
<
initial_dt
>120</initial_dt>
<
minimum_dt
>120</minimum_dt>
<
maximum_dt
>120</maximum_dt>
<
number_iterations
>1 2 5 10 20</number_iterations>
<
multiplier
>1.6 1.4 1.0 0.7 0.5</multiplier>
</time_stepping>
</process>
<
process
ref
="hc">
<
nonlinear_solver
>basic_picard</nonlinear_solver>
<
convergence_criterion
>
<
type
>
DeltaX
</type>
<
norm_type
>NORM2</norm_type>
<
reltol
>1e-10</reltol>
</convergence_criterion>
<
time_discretization
>
<
type
>
BackwardEuler
</type>
</time_discretization>
<
time_stepping
>
<
type
>
IterationNumberBasedTimeStepping
</type>
<
t_initial
>0</t_initial>
<
t_end
>1440000</t_end>
<
initial_dt
>120</initial_dt>
<
minimum_dt
>120</minimum_dt>
<
maximum_dt
>120</maximum_dt>
<
number_iterations
>1 2 5 10 20</number_iterations>
<
multiplier
>1.6 1.4 1.0 0.7 0.5</multiplier>
</time_stepping>
</process>
<
process
ref
="hc">
<
nonlinear_solver
>basic_picard</nonlinear_solver>
<
convergence_criterion
>
<
type
>
DeltaX
</type>
<
norm_type
>NORM2</norm_type>
<
reltol
>1e-10</reltol>
</convergence_criterion>
<
time_discretization
>
<
type
>
BackwardEuler
</type>
</time_discretization>
<
time_stepping
>
<
type
>
IterationNumberBasedTimeStepping
</type>
<
t_initial
>0</t_initial>
<
t_end
>1440000</t_end>
<
initial_dt
>120</initial_dt>
<
minimum_dt
>120</minimum_dt>
<
maximum_dt
>120</maximum_dt>
<
number_iterations
>1 2 5 10 20</number_iterations>
<
multiplier
>1.6 1.4 1.0 0.7 0.5</multiplier>
</time_stepping>
</process>
<
process
ref
="hc">
<
nonlinear_solver
>basic_picard</nonlinear_solver>
<
convergence_criterion
>
<
type
>
DeltaX
</type>
<
norm_type
>NORM2</norm_type>
<
reltol
>1e-10</reltol>
</convergence_criterion>
<
time_discretization
>
<
type
>
BackwardEuler
</type>
</time_discretization>
<
time_stepping
>
<
type
>
IterationNumberBasedTimeStepping
</type>
<
t_initial
>0</t_initial>
<
t_end
>1440000</t_end>
<
initial_dt
>120</initial_dt>
<
minimum_dt
>120</minimum_dt>
<
maximum_dt
>120</maximum_dt>
<
number_iterations
>1 2 5 10 20</number_iterations>
<
multiplier
>1.6 1.4 1.0 0.7 0.5</multiplier>
</time_stepping>
</process>
<
process
ref
="hc">
<
nonlinear_solver
>basic_picard</nonlinear_solver>
<
convergence_criterion
>
<
type
>
DeltaX
</type>
<
norm_type
>NORM2</norm_type>
<
reltol
>1e-10</reltol>
</convergence_criterion>
<
time_discretization
>
<
type
>
BackwardEuler
</type>
</time_discretization>
<
time_stepping
>
<
type
>
IterationNumberBasedTimeStepping
</type>
<
t_initial
>0</t_initial>
<
t_end
>1440000</t_end>
<
initial_dt
>120</initial_dt>
<
minimum_dt
>120</minimum_dt>
<
maximum_dt
>120</maximum_dt>
<
number_iterations
>1 2 5 10 20</number_iterations>
<
multiplier
>1.6 1.4 1.0 0.7 0.5</multiplier>
</time_stepping>
</process>
<
process
ref
="hc">
<
nonlinear_solver
>basic_picard</nonlinear_solver>
<
convergence_criterion
>
<
type
>
DeltaX
</type>
<
norm_type
>NORM2</norm_type>
<
reltol
>1e-10</reltol>
</convergence_criterion>
<
time_discretization
>
<
type
>
BackwardEuler
</type>
</time_discretization>
<
time_stepping
>
<
type
>
IterationNumberBasedTimeStepping
</type>
<
t_initial
>0</t_initial>
<
t_end
>1440000</t_end>
<
initial_dt
>120</initial_dt>
<
minimum_dt
>120</minimum_dt>
<
maximum_dt
>120</maximum_dt>
<
number_iterations
>1 2 5 10 20</number_iterations>
<
multiplier
>1.6 1.4 1.0 0.7 0.5</multiplier>
</time_stepping>
</process>
<
process
ref
="hc">
<
nonlinear_solver
>basic_picard</nonlinear_solver>
<
convergence_criterion
>
<
type
>
DeltaX
</type>
<
norm_type
>NORM2</norm_type>
<
reltol
>1e-10</reltol>
</convergence_criterion>
<
time_discretization
>
<
type
>
BackwardEuler
</type>
</time_discretization>
<
time_stepping
>
<
type
>
IterationNumberBasedTimeStepping
</type>
<
t_initial
>0</t_initial>
<
t_end
>1440000</t_end>
<
initial_dt
>120</initial_dt>
<
minimum_dt
>120</minimum_dt>
<
maximum_dt
>120</maximum_dt>
<
number_iterations
>1 2 5 10 20</number_iterations>
<
multiplier
>1.6 1.4 1.0 0.7 0.5</multiplier>
</time_stepping>
</process>
</processes>
<
output
>
<
type
>
VTK
</type>
<
prefix
>hc_porosity_change</prefix>
<
timesteps
>
<
pair
>
<
repeat
>1</repeat>
<
each_steps
>1</each_steps>
</pair>
</timesteps>
<
variables
/>
</output>
</time_loop>
<
chemical_system
chemical_solver
="Phreeqc">
<
mesh
>domain</mesh>
<
linear_solver
>general_linear_solver</linear_solver>
<
database
>llnl.dat</database>
<
solution
>
<
temperature
>25</temperature>
<
pressure
>1</pressure>
<
pe
>4</pe>
<
components
>
<
component
>S(6)</component>
<
component
>C</component>
<
component
>Ca</component>
<
component
>Na</component>
<
component
>Cl</component>
</components>
</solution>
<
kinetic_reactants
>
<
kinetic_reactant
>
<
name
>Calcite</name>
</kinetic_reactant>
</kinetic_reactants>
<
rates
>
<
rate
>
<
kinetic_reactant
>Calcite</kinetic_reactant>
<
expression
>
<
statement
>if (M <= 0) then goto 25</statement>
<
statement
>R = 8.314472</statement>
<
statement
>deltaT = 1
/
TK - 1
/
298.15</statement>
<
statement
>logK25 = -0.30</statement>
<
statement
>Ea = 14400</statement>
<
statement
>ny = 1.0</statement>
<
statement
>mech_a = (10^logK25) * ACT("H+")^ny * EXP(- Ea
/
R * deltaT)</statement>
<
statement
>logK25 = -5.81</statement>
<
statement
>Ea = 23500</statement>
<
statement
>mech_b = (10^logK25) * EXP(- Ea
/
R * deltaT)</statement>
<
statement
>logK25 = -3.48</statement>
<
statement
>Ea = 35400</statement>
<
statement
>ny = 1.0</statement>
<
statement
>mech_c = (10^logK25) * SR("CO2(g)")^ny * EXP(- Ea
/
R * deltaT)</statement>
<
statement
>K_temp = mech_a + mech_b + mech_c</statement>
<
statement
>teta = 1</statement>
<
statement
>eta = 1</statement>
<
statement
>molar_volume = 3.692e-05</statement>
<
statement
>bulk_volume = molar_volume * PARM(1)</statement>
<
statement
>specific_surface_area = 20</statement>
<
statement
>surface_area = specific_surface_area * bulk_volume</statement>
<
statement
>rate = surface_area * K_temp * (1 - SR("Calcite")^teta)^eta</statement>
<
statement
>if rate < 0 then rate = 0</statement>
<
statement
>moles = rate * time</statement>
<
statement
>save moles</statement>
</expression>
</rate>
</rates>
<
knobs
>
<
max_iter
>100</max_iter>
<
relative_convergence_tolerance
>1e-12</relative_convergence_tolerance>
<
tolerance
>1e-15</tolerance>
<
step_size
>100</step_size>
<
scaling
>0</scaling>
</knobs>
</chemical_system>
<
parameters
>
<
parameter
>
<
name
>porosity_upstream</name>
<
type
>
Constant
</type>
<
value
>0.4277</value>
</parameter>
<
parameter
>
<
name
>porosity_reactive</name>
<
type
>
Constant
</type>
<
value
>0.3255</value>
</parameter>
<
parameter
>
<
name
>porosity_downstream</name>
<
type
>
Constant
</type>
<
value
>0.4685</value>
</parameter>
<
parameter
>
<
name
>p_initial</name>
<
type
>
Constant
</type>
<
value
>101325</value>
</parameter>
<
parameter
>
<
name
>p_outlet</name>
<
type
>
Constant
</type>
<
value
>101325</value>
</parameter>
<
parameter
>
<
name
>q_inlet</name>
<
type
>
Constant
</type>
<
value
>2.16948e-3</value>
</parameter>
<
parameter
>
<
name
>S6_initial</name>
<
type
>
Constant
</type>
<
value
>1e-8</value>
</parameter>
<
parameter
>
<
name
>S6_inlet</name>
<
type
>
Constant
</type>
<
value
>5e-3</value>
</parameter>
<
parameter
>
<
name
>C_initial</name>
<
type
>
MeshNode
</type>
<
field_name
>C</field_name>
</parameter>
<
parameter
>
<
name
>C_inlet</name>
<
type
>
Constant
</type>
<
value
>1.6e-5</value>
</parameter>
<
parameter
>
<
name
>Ca_initial</name>
<
type
>
MeshNode
</type>
<
field_name
>Ca</field_name>
</parameter>
<
parameter
>
<
name
>Ca_inlet</name>
<
type
>
Constant
</type>
<
value
>1e-8</value>
</parameter>
<
parameter
>
<
name
>NaCl_initial</name>
<
type
>
Constant
</type>
<
value
>3e-8</value>
</parameter>
<
parameter
>
<
name
>NaCl_inlet</name>
<
type
>
Constant
</type>
<
value
>3e-8</value>
</parameter>
<
parameter
>
<
name
>H_initial</name>
<
type
>
MeshNode
</type>
<
field_name
>H</field_name>
</parameter>
<
parameter
>
<
name
>H_inlet</name>
<
type
>
Constant
</type>
<
value
>2.461e-6</value>
</parameter>
</parameters>
<
process_variables
>
<
process_variable
>
<
name
>pressure</name>
<
components
>1</components>
<
order
>1</order>
<
initial_condition
>p_initial</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>physical_group_Left</mesh>
<
type
>
Neumann
</type>
<
parameter
>q_inlet</parameter>
</boundary_condition>
<
boundary_condition
>
<
mesh
>physical_group_Right</mesh>
<
type
>
Dirichlet
</type>
<
parameter
>p_outlet</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>S(6)</name>
<
components
>1</components>
<
order
>1</order>
<
initial_condition
>S6_initial</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>physical_group_Left</mesh>
<
type
>
Dirichlet
</type>
<
parameter
>S6_inlet</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>C</name>
<
components
>1</components>
<
order
>1</order>
<
initial_condition
>C_initial</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>physical_group_Left</mesh>
<
type
>
Dirichlet
</type>
<
parameter
>C_inlet</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>Ca</name>
<
components
>1</components>
<
order
>1</order>
<
initial_condition
>Ca_initial</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>physical_group_Left</mesh>
<
type
>
Dirichlet
</type>
<
parameter
>Ca_inlet</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>Na</name>
<
components
>1</components>
<
order
>1</order>
<
initial_condition
>NaCl_initial</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>physical_group_Left</mesh>
<
type
>
Dirichlet
</type>
<
parameter
>NaCl_inlet</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>Cl</name>
<
components
>1</components>
<
order
>1</order>
<
initial_condition
>NaCl_initial</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>physical_group_Left</mesh>
<
type
>
Dirichlet
</type>
<
parameter
>NaCl_inlet</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<
process_variable
>
<
name
>H</name>
<
components
>1</components>
<
order
>1</order>
<
initial_condition
>H_initial</initial_condition>
<
boundary_conditions
>
<
boundary_condition
>
<
mesh
>physical_group_Left</mesh>
<
type
>
Dirichlet
</type>
<
parameter
>H_inlet</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_solvers>
<
linear_solvers
>
<
linear_solver
>
<
name
>general_linear_solver</name>
<
eigen
>
<
solver_type
>BiCGSTAB</solver_type>
<
precon_type
>ILUT</precon_type>
<
max_iteration_step
>1000</max_iteration_step>
<
error_tolerance
>1e-14</error_tolerance>
</eigen>
<
petsc
>
<
prefix
>hc</prefix>
<
parameters
>-hc_ksp_type bcgs -hc_pc_type bjacobi -hc_ksp_rtol 1e-14 -hc_ksp_max_it 20000</parameters>
</petsc>
</linear_solver>
</linear_solvers>
</OpenGeoSysProject>
OGS CTests—Project Files
Parabolic
ComponentTransport
ReactiveTransport
Acidification
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