From 90e014c4b5f00ffb7ee5285d3253981d63cc11cb Mon Sep 17 00:00:00 2001
From: joboog <johannesboog@yahoo.de>
Date: Fri, 12 Jul 2019 11:16:35 +0200
Subject: [PATCH] [T] KineticReactant_AllAsComponents 2d added
---
ProcessLib/ComponentTransport/Tests.cmake | 41 ++
.../KineticReactant2_2d.gml | 3 +
.../KineticReactant2_2d.prj | 527 ++++++++++++++++++
.../KineticReactant2_2d.vtu | 3 +
...ant2_2d_pcs_4_ts_0_t_0.000000_expected.vtu | 3 +
..._2d_pcs_4_ts_12_t_1200.000000_expected.vtu | 3 +
..._2d_pcs_4_ts_16_t_1600.000000_expected.vtu | 3 +
..._2d_pcs_4_ts_20_t_2000.000000_expected.vtu | 3 +
...t2_2d_pcs_4_ts_4_t_400.000000_expected.vtu | 3 +
...t2_2d_pcs_4_ts_8_t_800.000000_expected.vtu | 3 +
.../KineticReactant_AllAsComponents/test.dat | 52 ++
11 files changed, 644 insertions(+)
create mode 100644 Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d.gml
create mode 100644 Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d.prj
create mode 100644 Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d.vtu
create mode 100644 Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d_pcs_4_ts_0_t_0.000000_expected.vtu
create mode 100644 Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d_pcs_4_ts_12_t_1200.000000_expected.vtu
create mode 100644 Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d_pcs_4_ts_16_t_1600.000000_expected.vtu
create mode 100644 Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d_pcs_4_ts_20_t_2000.000000_expected.vtu
create mode 100644 Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d_pcs_4_ts_4_t_400.000000_expected.vtu
create mode 100644 Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d_pcs_4_ts_8_t_800.000000_expected.vtu
create mode 100644 Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/test.dat
diff --git a/ProcessLib/ComponentTransport/Tests.cmake b/ProcessLib/ComponentTransport/Tests.cmake
index eced87a33f8..3d95092f9c4 100644
--- a/ProcessLib/ComponentTransport/Tests.cmake
+++ b/ProcessLib/ComponentTransport/Tests.cmake
@@ -1034,3 +1034,44 @@ KineticReactant2_pcs_4_ts_168_t_16800.000000_expected.vtu KineticReactant2_pcs_4
KineticReactant2_pcs_4_ts_168_t_16800.000000_expected.vtu KineticReactant2_pcs_4_ts_168_t_16800.000000.vtu H H 1e-10 1e-16
KineticReactant2_pcs_4_ts_210_t_21000.000000_expected.vtu KineticReactant2_pcs_4_ts_210_t_21000.000000.vtu H H 1e-10 1e-16
)
+
+AddTest(
+ NAME 2D_ReactiveMassTransport_KineticReactantBlockTest_AllAsComponents
+ PATH Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents
+ EXECUTABLE ogs
+ EXECUTABLE_ARGS KineticReactant2_2d.prj
+ WRAPPER time
+ TESTER vtkdiff
+ REQUIREMENTS NOT OGS_USE_MPI
+ DIFF_DATA
+ KineticReactant2_2d_pcs_4_ts_4_t_400.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_4_t_400.000000.vtu pressure pressure 1e-6 1e-10
+ KineticReactant2_2d_pcs_4_ts_8_t_800.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_8_t_800.000000.vtu pressure pressure 1e-6 1e-10
+ KineticReactant2_2d_pcs_4_ts_12_t_1200.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_12_t_1200.000000.vtu pressure pressure 1e-6 1e-10
+ KineticReactant2_2d_pcs_4_ts_16_t_1600.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_16_t_1600.000000.vtu pressure pressure 1e-6 1e-10
+ KineticReactant2_2d_pcs_4_ts_20_t_2000.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_20_t_2000.000000.vtu pressure pressure 1e-6 1e-10
+ KineticReactant2_2d_pcs_4_ts_4_t_400.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_4_t_400.000000.vtu pressure pressure 1e-6 1e-10
+ KineticReactant2_2d_pcs_4_ts_8_t_800.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_8_t_800.000000.vtu pressure pressure 1e-6 1e-10
+ KineticReactant2_2d_pcs_4_ts_12_t_1200.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_12_t_1200.000000.vtu pressure pressure 1e-6 1e-10
+ KineticReactant2_2d_pcs_4_ts_16_t_1600.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_16_t_1600.000000.vtu pressure pressure 1e-6 1e-10
+ KineticReactant2_2d_pcs_4_ts_20_t_2000.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_20_t_2000.000000.vtu pressure pressure 1e-6 1e-10
+ KineticReactant2_2d_pcs_4_ts_4_t_400.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_4_t_400.000000.vtu Synthetica Synthetica 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_8_t_800.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_8_t_800.000000.vtu Synthetica Synthetica 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_12_t_1200.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_12_t_1200.000000.vtu Synthetica Synthetica 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_16_t_1600.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_16_t_1600.000000.vtu Synthetica Synthetica 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_20_t_2000.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_20_t_2000.000000.vtu Synthetica Synthetica 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_4_t_400.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_4_t_400.000000.vtu Syntheticb Syntheticb 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_8_t_800.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_8_t_800.000000.vtu Syntheticb Syntheticb 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_12_t_1200.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_12_t_1200.000000.vtu Syntheticb Syntheticb 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_16_t_1600.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_16_t_1600.000000.vtu Syntheticb Syntheticb 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_20_t_2000.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_20_t_2000.000000.vtu Syntheticb Syntheticb 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_4_t_400.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_4_t_400.000000.vtu Productd Productd 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_8_t_800.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_8_t_800.000000.vtu Productd Productd 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_12_t_1200.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_12_t_1200.000000.vtu Productd Productd 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_16_t_1600.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_16_t_1600.000000.vtu Productd Productd 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_20_t_2000.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_20_t_2000.000000.vtu Productd Productd 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_4_t_400.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_4_t_400.000000.vtu H H 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_8_t_800.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_8_t_800.000000.vtu H H 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_12_t_1200.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_12_t_1200.000000.vtu H H 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_16_t_1600.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_16_t_1600.000000.vtu H H 1e-10 1e-16
+ KineticReactant2_2d_pcs_4_ts_20_t_2000.000000_expected.vtu KineticReactant2_2d_pcs_4_ts_20_t_2000.000000.vtu H H 1e-10 1e-16
+)
diff --git a/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d.gml b/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d.gml
new file mode 100644
index 00000000000..b22889ea64b
--- /dev/null
+++ b/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d.gml
@@ -0,0 +1,3 @@
+version https://git-lfs.github.com/spec/v1
+oid sha256:bbbab1bc2495fca2ba28adf2b243002873448fd5a59afcbe12919e1fa64b60f2
+size 778
diff --git a/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d.prj b/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d.prj
new file mode 100644
index 00000000000..a5e8d3ac450
--- /dev/null
+++ b/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d.prj
@@ -0,0 +1,527 @@
+<?xml version="1.0" encoding="ISO-8859-1"?>
+<OpenGeoSysProject>
+ <mesh>KineticReactant2_2d.vtu</mesh>
+ <geometry>KineticReactant2_2d.gml</geometry>
+ <processes>
+ <process>
+ <name>hc</name>
+ <type>ComponentTransport</type>
+ <integration_order>2</integration_order>
+ <coupling_scheme>staggered</coupling_scheme>
+ <process_variables>
+ <concentration>H</concentration>
+ <concentration>Synthetica</concentration>
+ <concentration>Syntheticb</concentration>
+ <concentration>Productd</concentration>
+ <pressure>pressure</pressure>
+ </process_variables>
+ <fluid>
+ <density>
+ <type>Constant</type>
+ <value>1e3</value>
+ </density>
+ <viscosity>
+ <type>Constant</type>
+ <value>1e-3</value>
+ </viscosity>
+ </fluid>
+ <porous_medium>
+ <porous_medium id="0">
+ <permeability>
+ <type>Constant</type>
+ <permeability_tensor_entries>kappa</permeability_tensor_entries>
+ </permeability>
+ <porosity>
+ <type>Constant</type>
+ <porosity_parameter>porosity</porosity_parameter>
+ </porosity>
+ <storage>
+ <type>Constant</type>
+ <value>0.0</value>
+ </storage>
+ </porous_medium>
+ </porous_medium>
+ <fluid_reference_density>rho_fluid</fluid_reference_density>
+ <decay_rate>decay</decay_rate>
+ <specific_body_force>0 0</specific_body_force>
+ <secondary_variables>
+ <secondary_variable type="static" internal_name="darcy_velocity" output_name="darcy_velocity"/>
+ </secondary_variables>
+ </process>
+ </processes>
+ <media>
+ <medium id="0">
+ <phases>
+ <phase>
+ <type>AqueousLiquid</type>
+ <components>
+ <component>
+ <name>H</name>
+ <properties>
+ <property>
+ <name>molecular_diffusion</name>
+ <type>Constant</type>
+ <value>1e-7</value>
+ </property>
+ <property>
+ <name>retardation_factor</name>
+ <type>Constant</type>
+ <value>1</value>
+ </property>
+ </properties>
+ </component>
+ <component>
+ <name>Synthetica</name>
+ <properties>
+ <property>
+ <name>molecular_diffusion</name>
+ <type>Constant</type>
+ <value>1e-12</value>
+ </property>
+ <property>
+ <name>retardation_factor</name>
+ <type>Constant</type>
+ <value>1</value>
+ </property>
+ </properties>
+ </component>
+ <component>
+ <name>Syntheticb</name>
+ <properties>
+ <property>
+ <name>molecular_diffusion</name>
+ <type>Constant</type>
+ <value>1e-12</value>
+ </property>
+ <property>
+ <name>retardation_factor</name>
+ <type>Constant</type>
+ <value>1</value>
+ </property>
+ </properties>
+ </component>
+ <component>
+ <name>Productd</name>
+ <properties>
+ <property>
+ <name>molecular_diffusion</name>
+ <type>Constant</type>
+ <value>1e-12</value>
+ </property>
+ <property>
+ <name>retardation_factor</name>
+ <type>Constant</type>
+ <value>1</value>
+ </property>
+ </properties>
+ </component>
+ </components>
+ </phase>
+ </phases>
+ <properties>
+ <property>
+ <name>longitudinal_dispersivity</name>
+ <type>Constant</type>
+ <value>0</value>
+ </property>
+ <property>
+ <name>transversal_dispersivity</name>
+ <type>Constant</type>
+ <value>0</value>
+ </property>
+ </properties>
+ </medium>
+ </media>
+ <time_loop>
+ <global_process_coupling>
+ <max_iter>6</max_iter>
+ <convergence_criteria>
+ <!-- convergence criterion for the first process (P) -->
+ <convergence_criterion>
+ <type>DeltaX</type>
+ <norm_type>NORM2</norm_type>
+ <reltol>1e-14</reltol>
+ </convergence_criterion>
+ <!-- convergence criterion for the second process (H) -->
+ <convergence_criterion>
+ <type>DeltaX</type>
+ <norm_type>NORM2</norm_type>
+ <reltol>1e-14</reltol>
+ </convergence_criterion>
+ <!-- convergence criterion for the second process (Synthetica) -->
+ <convergence_criterion>
+ <type>DeltaX</type>
+ <norm_type>NORM2</norm_type>
+ <reltol>1e-14</reltol>
+ </convergence_criterion>
+ <!-- convergence criterion for the second process (Syntheticb) -->
+ <convergence_criterion>
+ <type>DeltaX</type>
+ <norm_type>NORM2</norm_type>
+ <reltol>1e-14</reltol>
+ </convergence_criterion>
+ <!-- convergence criterion for the second process (Productd) -->
+ <convergence_criterion>
+ <type>DeltaX</type>
+ <norm_type>NORM2</norm_type>
+ <reltol>1e-14</reltol>
+ </convergence_criterion>
+ </convergence_criteria>
+ </global_process_coupling>
+ <processes>
+ <!-- convergence criterion for hydraulic equation -->
+ <process ref="hc">
+ <nonlinear_solver>basic_picard</nonlinear_solver>
+ <convergence_criterion>
+ <type>DeltaX</type>
+ <norm_type>NORM2</norm_type>
+ <reltol>1e-14</reltol>
+ </convergence_criterion>
+ <time_discretization>
+ <type>BackwardEuler</type>
+ </time_discretization>
+ <time_stepping>
+ <type>FixedTimeStepping</type>
+ <t_initial>0.0</t_initial>
+ <t_end>2000</t_end>
+ <timesteps>
+ <pair>
+ <repeat>20</repeat>
+ <delta_t>100</delta_t>
+ </pair>
+ </timesteps>
+ </time_stepping>
+ </process>
+ <!-- convergence criterion for component transport equation (H) -->
+ <process ref="hc">
+ <nonlinear_solver>basic_picard</nonlinear_solver>
+ <convergence_criterion>
+ <type>DeltaX</type>
+ <norm_type>NORM2</norm_type>
+ <reltol>1e-14</reltol>
+ </convergence_criterion>
+ <time_discretization>
+ <type>BackwardEuler</type>
+ </time_discretization>
+ <time_stepping>
+ <type>FixedTimeStepping</type>
+ <t_initial>0.0</t_initial>
+ <t_end>2000</t_end>
+ <timesteps>
+ <pair>
+ <repeat>20</repeat>
+ <delta_t>100</delta_t>
+ </pair>
+ </timesteps>
+ </time_stepping>
+ </process>
+ <!-- convergence criterion for component transport equation (Synthetica) -->
+ <process ref="hc">
+ <nonlinear_solver>basic_picard</nonlinear_solver>
+ <convergence_criterion>
+ <type>DeltaX</type>
+ <norm_type>NORM2</norm_type>
+ <reltol>1e-14</reltol>
+ </convergence_criterion>
+ <time_discretization>
+ <type>BackwardEuler</type>
+ </time_discretization>
+ <time_stepping>
+ <type>FixedTimeStepping</type>
+ <t_initial>0.0</t_initial>
+ <t_end>2000</t_end>
+ <timesteps>
+ <pair>
+ <repeat>20</repeat>
+ <delta_t>100</delta_t>
+ </pair>
+ </timesteps>
+ </time_stepping>
+ </process>
+ <!-- convergence criterion for component transport equation (Syntheticb) -->
+ <process ref="hc">
+ <nonlinear_solver>basic_picard</nonlinear_solver>
+ <convergence_criterion>
+ <type>DeltaX</type>
+ <norm_type>NORM2</norm_type>
+ <reltol>1e-14</reltol>
+ </convergence_criterion>
+ <time_discretization>
+ <type>BackwardEuler</type>
+ </time_discretization>
+ <time_stepping>
+ <type>FixedTimeStepping</type>
+ <t_initial>0.0</t_initial>
+ <t_end>2000</t_end>
+ <timesteps>
+ <pair>
+ <repeat>20</repeat>
+ <delta_t>100</delta_t>
+ </pair>
+ </timesteps>
+ </time_stepping>
+ </process>
+ <!-- convergence criterion for component transport equation (Productd) -->
+ <process ref="hc">
+ <nonlinear_solver>basic_picard</nonlinear_solver>
+ <convergence_criterion>
+ <type>DeltaX</type>
+ <norm_type>NORM2</norm_type>
+ <reltol>1e-14</reltol>
+ </convergence_criterion>
+ <time_discretization>
+ <type>BackwardEuler</type>
+ </time_discretization>
+ <time_stepping>
+ <type>FixedTimeStepping</type>
+ <t_initial>0.0</t_initial>
+ <t_end>2000</t_end>
+ <timesteps>
+ <pair>
+ <repeat>20</repeat>
+ <delta_t>100</delta_t>
+ </pair>
+ </timesteps>
+ </time_stepping>
+ </process>
+ </processes>
+ <output>
+ <type>VTK</type>
+ <prefix>KineticReactant2_2d</prefix>
+ <timesteps>
+ <pair>
+ <repeat>5</repeat>
+ <each_steps>4</each_steps>
+ </pair>
+ </timesteps>
+ <variables>
+ <variable>H</variable>
+ <variable>Synthetica</variable>
+ <variable>Syntheticb</variable>
+ <variable>Productd</variable>
+ <variable>pressure</variable>
+ <variable>darcy_velocity</variable>
+ </variables>
+ </output>
+ </time_loop>
+ <chemical_system chemical_solver="Phreeqc">
+ <database>test.dat</database>
+ <solution>
+ <temperature>25</temperature>
+ <pressure>1</pressure>
+ <pe>4</pe>
+ <components>
+ <component>Synthetica</component>
+ <component>Syntheticb</component>
+ <component>Productd</component>
+ </components>
+ </solution>
+ <kinetic_reactants>
+ <kinetic_reactant>
+ <name>Synthetics_to_Productd</name>
+ <chemical_formula>Productd 1 Synthetica -1 Syntheticb -0.5</chemical_formula>
+ <initial_amount>1.0</initial_amount>
+ </kinetic_reactant>
+ </kinetic_reactants>
+ <rates>
+ <rate>
+ <kinetic_reactant>Synthetics_to_Productd</kinetic_reactant>
+ <expression>
+ <statement>Km = 10</statement>
+ <statement>U = 1e-4</statement>
+ <statement>rate = U * TOT("Synthetica") / (Km + TOT("Syntheticb"))</statement>
+ <statement>moles = rate * TIME</statement>
+ <statement>save moles</statement>
+ </expression>
+ </rate>
+ </rates>
+ </chemical_system>
+ <parameters>
+ <parameter>
+ <name>kappa</name>
+ <type>Constant</type>
+ <values>1.157e-12 0 0 1.157e-12</values>
+ </parameter>
+ <parameter>
+ <name>porosity</name>
+ <type>Constant</type>
+ <value>1</value>
+ </parameter>
+ <parameter>
+ <name>rho_fluid</name>
+ <type>Constant</type>
+ <value>1000</value>
+ </parameter>
+ <parameter>
+ <name>retardation</name>
+ <type>Constant</type>
+ <value>1</value>
+ </parameter>
+ <parameter>
+ <name>decay</name>
+ <type>Constant</type>
+ <value>0</value>
+ </parameter>
+ <parameter>
+ <name>p0</name>
+ <type>Constant</type>
+ <value>1e5</value>
+ </parameter>
+ <parameter>
+ <name>p_upstream</name>
+ <type>Constant</type>
+ <value>1e5</value>
+ </parameter>
+ <parameter>
+ <name>p_downstream_Neumann</name>
+ <type>Constant</type>
+ <value>-1.685e-2</value>
+ </parameter>
+ <parameter>
+ <name>c0_H</name>
+ <type>Constant</type>
+ <!--pH=7-->
+ <value>1e-7</value>
+ </parameter>
+ <parameter>
+ <name>c0_Synthetica</name>
+ <type>Constant</type>
+ <value>0.5</value>
+ </parameter>
+ <parameter>
+ <name>c0_Syntheticb</name>
+ <type>Constant</type>
+ <value>0.5</value>
+ </parameter>
+ <parameter>
+ <name>c0_Productd</name>
+ <type>Constant</type>
+ <value>0.0</value>
+ <!--type>Function</type>
+ <expression>1*x</expression-->
+ </parameter>
+ <parameter>
+ <name>c_H</name>
+ <type>Constant</type>
+ <!--pH=7-->
+ <value>1e-7</value>
+ </parameter>
+ <parameter>
+ <name>c_Synthetica</name>
+ <type>Constant</type>
+ <value>0.5</value>
+ </parameter>
+ <parameter>
+ <name>c_Syntheticb</name>
+ <type>Constant</type>
+ <value>0.5</value>
+ </parameter>
+ <parameter>
+ <name>c_Productd</name>
+ <type>Constant</type>
+ <value>0.00</value>
+ </parameter>
+ </parameters>
+ <process_variables>
+ <process_variable>
+ <name>pressure</name>
+ <components>1</components>
+ <order>1</order>
+ <initial_condition>p0</initial_condition>
+ <boundary_conditions>
+ <boundary_condition>
+ <geometrical_set>geometry</geometrical_set>
+ <geometry>upstream</geometry>
+ <type>Dirichlet</type>
+ <parameter>p_upstream</parameter>
+ </boundary_condition>
+ <boundary_condition>
+ <geometrical_set>geometry</geometrical_set>
+ <geometry>downstream</geometry>
+ <type>Neumann</type>
+ <parameter>p_downstream_Neumann</parameter>
+ </boundary_condition>
+ </boundary_conditions>
+ </process_variable>
+ <process_variable>
+ <name>H</name>
+ <components>1</components>
+ <order>1</order>
+ <initial_condition>c0_H</initial_condition>
+ <boundary_conditions>
+ <boundary_condition>
+ <geometrical_set>geometry</geometrical_set>
+ <geometry>upstream</geometry>
+ <type>Dirichlet</type>
+ <parameter>c_H</parameter>
+ </boundary_condition>
+ </boundary_conditions>
+ </process_variable>
+ <process_variable>
+ <name>Synthetica</name>
+ <components>1</components>
+ <order>1</order>
+ <initial_condition>c0_Synthetica</initial_condition>
+ <boundary_conditions>
+ <boundary_condition>
+ <geometrical_set>geometry</geometrical_set>
+ <geometry>upstream</geometry>
+ <type>Dirichlet</type>
+ <parameter>c_Synthetica</parameter>
+ </boundary_condition>
+ </boundary_conditions>
+ </process_variable>
+ <process_variable>
+ <name>Syntheticb</name>
+ <components>1</components>
+ <order>1</order>
+ <initial_condition>c0_Syntheticb</initial_condition>
+ <boundary_conditions>
+ <boundary_condition>
+ <geometrical_set>geometry</geometrical_set>
+ <geometry>upstream</geometry>
+ <type>Dirichlet</type>
+ <parameter>c_Syntheticb</parameter>
+ </boundary_condition>
+ </boundary_conditions>
+ </process_variable>
+ <process_variable>
+ <name>Productd</name>
+ <components>1</components>
+ <order>1</order>
+ <initial_condition>c0_Productd</initial_condition>
+ <boundary_conditions>
+ <boundary_condition>
+ <geometrical_set>geometry</geometrical_set>
+ <geometry>upstream</geometry>
+ <type>Dirichlet</type>
+ <parameter>c_Productd</parameter>
+ </boundary_condition>
+ </boundary_conditions>
+ </process_variable>
+ </process_variables>
+ <nonlinear_solvers>
+ <nonlinear_solver>
+ <name>basic_picard</name>
+ <type>Picard</type>
+ <max_iter>10</max_iter>
+ <linear_solver>general_linear_solver</linear_solver>
+ </nonlinear_solver>
+ </nonlinear_solvers>
+ <linear_solvers>
+ <linear_solver>
+ <name>general_linear_solver</name>
+ <!--lis>-i cg -p jacobi -tol 1e-16 -maxiter 20000</lis-->
+ <eigen>
+ <solver_type>BiCGSTAB</solver_type>
+ <precon_type>ILUT</precon_type>
+ <max_iteration_step>10000</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-8 -hc_ksp_max_it 20000</parameters>
+ </petsc-->
+ </linear_solver>
+ </linear_solvers>
+</OpenGeoSysProject>
diff --git a/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d.vtu b/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d.vtu
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--- /dev/null
+++ b/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d.vtu
@@ -0,0 +1,3 @@
+version https://git-lfs.github.com/spec/v1
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+size 547703
diff --git a/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d_pcs_4_ts_0_t_0.000000_expected.vtu b/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d_pcs_4_ts_0_t_0.000000_expected.vtu
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@@ -0,0 +1,3 @@
+version https://git-lfs.github.com/spec/v1
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diff --git a/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d_pcs_4_ts_12_t_1200.000000_expected.vtu b/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d_pcs_4_ts_12_t_1200.000000_expected.vtu
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diff --git a/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d_pcs_4_ts_16_t_1600.000000_expected.vtu b/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/KineticReactant2_2d_pcs_4_ts_16_t_1600.000000_expected.vtu
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@@ -0,0 +1,3 @@
+version https://git-lfs.github.com/spec/v1
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diff --git a/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/test.dat b/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/test.dat
new file mode 100644
index 00000000000..d2b2f4c09ff
--- /dev/null
+++ b/Tests/Data/Parabolic/ComponentTransport/ReactiveTransport/KineticReactant_AllAsComponents/test.dat
@@ -0,0 +1,52 @@
+# name: test data base
+# date: 11.07.2019
+# author: Johanns Boog, Vanessa Montoya
+
+SOLUTION_MASTER_SPECIES
+
+#element species alk gfw_formula element_gfw
+
+E e- 0.0 0.0 0.0
+H H+ -1.0 H 1.008
+H(0) H2 0 H
+H(1) H+ -1.0 0
+O H2O 0 O 16.0
+O(-2) H2O 0 0
+O(0) O2 0 O
+Synthetica Synthetica 0 1 1
+Syntheticb Syntheticb 0 1 1
+Productd Productd 0 1 1
+
+SOLUTION_SPECIES
+
+### Primary Master Species
+e- = e-
+ -log_k 0
+
+H+ = H+
+ -log_k 0
+
+H2O = H2O
+ -log_k 0
+
+Synthetica = Synthetica
+ -log_k 0.0
+
+Syntheticb = Syntheticb
+ -log_k 0.0
+
+Productd = Productd
+ -log_k 0.0
+
+### Secondary Master Species
+
+2 H+ + 2 e- = H2
+ -log_k -3.15
+
+2 H2O - 4 H+ - 4 e- = O2
+ -log_k -86.08
+
+### Aquaeous Species
+
+H2O - H+ = OH-
+ -log_k -13.9951
--
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