diff --git a/web/content/docs/benchmarks/bgr_verification_examples/heatconduction.md b/web/content/docs/benchmarks/bgr_verification_examples/heatconduction/index.md
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diff --git a/web/content/docs/benchmarks/bgr_verification_examples/hydromechanics.md b/web/content/docs/benchmarks/bgr_verification_examples/hydromechanics/index.md
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diff --git a/web/content/docs/benchmarks/bgr_verification_examples/liquid_flow.md b/web/content/docs/benchmarks/bgr_verification_examples/liquid_flow/index.md
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diff --git a/web/content/docs/benchmarks/bgr_verification_examples/mechanics.md b/web/content/docs/benchmarks/bgr_verification_examples/mechanics/index.md
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diff --git a/web/content/docs/benchmarks/bgr_verification_examples/thermohydromechanics.md b/web/content/docs/benchmarks/bgr_verification_examples/thermohydromechanics/index.md
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rename from web/content/docs/benchmarks/bgr_verification_examples/thermohydromechanics.md
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diff --git a/web/content/docs/benchmarks/bgr_verification_examples/thermomechanics.md b/web/content/docs/benchmarks/bgr_verification_examples/thermomechanics/index.md
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rename from web/content/docs/benchmarks/bgr_verification_examples/thermomechanics.md
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diff --git a/web/content/docs/benchmarks/creepbgra/CreepBGRa/index.md b/web/content/docs/benchmarks/creepbgra/CreepBGRa/index.md
index 225410b6a3bfabc1db82538ec7dc34f99cc1c8b4..323808fe362476c5e7c6c7530245a298a115cbaa 100644
--- a/web/content/docs/benchmarks/creepbgra/CreepBGRa/index.md
+++ b/web/content/docs/benchmarks/creepbgra/CreepBGRa/index.md
@@ -190,6 +190,7 @@ A short python snippet, to compute the values.
<summary>
Insert this into Paraview's ProgrammableFilter:
</summary>
+
```python
A = self.GetInputDataObject(0, 0)
numPoints = A.GetNumberOfPoints()
@@ -226,4 +227,5 @@ output.GetPointData().AddArray(outSyy)
output.GetPointData().AddArray(outSzz)
output.GetPointData().AddArray(outSxy)
```
+
</details>
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE_figures/In_out_temperature_comparison.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE/In_out_temperature_comparison.png
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rename from web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE_figures/In_out_temperature_comparison.png
rename to web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE/In_out_temperature_comparison.png
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE.md b/web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE/index.md
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rename from web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE.md
rename to web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE/index.md
index f692d9d23fe33875797e5b01a7ad2a98736d0b29..917f6db4c7fc82615c688278e73299ee5f58425b 100644
--- a/web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE.md
+++ b/web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE/index.md
@@ -38,7 +38,7 @@ For this benchmark, Two different scenarios were carried out by applying two dif
The detailed input parameters can be seen from the 3D_2U_BHE.prj file. The inflow temperature of the BHE, which was imposed as boundary condition of the BHE is shown in Figure 1. All the initial temperatures are set as 22 $^{\circ}$C. The flow rate within each U-pipe is set to $2.0\times10^{-4}$ $\mathrm{m^{3} s^{-1}}$ during the whole simulation time.
-{{< img src="../3D_2U_BHE_figures/In_out_temperature_comparison.png" width="200">}}
+{{< img src="In_out_temperature_comparison.png" width="200">}}
Figure 1: Inflow temperature curve and outflow temperature comparison
@@ -62,7 +62,7 @@ The computed resutls from scenario by adopting the fixed inflow boundary conditi
The OGS numerical outflow temperature over time was compared against results of the FEFLOW software as shown in the Figure 1. And the vertical distributed temperature of circulating water was presented in Figure 2 after operation for 3300 s.
The comparison figures demonstrate that the OGS numerical results and FEFLOW results can match very well and the biggest absolute error of outflow temperature is 0.20 $^{\circ}$C after 360 s' operation, while such error decreases to 0.037 $^{\circ}$C after 3600 s' operation. The maximum relative error of vertical temperature is 0.019 \% after operation for 3300 s.
-{{< img src="../3D_2U_BHE_figures/vertical_temperature_distribution.png" width="200">}}
+{{< img src="vertical_temperature_distribution.png" width="200">}}
Figure 2: Comparison of vertical temperature distribution from scenario by adopting the fixed inflow boundary condition
@@ -75,7 +75,7 @@ Besides, by setting python bindings, the current OGS `Heat_Transport_BHE` proces
In this way, the computed vertical distributed circulating fluid temperature is updated to the black and red solid line illustrated in the figure 3.
It shows that in this case, the difference between the OGS and FEFLOW models is becoming much closer to each other, which is about 0.037 $^{\circ}$C.
-{{< img src="../3D_2U_BHE_figures/vertical_temperature_distribution_powerBC.png" width="200">}}
+{{< img src="vertical_temperature_distribution_powerBC.png" width="200">}}
Figure 3: Comparison of vertical temperature distribution from scenarios by adopting the power boundary conditions
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE_figures/vertical_temperature_distribution.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE/vertical_temperature_distribution.png
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rename from web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE_figures/vertical_temperature_distribution.png
rename to web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE/vertical_temperature_distribution.png
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE_figures/vertical_temperature_distribution_powerBC.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE/vertical_temperature_distribution_powerBC.png
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rename from web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE_figures/vertical_temperature_distribution_powerBC.png
rename to web/content/docs/benchmarks/heat-transport-bhe/3D_2U_BHE/vertical_temperature_distribution_powerBC.png
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array_figures/BHE_network.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array/BHE_network.png
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rename from web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array_figures/BHE_network.png
rename to web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array/BHE_network.png
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array_figures/BHE_network_closedloop.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array/BHE_network_closedloop.png
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diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array_figures/Heat_extraction_rate.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array/Heat_extraction_rate.png
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diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array_figures/Heat_extraction_rate_closedloop.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array/Heat_extraction_rate_closedloop.png
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diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array_figures/Inflow_and_outflow_temperature.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array/Inflow_and_outflow_temperature.png
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diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array_figures/Inflow_temperature_and_flow_rate.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array/Inflow_temperature_and_flow_rate.png
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diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array_figures/Soil_temperature.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array/Soil_temperature.png
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rename from web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array_figures/Soil_temperature.png
rename to web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array/Soil_temperature.png
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array.md b/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array/index.md
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rename from web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array.md
rename to web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array/index.md
index e3236781da346b05d901ee543b4c69a0c0e8c52d..b6e29c1f28876c60de2d809eb8388ce3d99b00df 100644
--- a/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array.md
+++ b/web/content/docs/benchmarks/heat-transport-bhe/3D_3BHEs_array/index.md
@@ -80,7 +80,7 @@ During the calculation of the TESPy solver, the flow density and the related spe
To check their concrete value under specific temperature and pressure conditions, interested readers may refer to e.g. the 'PropsSI' function introduced in the webpage of CoolProp.
For the fast execution of this benchmark, the total simulation time is shorten to 600 seconds. If the reader wishes to reproduce the same results, a full simulation of 6 months needs to be performed.
-{{< img src="../3D_3BHEs_array_figures/BHE_network.png" width="200">}}
+{{< img src="BHE_network.png" width="200">}}
Figure 1a: One-way pipeline network model
@@ -90,7 +90,7 @@ The setup for a closed-loop network model is illustrated in Figure 1b.
Compared to the configuration in the one-way network, the refrigerant in the closed loop network is circulating through the entire system.
In this case, the flow rate will be automatically adjusted by the water pump in each time step, as its pressure head is directly linked to the flow rate. Subsequently, the flow rate is determined by the pressure losses in the BHE array.
-{{< img src="../3D_3BHEs_array_figures/BHE_network_closedloop.png" width="200">}}
+{{< img src="BHE_network_closedloop.png" width="200">}}
Figure 1b: Closed-loop pipeline network model
@@ -114,24 +114,24 @@ Except for the thermal shifiting behavior among the BHEs, the averaged heat extr
This is due to the fact that additional energy is required to compensate the hydraulic loss of the pipe.
-{{< img src="../3D_3BHEs_array_figures/Soil_temperature.png" width="200">}}
+{{< img src="Soil_temperature.png" width="200">}}
Figure 2: Evolution of the soil temperature located at the 1 m distance away from each BHE
-{{< img src="../3D_3BHEs_array_figures/Inflow_and_outflow_temperature.png" width="200">}}
+{{< img src="Inflow_and_outflow_temperature.png" width="200">}}
Figure 3: Evolution of the inflow and outflow refrigerant temperature of each BHE
-{{< img src="../3D_3BHEs_array_figures/Heat_extraction_rate.png" width="200">}}
+{{< img src="Heat_extraction_rate.png" width="200">}}
Figure 4: Evolution of the heat extraction rate of each BHE
-{{< img src="../3D_3BHEs_array_figures/Inflow_temperature_and_flow_rate.png" width="200">}}
+{{< img src="Inflow_temperature_and_flow_rate.png" width="200">}}
Figure 5: Evolution of the inflow refrigerant temperature and flow rate entering the BHE array
-{{< img src="../3D_3BHEs_array_figures/Heat_extraction_rate_closedloop.png" width="200">}}
+{{< img src="Heat_extraction_rate_closedloop.png" width="200">}}
Figure 6: Evolution of the heat extraction rate of each BHE with close loop network model
## References
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/BHE_GW_advection_2years.zip b/web/content/docs/benchmarks/heat-transport-bhe/3D_BHE_GW_advection/BHE_GW_advection_2years.zip
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rename from web/content/docs/benchmarks/heat-transport-bhe/BHE_GW_advection_2years.zip
rename to web/content/docs/benchmarks/heat-transport-bhe/3D_BHE_GW_advection/BHE_GW_advection_2years.zip
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_BHE_GW_advection.md b/web/content/docs/benchmarks/heat-transport-bhe/3D_BHE_GW_advection/index.md
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rename from web/content/docs/benchmarks/heat-transport-bhe/3D_BHE_GW_advection.md
rename to web/content/docs/benchmarks/heat-transport-bhe/3D_BHE_GW_advection/index.md
index 27a633b9c4f120a70b337c74a6fef1676b964472..faf1655c28d0c1d99422cd03a303c2f3baa6bbf8 100644
--- a/web/content/docs/benchmarks/heat-transport-bhe/3D_BHE_GW_advection.md
+++ b/web/content/docs/benchmarks/heat-transport-bhe/3D_BHE_GW_advection/index.md
@@ -52,7 +52,7 @@ induced ground temperature.
## Model Setup
The input files for the full simulation including the analytical solution for
-the soil temperature can be found [here](../BHE_GW_advection_2years.zip). The
+the soil temperature can be found [here](BHE_GW_advection_2years.zip). The
geometry of the model is
illustrated in Figure 1. The depth of the model domain is 15 m with an areal
extent of 80 m x 80 m. The BHE is 1U-type and is
@@ -76,7 +76,7 @@ The BHE parameters are only relevant for the numerical model and are adopted
from the [3D Beier sandbox
benchmark]({{< ref "3D_Beier_sandbox.md" >}}).
-{{< img src="../3D_BHE_GW_advection_figures/mesh.png" width="150">}}
+{{< img src="mesh.png" width="150">}}
Figure 1: Geometry and mesh of the BHE model
@@ -90,12 +90,12 @@ and analytical solution match very well as the maximum relative error of
ground temperature is less than 0.2 \%. The largest difference is found near
the BHE node towards which the analytical solution approaches infinity.
-{{< img src="../3D_BHE_GW_advection_figures/temperature_soil_2years.png"
+{{< img src="temperature_soil_2years.png"
width="150">}}
Figure 2: Ground temperature distribution after two years at $z=-7$ m.
-{{< img src="../3D_BHE_GW_advection_figures/rel_err.png" width="150">}}
+{{< img src="rel_err.png" width="150">}}
Figure 3: Comparison of OGS-6 results and analytical solution. Note the
singularity of the analytical solution at the BHE node.
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_BHE_GW_advection_figures/mesh.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_BHE_GW_advection/mesh.png
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rename from web/content/docs/benchmarks/heat-transport-bhe/3D_BHE_GW_advection_figures/mesh.png
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diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_BHE_GW_advection_figures/rel_err.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_BHE_GW_advection/rel_err.png
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diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_BHE_GW_advection_figures/temperature_soil_2years.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_BHE_GW_advection/temperature_soil_2years.png
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diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox_figures/Inflow_temp.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox/Inflow_temp.png
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diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox_figures/comparison_with_experiment_data_and_OGS5.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox/comparison_with_experiment_data_and_OGS5.png
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rename from web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox_figures/comparison_with_experiment_data_and_OGS5.png
rename to web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox/comparison_with_experiment_data_and_OGS5.png
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox.md b/web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox/index.md
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rename from web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox.md
rename to web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox/index.md
index 1700fb1081a89b974accda935548ce0f927b36ba..57206dc67d79499c0c5b159b6853bffb860e8db0 100644
--- a/web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox.md
+++ b/web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox/index.md
@@ -34,7 +34,7 @@ The numerical model was established using dual continuum method Diersch et al. (
| Grout thermal conductivity | $\lambda_{g}$ | 0.806 | $\mathrm{W m^{-1} K^{-1}}$ |
| Grout heat capacity | $(\rho c)_{grout}$ | $3.8\times10^{6}$ | $\mathrm{Jm^{-3}K^{-1}}$ |
-{{< img src="../3D_Beier_sandbox_figures/numerical_geometry_of_BHE.png" width="200">}}
+{{< img src="numerical_geometry_of_BHE.png" width="200">}}
Figure 1: Sandbox model
@@ -44,7 +44,7 @@ In Beier's experiment, the inner diameter of aluminum pipe is 12.6 $\mathrm{cm}$
The detailed input file can be seen from the .prj file. The inflow temperature of the BHE, which was imposed as boundary condition of the BHE can be shown in Figure 2. Initial conditions of inflow and outflow temperature for the BHE were directly obtained from the measurements at t=0. For the initial soil temperature, the average value of all sensors placed in the sand and the borehole wall was set in the numerical model.
-{{< img src="../3D_Beier_sandbox_figures/Inflow_temp.png" width="200">}}
+{{< img src="Inflow_temp.png" width="200">}}
Figure 2: Inflow temperature curve as the BHE boundary condition
@@ -52,11 +52,11 @@ Figure 2: Inflow temperature curve as the BHE boundary condition
The numerical outflow temperature of OGS-5 (Shao et al. (2016)) and OGS-6 was compared with the experimental results, which is presented in the Figure 3. And the soil temperature at different locations among experimental and numerical results were compared and shown in the Figure 4. The comparison figures demonstrate that the numerical results and experimental data can fit very well and the largest relative error is 0.17\% on the wall temperature and 0.014\% on the outflow temperature. The initial temperature of borehole wall in numerical model was set an average value as mentioned in the above, which has initial error of 0.07 K compared to the experimental data. Besides, normally, the error of measuring temperatures during experiment, difference on the real thermal physical parameters of the sand and the BHE are all at the same value range. Therefore, it can be concluded that the numerical model of 1U-type BHE is fully verified.
-{{< img src="../3D_Beier_sandbox_figures/comparison_with_experiment_data_and_OGS5.png" width="200">}}
+{{< img src="comparison_with_experiment_data_and_OGS5.png" width="200">}}
Figure 3: Comparison with experiment and OGS-5 results regarding outflow temperature of the BHE
-{{< img src="../3D_Beier_sandbox_figures/soil_temp_comparison.png" width="200">}}
+{{< img src="soil_temp_comparison.png" width="200">}}
Figure 4: Comparison of modelled and measured wall and soil temperatures
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox_figures/numerical_geometry_of_BHE.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox/numerical_geometry_of_BHE.png
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diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox_figures/soil_temp_comparison.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_Beier_sandbox/soil_temp_comparison.png
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diff --git a/web/content/docs/benchmarks/heat-transport-bhe/Analytical_coaxial_BHE.zip b/web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE/Analytical_coaxial_BHE.zip
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diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE_figures/coaxial_deep_BHE.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE/coaxial_deep_BHE.png
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diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE.md b/web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE/index.md
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rename from web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE.md
rename to web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE/index.md
index 74f0890f9e28135a33b646f4cb169ee75f96fcad..56ae730af120b57965ebcac83f592ba4f6b80998 100644
--- a/web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE.md
+++ b/web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE/index.md
@@ -17,7 +17,7 @@ project = "Parabolic/T/3D_deep_BHE/3D_deep_BHE_CXA.prj"
In recent years, Borehole Heat Exchangers (BHE) are very widely utilized to extract geothermal energy for building heating. For coaxial type of BHEs, an inner pipe is installed inside of an outer pipe, allowing the downward and upward flow to be separated. In some projects, very long coaxial BHEs are installed down to a 2-km depth, in order to extract more energy from the deep subsurface (Kong et al., 2017). Based on the flow directions, there are two types of coaxial BHEs. When downward flow is located in the inner pipe, it is called Coaxial-Centred (CXC) type. On the countary, if the inflow is introduced in the annular space, it is called a CXA type. Detailed schematization of the CXA-type BHE system is shown in Figure 1. In this benchmark, the numerical model in OGS-6 has been tested for the 2 coaxial types of BHEs. The simulation results are compared with previous OGS-5 results and also the analytical solution proposed by [Beier et al. (2014)](../Analytical_coaxial_BHE.zip).
-{{< img src="../3D_coaxial_deep_BHE_figures/coaxial_deep_BHE.png" width="200">}}
+{{< img src="coaxial_deep_BHE.png" width="200">}}
Figure 1: Coaxial BHE of CXA (Kong et al. (2017))
@@ -40,7 +40,7 @@ The implemented numerical model was established based on the dual continuum appr
| Grout thermal conductivity | $\lambda_{g}$ | 0.73 | $\mathrm{W m^{-1} K^{-1}}$ |
| Grout heat capacity | $(\rho c)_{g}$ | $3.8\times10^{6}$ | $\mathrm{Jm^{-3}K^{-1}}$ |
-{{< img src="../3D_coaxial_deep_BHE_figures/numerical_geometry_model.png" width="80">}}
+{{< img src="numerical_geometry_model.png" width="80">}}
Figure 2: Geometry and mesh of the coaxial BHE model
@@ -56,11 +56,11 @@ where $\rho^r c^r$ is heat capacity of circulating fluid and $Q^r$ is circulatin
In Figure 3, the numerically simulated outflow temperature from OGS-6 was compared against the OGS-5 result, as well as the analytical solution by Beier et al. (2014). Also, the temperature distribution of circulating water inside of the BHE after 3000 seconds was presented in Figure 4. The comparison demonstrates that the numerical results and analytical solution can match very well and the biggest absolute error of outflow temperature is around 1.6 $^{\circ}$C at the starting up stage, while such error will decrease to around 0.5 $^{\circ}$C after 30 days' operation. The maximum relative error regarding temperature distribution of circulating water after operation for 3000 s is around 2 \%. The soil temperature verification can be seen in the Benchmark of 3D Beier sandbox.
-{{< img src="../3D_coaxial_deep_BHE_figures/outflow_temperature_over_time_long-term.png" width="120">}}
+{{< img src="outflow_temperature_over_time_long-term.png" width="120">}}
Figure 3: Comparison with analytical solution and OGS-5 results
-{{< img src="../3D_coaxial_deep_BHE_figures/temperature_distribution_3000s.png" width="200">}}
+{{< img src="temperature_distribution_3000s.png" width="200">}}
Figure 4: Distributed temperature of circulating water
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE_figures/numerical_geometry_model.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE/numerical_geometry_model.png
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rename from web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE_figures/numerical_geometry_model.png
rename to web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE/numerical_geometry_model.png
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE_figures/outflow_temperature_over_time_long-term.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE/outflow_temperature_over_time_long-term.png
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rename from web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE_figures/outflow_temperature_over_time_long-term.png
rename to web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE/outflow_temperature_over_time_long-term.png
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE_figures/temperature_distribution_3000s.png b/web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE/temperature_distribution_3000s.png
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rename from web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE_figures/temperature_distribution_3000s.png
rename to web/content/docs/benchmarks/heat-transport-bhe/3D_coaxial_deep_BHE/temperature_distribution_3000s.png
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/Analytical_wellbore_heat_transport.zip b/web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE/Analytical_wellbore_heat_transport.zip
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rename from web/content/docs/benchmarks/heat-transport-bhe/Analytical_wellbore_heat_transport.zip
rename to web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE/Analytical_wellbore_heat_transport.zip
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE_figures/T_out_comparison.png b/web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE/T_out_comparison.png
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rename from web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE_figures/T_out_comparison.png
rename to web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE/T_out_comparison.png
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE_figures/absolute_error_fluid_T_30d.png b/web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE/absolute_error_fluid_T_30d.png
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rename from web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE_figures/absolute_error_fluid_T_30d.png
rename to web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE/absolute_error_fluid_T_30d.png
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE.md b/web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE/index.md
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rename from web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE.md
rename to web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE/index.md
index 8714d87ad72d1722d8cf71f6a4daad8888e4c3a3..31f9c7121b8b19e005c545446fad8159e5db6111 100644
--- a/web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE.md
+++ b/web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE/index.md
@@ -15,13 +15,13 @@ project = "Parabolic/T/BHE_1P/BHE_1P.prj"
## Problem description
-Ramey (Ramey et al. (1962)) proposed the analytical solution concerning the wellbore heat transmission, which can be used to quantify the fluid temperature change in the wellbore. In order to verify the single pipe flow model in the OGS, the numerical results was compared with the [Ramey's analytical solution](../Analytical_wellbore_heat_transport.zip). The detailed calculation of the Ramey's analytical solution is given below.
+Ramey (Ramey et al. (1962)) proposed the analytical solution concerning the wellbore heat transmission, which can be used to quantify the fluid temperature change in the wellbore. In order to verify the single pipe flow model in the OGS, the numerical results was compared with the [Ramey's analytical solution](Analytical_wellbore_heat_transport.zip). The detailed calculation of the Ramey's analytical solution is given below.
## Model Setup
In this benchmark, the length of the wellbore is 30 m as shown in Figure 1 and the cold water is injected into the inlet point of the wellbore with temperature of 20 $^{\circ}$C. The initial temperature of the fluid and grout in the wellbore is 20 $^{\circ}$C, and temperature of the surrounding rock is 55 $^{\circ}$C. The wellbore and pipe diameter are 0.28 m and 0.25826 m, respectively. And the flow rate is 0.0002 $m^3/s$.
-{{< img src="../pipe_flow_EBHE_figures/pipe_flow_3d_model.png" width="80">}}
+{{< img src="pipe_flow_3d_model.png" width="80">}}
Figure 1: Single pipe flow model
@@ -84,11 +84,11 @@ The outlet temperature change over time was compared against analytical solution
In numerical model, the outlet temperature at beginning stage is affected by the initial temperature in the pipe inside the wellbore. The initial fluid temperature set in the benchmark means there is water with 20 $^{\circ}$C filled in the wellbore already before injecting water into the wellbore. But in the analytical solution, no initial temperature is set and the temperature keeps equilibrium state at every moment. The impact of initial temperature condition in numerical model is decreasing with increasement of the operational time as shown in Figure 2.
-{{< img src="../pipe_flow_EBHE_figures/T_out_comparison.png" width="120">}}
+{{< img src="T_out_comparison.png" width="120">}}
Figure 2: Comparison with analytical solution results
-{{< img src="../pipe_flow_EBHE_figures/absolute_error_fluid_T_30d.png" width="200">}}
+{{< img src="absolute_error_fluid_T_30d.png" width="200">}}
Figure 3: Distributed temperature of fluid and absolute error.
diff --git a/web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE_figures/pipe_flow_3d_model.png b/web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE/pipe_flow_3d_model.png
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rename from web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE_figures/pipe_flow_3d_model.png
rename to web/content/docs/benchmarks/heat-transport-bhe/pipe_flow_EBHE/pipe_flow_3d_model.png
diff --git a/web/content/docs/benchmarks/heatconduction/bhe_array_analytical_solver.py b/web/content/docs/benchmarks/heatconduction/BHE_array_benchmark/bhe_array_analytical_solver.py
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rename from web/content/docs/benchmarks/heatconduction/bhe_array_analytical_solver.py
rename to web/content/docs/benchmarks/heatconduction/BHE_array_benchmark/bhe_array_analytical_solver.py
diff --git a/web/content/docs/benchmarks/heatconduction/bhe_array_benchmark.bib b/web/content/docs/benchmarks/heatconduction/BHE_array_benchmark/bhe_array_benchmark.bib
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rename from web/content/docs/benchmarks/heatconduction/bhe_array_benchmark.bib
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diff --git a/web/content/docs/benchmarks/heatconduction/BHE_array_benchmark_figures/figure_1.png b/web/content/docs/benchmarks/heatconduction/BHE_array_benchmark/figure_1.png
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diff --git a/web/content/docs/benchmarks/heatconduction/BHE_array_benchmark_figures/figure_4.png b/web/content/docs/benchmarks/heatconduction/BHE_array_benchmark/figure_4.png
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rename from web/content/docs/benchmarks/heatconduction/BHE_array_benchmark_figures/figure_4.png
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diff --git a/web/content/docs/benchmarks/heatconduction/BHE_array_benchmark_figures/figure_5.png b/web/content/docs/benchmarks/heatconduction/BHE_array_benchmark/figure_5.png
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rename from web/content/docs/benchmarks/heatconduction/BHE_array_benchmark_figures/figure_5.png
rename to web/content/docs/benchmarks/heatconduction/BHE_array_benchmark/figure_5.png
diff --git a/web/content/docs/benchmarks/heatconduction/BHE_array_benchmark.md b/web/content/docs/benchmarks/heatconduction/BHE_array_benchmark/index.md
similarity index 96%
rename from web/content/docs/benchmarks/heatconduction/BHE_array_benchmark.md
rename to web/content/docs/benchmarks/heatconduction/BHE_array_benchmark/index.md
index d9fb7bb7905bd25e158de86cc4553186b7e6756d..231516dfb9da4b564a7ff2df9826cff076f0dc4d 100644
--- a/web/content/docs/benchmarks/heatconduction/BHE_array_benchmark.md
+++ b/web/content/docs/benchmarks/heatconduction/BHE_array_benchmark/index.md
@@ -57,7 +57,7 @@ In this model, the quad element was adopted to compose the mesh. The initial tem
| Heat extraction rate of the BHE | $q$ | $35$ | $W/m$ |
| Diameter of the BHE | $D$ | $0.15$ | $m$ |
-{{< img src="../BHE_array_benchmark_figures/figure_1.png" >}}
+{{< img src="figure_1.png" >}}
Figure 1: Model geometry, BHE location, and the observation profile
@@ -85,21 +85,21 @@ where $r_b$ is the BHE radius. n denotes the number of surrounding nodes. n =Â 8
Figure 2 and 3 show the comparison of the temperature distribution along the observation profile (position see Figure 1) using analytical solution with the numerical results from OGS5 and OGS6 for every 4 months in the whole simulated time. It shows the numerical solution has a very good agreement with the analytical solution.
-{{< img src="../BHE_array_benchmark_figures/figure_2.png" width="200">}}
+{{< img src="figure_2.png" width="200">}}
Figure 2: The temperature evolution of the BHEs field along the observation profile
-{{< img src="../BHE_array_benchmark_figures/figure_3.png" width="200">}}
+{{< img src="figure_3.png" width="200">}}
Figure 3: The temperature evolution of the BHEs field along the observation profile
In order to investigate the impact of mesh density on the accuracy of numerical result, the simulated temperature profile at the observation point A (53 m, 52.5 m) was plotted and compared against the analytical solution. Figure 3 shows the relative difference of the computed temperature between the analytical and numerical solution by using different mesh size (2.5 m, 1 m, 0.5 m, 0.25 m and 0.2 m). The results show that the difference becomes smaller when the mesh size is approaching 0.5 m, which is expected as the optimal mesh size mentioned in Diersch et al. (2011). From Figure 4, it can be found that the absolute error of temperature values at point A should be less than 2.5e-3 if the mesh size is kept denser than 0.5m.
-{{< img src="../BHE_array_benchmark_figures/figure_4.png" width="200">}}
+{{< img src="figure_4.png" width="200">}}
Figure 4: The relative difference of computed temperature at point A between the analytical and numerical solution using different mesh size
-{{< img src="../BHE_array_benchmark_figures/figure_5.png" width="200">}}
+{{< img src="figure_5.png" width="200">}}
Figure 5: The absolute difference of computed temperature along the diagonal profile between the analytical and numerical solution using different mesh size
diff --git a/web/content/docs/benchmarks/heatconduction/heatconduction-dirichlet.md b/web/content/docs/benchmarks/heatconduction/heatconduction-dirichlet/index.md
similarity index 98%
rename from web/content/docs/benchmarks/heatconduction/heatconduction-dirichlet.md
rename to web/content/docs/benchmarks/heatconduction/heatconduction-dirichlet/index.md
index 5d1d8bf17f86157c1891f3a52ee4d5b4e9860e17..3f50d4489b6939cf56b2ebe60540946fea9b2868 100644
--- a/web/content/docs/benchmarks/heatconduction/heatconduction-dirichlet.md
+++ b/web/content/docs/benchmarks/heatconduction/heatconduction-dirichlet/index.md
@@ -70,4 +70,4 @@ The result, written in the `.vtu` file, can be visualized with Paraview, for exa
Loading the `line_60_heat_pcs_0_ts_65_t_5078125.000000.vtu` file in Paraview and Plotting over line. Compared to the analytical solution 'temperature_analytical.vtu', the results are very good:
-{{< img src="../validation-1.png" >}}
+{{< img src="validation-1.png" >}}
diff --git a/web/content/docs/benchmarks/heatconduction/validation-1.png b/web/content/docs/benchmarks/heatconduction/heatconduction-dirichlet/validation-1.png
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rename from web/content/docs/benchmarks/heatconduction/validation-1.png
rename to web/content/docs/benchmarks/heatconduction/heatconduction-dirichlet/validation-1.png
diff --git a/web/content/docs/benchmarks/heatconduction/LineSourceTermFigures/comparison_plot_over_line_diff_analytical_solution_temperature_and_simulated_temperature_line_source_term_in_cylinder.png b/web/content/docs/benchmarks/heatconduction/heatconduction-line_source_term/comparison_plot_over_line_diff_analytical_solution_temperature_and_simulated_temperature_line_source_term_in_cylinder.png
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rename from web/content/docs/benchmarks/heatconduction/LineSourceTermFigures/comparison_plot_over_line_diff_analytical_solution_temperature_and_simulated_temperature_line_source_term_in_cylinder.png
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diff --git a/web/content/docs/benchmarks/heatconduction/LineSourceTermFigures/comparison_plot_over_line_rel_diff_analytical_solution_temperature_and_simulated_temperature_line_source_term_in_cylinder.png b/web/content/docs/benchmarks/heatconduction/heatconduction-line_source_term/comparison_plot_over_line_rel_diff_analytical_solution_temperature_and_simulated_temperature_line_source_term_in_cylinder.png
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rename from web/content/docs/benchmarks/heatconduction/LineSourceTermFigures/comparison_plot_over_line_rel_diff_analytical_solution_temperature_and_simulated_temperature_line_source_term_in_cylinder.png
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diff --git a/web/content/docs/benchmarks/heatconduction/heatconduction-line_source_term.md b/web/content/docs/benchmarks/heatconduction/heatconduction-line_source_term/index.md
similarity index 81%
rename from web/content/docs/benchmarks/heatconduction/heatconduction-line_source_term.md
rename to web/content/docs/benchmarks/heatconduction/heatconduction-line_source_term/index.md
index 16ddfb9728b5d1f87649c57d6429e1d77d34d5ba..3a8958ce3da0b1bc7590f4fd13bec9de9f152768 100644
--- a/web/content/docs/benchmarks/heatconduction/heatconduction-line_source_term.md
+++ b/web/content/docs/benchmarks/heatconduction/heatconduction-line_source_term/index.md
@@ -43,7 +43,7 @@ is sketched. Furthermore, the mesh resolution is shown in the cylindrical domain
within the first quadrant of the coordinate system. In the second quadrant the
simulated temperature distribution is depicted.
-{{< img src="../LineSourceTermFigures/temperature_distribution_line_source_term_in_cylinder.png" >}}
+{{< img src="temperature_distribution_line_source_term_in_cylinder.png" >}}
The source term is defined along the line in the center of the cylinder:
$$
@@ -74,7 +74,7 @@ if (coordsX^2<0.0001 & coordsY^2<0.0001, temperature, -1/(4*asin(1))*ln(sqrt(coo
The following plot shows the temperature along the white line in the figure above.
-{{< img src="../LineSourceTermFigures/temperature_profile_line_source_term_in_cylinder.png" >}}
+{{< img src="temperature_profile_line_source_term_in_cylinder.png" >}}
- Comparison with analytical solution:
@@ -82,12 +82,12 @@ The differences of analytical and computed solutions for two different domain
discretizations are small outside of the center. In the finer mesh the error
outside of the middle region is smaller than in the coarser mesh.
{{< img
-src="../LineSourceTermFigures/comparison_plot_over_line_diff_analytical_solution_temperature_and_simulated_temperature_line_source_term_in_cylinder.png" >}}
+src="comparison_plot_over_line_diff_analytical_solution_temperature_and_simulated_temperature_line_source_term_in_cylinder.png" >}}
Due to the numerical evaluation of the relative error of the computed solution
the error grows in the vicinity of the boundary and in the center.
{{< img
-src="../LineSourceTermFigures/comparison_plot_over_line_rel_diff_analytical_solution_temperature_and_simulated_temperature_line_source_term_in_cylinder.png" >}}
+src="comparison_plot_over_line_rel_diff_analytical_solution_temperature_and_simulated_temperature_line_source_term_in_cylinder.png" >}}
#### Input files
@@ -108,18 +108,18 @@ $r=1$ is solved. The cylindrical domain is defined as axisymmetric.
#### Results and evaluation
{{< img
-src="../LineSourceTermFigures/simulated_temperature_distribution_line_source_term_in_axisymmetric_cylinder.png" >}}
+src="simulated_temperature_distribution_line_source_term_in_axisymmetric_cylinder.png" >}}
The above figure shows the computed temperature distribution.
The following plot shows the temperature along the white line in the figure above.
{{< img
-src="../LineSourceTermFigures/temperature_profile_line_source_term_in_axisymmetric_cylinder.png" >}}
+src="temperature_profile_line_source_term_in_axisymmetric_cylinder.png" >}}
The error and relative error shows the same behaviour like in the simulation
models above. Outside of the center, that has a singularity in the analytical
solution, the errors decreases very fast.
{{< img
-src="../LineSourceTermFigures/plot_over_line_diff_and_rel_diff_analytical_solution_temperature_and_simulated_temperature_line_source_term_in_axisymmetric_cylinder.png" >}}
+src="plot_over_line_diff_and_rel_diff_analytical_solution_temperature_and_simulated_temperature_line_source_term_in_axisymmetric_cylinder.png" >}}
#### Input files
diff --git a/web/content/docs/benchmarks/heatconduction/LineSourceTermFigures/plot_over_line_diff_and_rel_diff_analytical_solution_temperature_and_simulated_temperature_line_source_term_in_axisymmetric_cylinder.png b/web/content/docs/benchmarks/heatconduction/heatconduction-line_source_term/plot_over_line_diff_and_rel_diff_analytical_solution_temperature_and_simulated_temperature_line_source_term_in_axisymmetric_cylinder.png
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diff --git a/web/content/docs/benchmarks/heatconduction/LineSourceTermFigures/simulated_temperature_distribution_line_source_term_in_axisymmetric_cylinder.png b/web/content/docs/benchmarks/heatconduction/heatconduction-line_source_term/simulated_temperature_distribution_line_source_term_in_axisymmetric_cylinder.png
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diff --git a/web/content/docs/benchmarks/heatconduction/LineSourceTermFigures/temperature_profile_line_source_term_in_cylinder.png b/web/content/docs/benchmarks/heatconduction/heatconduction-line_source_term/temperature_profile_line_source_term_in_cylinder.png
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diff --git a/web/content/docs/benchmarks/heatconduction/heatconduction-neumann.md b/web/content/docs/benchmarks/heatconduction/heatconduction-neumann/index.md
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rename from web/content/docs/benchmarks/heatconduction/heatconduction-neumann.md
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index b2dd6917ef73fe6cc1a88a84cdc9083cbb7d5710..ef60d8909f971f7aeaa9e8e88b9402036809b0cd 100644
--- a/web/content/docs/benchmarks/heatconduction/heatconduction-neumann.md
+++ b/web/content/docs/benchmarks/heatconduction/heatconduction-neumann/index.md
@@ -76,8 +76,8 @@ tolerances.
| | |
|----------|--------------------|
-| {{< img title="Time step 1, time 78125s." src="../picard_vs_newton_ts_1_t_78125.png" >}} | {{< img title="Time step 3, time 234375s." src="../picard_vs_newton_ts_3_t_234375.png" >}} |
-| {{< img title="Time step 65, time 5078125s." src="../picard_vs_newton_ts_65_t_5078125.png" >}} | {{< img title="Time step 405, time 31640625s." src="../picard_vs_newton_ts_405_t_31640625.png" >}} |
+| {{< img title="Time step 1, time 78125s." src="picard_vs_newton_ts_1_t_78125.png" >}} | {{< img title="Time step 3, time 234375s." src="picard_vs_newton_ts_3_t_234375.png" >}} |
+| {{< img title="Time step 65, time 5078125s." src="picard_vs_newton_ts_65_t_5078125.png" >}} | {{< img title="Time step 405, time 31640625s." src="picard_vs_newton_ts_405_t_31640625.png" >}} |
### Mass-lumping and analytical solution
@@ -86,5 +86,5 @@ on cost of accuracy as the error is significantly larger.
| | |
|----------|--------------------|
-| {{< img title="Time step 1, time 78125s." src="../temperature_error_ts_1_t_78125.png" >}} | {{< img title="Time step 3, time 234375s." src="../temperature_error_ts_3_t_234375.png" >}} |
-| {{< img title="Time step 65, time 5078125s." src="../temperature_error_ts_65_t_5078125.png" >}} | {{< img title="Time step 405, time 31640625s." src="../temperature_error_ts_405_t_31640625.png" >}} |
+| {{< img title="Time step 1, time 78125s." src="temperature_error_ts_1_t_78125.png" >}} | {{< img title="Time step 3, time 234375s." src="temperature_error_ts_3_t_234375.png" >}} |
+| {{< img title="Time step 65, time 5078125s." src="temperature_error_ts_65_t_5078125.png" >}} | {{< img title="Time step 405, time 31640625s." src="temperature_error_ts_405_t_31640625.png" >}} |
diff --git a/web/content/docs/benchmarks/heatconduction/picard_vs_newton_ts_1_t_78125.png b/web/content/docs/benchmarks/heatconduction/heatconduction-neumann/picard_vs_newton_ts_1_t_78125.png
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diff --git a/web/content/docs/benchmarks/heatconduction/picard_vs_newton_ts_3_t_234375.png b/web/content/docs/benchmarks/heatconduction/heatconduction-neumann/picard_vs_newton_ts_3_t_234375.png
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diff --git a/web/content/docs/benchmarks/heatconduction/temperature_error_ts_1_t_78125.png b/web/content/docs/benchmarks/heatconduction/heatconduction-neumann/temperature_error_ts_1_t_78125.png
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diff --git a/web/content/docs/benchmarks/heatconduction/temperature_error_ts_3_t_234375.png b/web/content/docs/benchmarks/heatconduction/heatconduction-neumann/temperature_error_ts_3_t_234375.png
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diff --git a/web/content/docs/benchmarks/hydro-component/heterogeneous/comparison_2d.png b/web/content/docs/benchmarks/hydro-component/HC_ogs6-vs-ogs5/comparison_2d.png
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rename from web/content/docs/benchmarks/hydro-component/heterogeneous/concentration_3d.png
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diff --git a/web/content/docs/benchmarks/hydro-component/HC_ogs6-vs-ogs5.md b/web/content/docs/benchmarks/hydro-component/HC_ogs6-vs-ogs5/index.md
similarity index 73%
rename from web/content/docs/benchmarks/hydro-component/HC_ogs6-vs-ogs5.md
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index 062f00e8b2027c406daa23bf077078794e57cc00..214f1a1472c99ae7ca2715decfaac9c1c79ee809 100644
--- a/web/content/docs/benchmarks/hydro-component/HC_ogs6-vs-ogs5.md
+++ b/web/content/docs/benchmarks/hydro-component/HC_ogs6-vs-ogs5/index.md
@@ -25,20 +25,20 @@ The setups are steady-state for flow, with an extent of a $100$ m x $100$ m hori
Porosity is $0.01$, specific storage is $0$, fluid density is $1000$ kg$\cdot$m$^3$, dynamic viscosity is $10^{-3}$ Pa$\cdot$s, molecular diffusion coefficient is $2\cdot 10^{-9}$ m$\cdot$s$^{-2}$, dispersivities are longitudinal $1$ m and transverse $0.1$ m. The heterogeneous parameter fields of intrinsic permeability are shown in the figures below; creation of the tensor field is documented [here](https://github.com/ufz/ogs-utils/tree/master/post/merge-scalar-data-arrays).
-{{< img src="../heterogeneous/permeability_2d.png" title="Magnitude of isotropic permeability tensor for 2D setup.">}}
-{{< img src="../heterogeneous/permeability_3d.png" title="Magnitude of isotropic permeability tensor for 3D setup.">}}
+{{< img src="permeability_2d.png" title="Magnitude of isotropic permeability tensor for 2D setup.">}}
+{{< img src="permeability_3d.png" title="Magnitude of isotropic permeability tensor for 3D setup.">}}
### Model results
The comparison of velocity and hydraulic head are shown below. The numerical results of OGS6 fit very well to the OGS5 results with relative differences for velocity in the order of ca $10^{-2}$ and for hydraulic head in $10^{-4}$.
-{{< img src="../heterogeneous/comparison_2d.png" title="Relative differences of 2D simulation results between OGS5 and OGS6. On the top left figure, white lines represent hydraulic head values of OGS5, blue lines of OGS6.">}}
-{{< img src="../heterogeneous/comparison_3d.png" title="Relative differences of 3D simulation results between OGS5 and OGS6. On the top left figure, grey dots represent hydraulic head values of OGS6.">}}
+{{< img src="comparison_2d.png" title="Relative differences of 2D simulation results between OGS5 and OGS6. On the top left figure, white lines represent hydraulic head values of OGS5, blue lines of OGS6.">}}
+{{< img src="comparison_3d.png" title="Relative differences of 3D simulation results between OGS5 and OGS6. On the top left figure, grey dots represent hydraulic head values of OGS6.">}}
The mass transport simulation results (figures below) show an expected heterogeneous mass front moving through the domain.
-{{< img src="../heterogeneous/concentration_2d.png" title="Concentration distribution at simulation time $1e8$ s for the 2D setup.">}}
-{{< img src="../heterogeneous/concentration_3d.png" title="Concentration distribution at simulation time $1e8$ s for the 3D setup.">}}
+{{< img src="concentration_2d.png" title="Concentration distribution at simulation time $1e8$ s for the 2D setup.">}}
+{{< img src="concentration_3d.png" title="Concentration distribution at simulation time $1e8$ s for the 3D setup.">}}
[The project files for the 2D setup are here.]({{< data-url "Parabolic/ComponentTransport/heterogeneous/ogs5_H_2D/ogs5_H_2d.prj" >}})
[The project files for the 3D setup are here.]({{< data-url "Parabolic/ComponentTransport/heterogeneous/ogs5_H_3D/ogs5_H_3d.prj" >}})
diff --git a/web/content/docs/benchmarks/hydro-component/heterogeneous/permeability_2d.png b/web/content/docs/benchmarks/hydro-component/HC_ogs6-vs-ogs5/permeability_2d.png
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diff --git a/web/content/docs/benchmarks/hydro-component/contracer/ConTracer1d_results.png b/web/content/docs/benchmarks/hydro-component/contracer/ConTracer/ConTracer1d_results.png
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diff --git a/web/content/docs/benchmarks/hydro-component/contracer/ConTracer_domain.png b/web/content/docs/benchmarks/hydro-component/contracer/ConTracer/ConTracer_domain.png
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rename from web/content/docs/benchmarks/hydro-component/contracer/ConTracer_domain.png
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diff --git a/web/content/docs/benchmarks/hydro-component/contracer/ConTracer.md b/web/content/docs/benchmarks/hydro-component/contracer/ConTracer/index.md
similarity index 96%
rename from web/content/docs/benchmarks/hydro-component/contracer/ConTracer.md
rename to web/content/docs/benchmarks/hydro-component/contracer/ConTracer/index.md
index 20a3ff8433fa11c016e10d79c477fe3b3b3b1a2d..8289117c867becffa03265db2aa78622a76fb9cc 100644
--- a/web/content/docs/benchmarks/hydro-component/contracer/ConTracer.md
+++ b/web/content/docs/benchmarks/hydro-component/contracer/ConTracer/index.md
@@ -24,7 +24,7 @@ Hydraulic water influx was 0.768 $\textrm{m}^3~\textrm{d}^{-1}$ at the left side
The tracer (40.26 g of $\textrm{Br}^-$) was diluted in 12 L of waste water and added as a single impulse event at $t=0$.
Note, that only 89\% of the tracer was recovered at the outlet.
-
+
## Problem description (1D)
@@ -93,9 +93,9 @@ Both models (1D and 2D) fit the experimental tracer breakthrough curves quite we
The deviance at the peak and tail can be related to the fact that the simulations only consider conservative equilibrium transport (processes that may have occurred in the experimental system such as tracer sorption, non--equilibrium flow and evapotranspiration were not considered in the model).
The differences between the OGS-6 and OGS-5 simulation were very low (RMSQE$=$1.37e-07).
-
+
-
+
## References
diff --git a/web/content/docs/benchmarks/hydro-component/gif/elder.gif b/web/content/docs/benchmarks/hydro-component/elder/elder.gif
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rename from web/content/docs/benchmarks/hydro-component/gif/elder.gif
rename to web/content/docs/benchmarks/hydro-component/elder/elder.gif
diff --git a/web/content/docs/benchmarks/hydro-component/elder.md b/web/content/docs/benchmarks/hydro-component/elder/index.md
similarity index 93%
rename from web/content/docs/benchmarks/hydro-component/elder.md
rename to web/content/docs/benchmarks/hydro-component/elder/index.md
index 4810b42733f4c0a21b9d9bc2ae36536cee610aed..e080265bb8c70e985995da54b702f01f9f585aae 100644
--- a/web/content/docs/benchmarks/hydro-component/elder.md
+++ b/web/content/docs/benchmarks/hydro-component/elder/index.md
@@ -27,7 +27,7 @@ The Elder benchmark describes free convection of a dense fluid in mixable, singl
A comparison of the numerical data is shown in the figure below. The numerical results of OGS-6 coincide with those of OGS-5.
-{{< img src="../gif/elder.gif" title="Results for numerical (OGS-5 - green, OGS-6 - white) results together with concentration distribution in the domain and mesh resolution for different time steps.">}}
+{{< img src="elder.gif" title="Results for numerical (OGS-5 - green, OGS-6 - white) results together with concentration distribution in the domain and mesh resolution for different time steps.">}}
{{< data-link >}}
diff --git a/web/content/docs/benchmarks/hydro-component/Goswami_Exp_Num_Comp.png b/web/content/docs/benchmarks/hydro-component/goswami/Goswami_Exp_Num_Comp.png
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rename from web/content/docs/benchmarks/hydro-component/Goswami_Exp_Num_Comp.png
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diff --git a/web/content/docs/benchmarks/hydro-component/Goswami_Transient_States.png b/web/content/docs/benchmarks/hydro-component/goswami/Goswami_Transient_States.png
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rename from web/content/docs/benchmarks/hydro-component/Goswami_Transient_States.png
rename to web/content/docs/benchmarks/hydro-component/goswami/Goswami_Transient_States.png
diff --git a/web/content/docs/benchmarks/hydro-component/gif/goswami.gif b/web/content/docs/benchmarks/hydro-component/goswami/goswami.gif
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rename from web/content/docs/benchmarks/hydro-component/gif/goswami.gif
rename to web/content/docs/benchmarks/hydro-component/goswami/goswami.gif
diff --git a/web/content/docs/benchmarks/hydro-component/goswami.md b/web/content/docs/benchmarks/hydro-component/goswami/index.md
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rename from web/content/docs/benchmarks/hydro-component/goswami.md
rename to web/content/docs/benchmarks/hydro-component/goswami/index.md
index 1cedb0e0c1bb45e27e6e45f8d01c48625dab2d58..f41a5a2853858fbda5ec54eff17328b3b759da04 100644
--- a/web/content/docs/benchmarks/hydro-component/goswami.md
+++ b/web/content/docs/benchmarks/hydro-component/goswami/index.md
@@ -27,15 +27,15 @@ The Goswami-Clement benchmark is based on experiment observations for intruding
An example for the intruding salt front is shown below. The numerical results of OGS-6 coincide with those of OGS-5.
-{{< img src="../gif/goswami.gif" title="Results for numerical experiment. The steady state SS2 from the original experimental work is well reproduced.">}}
+{{< img src="goswami.gif" title="Results for numerical experiment. The steady state SS2 from the original experimental work is well reproduced.">}}
{{< data-link >}}
A comparison of numerical and laboratory data is shown in the figure below. The numerical results of ogs6 coincide with those of OGS5 and likewise with the laboratory observations.
-{{< img src="../Goswami_Exp_Num_Comp.png" title="Results for numerical (colored diamonds) and laboratory data (colored straight lines) on the steady state location of the concentration front (see original research paper).">}}
+{{< img src="Goswami_Exp_Num_Comp.png" title="Results for numerical (colored diamonds) and laboratory data (colored straight lines) on the steady state location of the concentration front (see original research paper).">}}
-{{< img src="../Goswami_Transient_States.png" title="Results for numerical (colored diamonds) and laboratory data (colored straight lines) on the transient state locations of the concentration front (see original research paper).">}}
+{{< img src="Goswami_Transient_States.png" title="Results for numerical (colored diamonds) and laboratory data (colored straight lines) on the transient state locations of the concentration front (see original research paper).">}}
## Literature
diff --git a/web/content/docs/benchmarks/hydro-component/gif/DiffusionAndStorage.gif b/web/content/docs/benchmarks/hydro-component/hydro-component/DiffusionAndStorage.gif
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diff --git a/web/content/docs/benchmarks/hydro-component/HC-NonBoussinesq.pdf b/web/content/docs/benchmarks/hydro-component/hydro-component/HC-NonBoussinesq.pdf
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diff --git a/web/content/docs/benchmarks/hydro-component/HC-Process.pdf b/web/content/docs/benchmarks/hydro-component/hydro-component/HC-Process.pdf
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rename from web/content/docs/benchmarks/hydro-component/HC-Process.pdf
rename to web/content/docs/benchmarks/hydro-component/hydro-component/HC-Process.pdf
diff --git a/web/content/docs/benchmarks/hydro-component/hydro-component.md b/web/content/docs/benchmarks/hydro-component/hydro-component/index.md
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rename from web/content/docs/benchmarks/hydro-component/hydro-component.md
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index e0bef7bfc07eb61938bacd2764cc6040018bfe8e..e68b0bd2b4ecd4f0444e1cc4d27519a6a7b2bd76 100644
--- a/web/content/docs/benchmarks/hydro-component/hydro-component.md
+++ b/web/content/docs/benchmarks/hydro-component/hydro-component/index.md
@@ -17,7 +17,7 @@ title = "Saturated Mass Transport"
This benchmark compiles a number of simple, synthetic setups to test different processes of saturated component transport of a solute.
-The development of the equation system is given in [this PDF](../HC-Process.pdf). In the following, we present the different setups.
+The development of the equation system is given in [this PDF](HC-Process.pdf). In the following, we present the different setups.
## Problem description
@@ -34,7 +34,7 @@ Left side boundary conditions for these two setups are pressure $p=0$ and concen
{{< data-link "The *Diffusion only* project file" "Parabolic/ComponentTransport/SimpleSynthetics/ConcentrationDiffusionOnly.prj" >}}
{{< data-link "The *Diffusion and Storage* project file" "Parabolic/ComponentTransport/SimpleSynthetics/ConcentrationDiffusionAndStorage.prj" >}}
-{{< img src="../gif/DiffusionAndStorage.gif" title="*Diffusion and Storage*">}}
+{{< img src="DiffusionAndStorage.gif" title="*Diffusion and Storage*">}}
#### Diffusion, Storage, and Advection
@@ -42,7 +42,7 @@ Left side boundary conditions for this setup are pressure $p=1$ and concentratio
{{< data-link "The *Diffusion, Storage, and Advection* project file" "Parabolic/ComponentTransport/SimpleSynthetics/DiffusionAndStorageAndAdvection.prj" >}}
-{{< img src="../gif/DiffusionAndStorageAndAdvection.gif" title="*Diffusion, Storage, and Advection*">}}
+{{< img src="DiffusionAndStorageAndAdvection.gif" title="*Diffusion, Storage, and Advection*">}}
#### Diffusion, Storage, Advection, and Dispersion
@@ -51,8 +51,8 @@ Left side boundary conditions for these setups are pressure $p=1$ and concentrat
{{< data-link "The *Diffusion, Storage, Advection, and Dispersion* project file" "Parabolic/ComponentTransport/SimpleSynthetics/DiffusionAndStorageAndAdvectionAndDispersion.prj" >}}
{{< data-link "The *Diffusion, Storage, Advection, and Dispersion Half* project file" "Parabolic/ComponentTransport/SimpleSynthetics/DiffusionAndStorageAndAdvectionAndDispersionHalf.prj" >}}
-{{< img src="../gif/DiffusionAndStorageAndAdvectionAndDispersion.gif" title="*Diffusion, Storage, Advection, and Dispersion*">}}
-{{< img src="../gif/DiffusionAndStorageAndAdvectionAndDispersionHalf.gif" title="*Diffusion, Storage, Advection, and Dispersion Half*">}}
+{{< img src="DiffusionAndStorageAndAdvectionAndDispersion.gif" title="*Diffusion, Storage, Advection, and Dispersion*">}}
+{{< img src="DiffusionAndStorageAndAdvectionAndDispersionHalf.gif" title="*Diffusion, Storage, Advection, and Dispersion Half*">}}
#### Diffusion, Storage, Gravity, and Dispersion
@@ -60,7 +60,7 @@ Boundary condition for this setup is pressure $p=0$ for the top left corner and
{{< data-link "The *Diffusion, Storage, Gravity, and Dispersion* project file" "Parabolic/ComponentTransport/SimpleSynthetics/DiffusionAndStorageAndGravityAndDispersionHalf.prj" >}}
-{{< img src="../gif/DiffusionAndStorageAndGravityAndDispersionHalf.gif" title="*Diffusion, Storage, Gravity, and Dispersion Half*">}}
+{{< img src="DiffusionAndStorageAndGravityAndDispersionHalf.gif" title="*Diffusion, Storage, Gravity, and Dispersion Half*">}}
#### Diffusion, Storage, Advection, and Decay
@@ -68,8 +68,8 @@ Left side boundary conditions for this setup are pressure $p=1$ and concentratio
{{< data-link "The *Diffusion, Storage, Advection, and Decay* project file" "Parabolic/ComponentTransport/SimpleSynthetics/DiffusionAndStorageAndAdvectionAndDecay.prj" >}}
-{{< img src="../gif/DiffusionAndStorageAndAdvectionAndDecay.gif" title="*Diffusion, Storage, Advection, and Decay*">}}
+{{< img src="DiffusionAndStorageAndAdvectionAndDecay.gif" title="*Diffusion, Storage, Advection, and Decay*">}}
#### Changes With Inclusion of Non Boussinesq-Effects
-The changes to the original setup are described in [this PDF](../HC-NonBoussinesq.pdf).
+The changes to the original setup are described in [this PDF](HC-NonBoussinesq.pdf).
diff --git a/web/content/docs/benchmarks/hydro-component/theis/BCs.png b/web/content/docs/benchmarks/hydro-component/theis/HC_Theis/BCs.png
similarity index 100%
rename from web/content/docs/benchmarks/hydro-component/theis/BCs.png
rename to web/content/docs/benchmarks/hydro-component/theis/HC_Theis/BCs.png
diff --git a/web/content/docs/benchmarks/hydro-component/theis/comparison.png b/web/content/docs/benchmarks/hydro-component/theis/HC_Theis/comparison.png
similarity index 100%
rename from web/content/docs/benchmarks/hydro-component/theis/comparison.png
rename to web/content/docs/benchmarks/hydro-component/theis/HC_Theis/comparison.png
diff --git a/web/content/docs/benchmarks/hydro-component/theis/HC_Theis.md b/web/content/docs/benchmarks/hydro-component/theis/HC_Theis/index.md
similarity index 93%
rename from web/content/docs/benchmarks/hydro-component/theis/HC_Theis.md
rename to web/content/docs/benchmarks/hydro-component/theis/HC_Theis/index.md
index d6b8247dea2df6ec2ac3915c4e53b11ac69ed9ee..5727730e0656932734d747d79d178e5e0c4013e8 100644
--- a/web/content/docs/benchmarks/hydro-component/theis/HC_Theis.md
+++ b/web/content/docs/benchmarks/hydro-component/theis/HC_Theis/index.md
@@ -30,7 +30,7 @@ Here, we verify pumping abstraction with Theis for the `ComponentTransport` proc
The setup comprises a 1/8th slice of a full circle (see figure 1).
-{{< img src="../BCs.png" title="Mesh and boundary conditions (BC); blue = outer Dirichlet pressure and concentration BC, red = inner Neumann abstraction BC.">}}
+{{< img src="BCs.png" title="Mesh and boundary conditions (BC); blue = outer Dirichlet pressure and concentration BC, red = inner Neumann abstraction BC.">}}
The outer boundary condition is set as Dirichlet with a hydrostatic pressure along the shell surface of the slice equivalent to a head of $h = 0 m$ (i.e. water level equals top of domain). For mass transport, a Dirichlet boundary conditions with concentration $c = 0$ is set at the outer shell. The inner boundary condition is equivalent to the eighth of a total abstraction rate of $Q_t = 15 m^3/d$ for a full cylinder. *NB: In the `ComponentTransport` process, the Neumann BC is given as mass flux and has to be calculated per area, such that the value for the project file is $Q = Q_t / 8 / A \cdot \rho_0 = 2.83542E-03 m^3/s/m^2 \cdot kg/m^3$ (units equal $\frac{kg}{s m^2}$) with fluid reference density $\rho_0 = 1000 kg/m^3$ and abstraction area $A = 7.65 m^2$.*
@@ -44,7 +44,7 @@ Initial conditions are $c = 0$ and hydrostatic pressure conditions.
The figure below compares the analytical Theis solution vs. the simulated values from OGS6.
-{{< img src="../comparison.png" title="Comparison between numerical (crosses) and analytical (lines) values.">}}
+{{< img src="comparison.png" title="Comparison between numerical (crosses) and analytical (lines) values.">}}
The top figure shows drawdown (i.e. the difference in water level compared to an initial state) over time at distance $r = 30 m$: for a simulation time $t < 40000 s$, the differences between analytical and numerical solutions are marginal; at later simulation times, the drawdown shows lower values than predicted from the analytical solution, as it is influenced by the outer Dirichlet pressure boundary condition.
diff --git a/web/content/docs/benchmarks/hydro-component/HC-VDBCTest.pdf b/web/content/docs/benchmarks/hydro-component/vdbc/HC-VDBCTest.pdf
similarity index 100%
rename from web/content/docs/benchmarks/hydro-component/HC-VDBCTest.pdf
rename to web/content/docs/benchmarks/hydro-component/vdbc/HC-VDBCTest.pdf
diff --git a/web/content/docs/benchmarks/hydro-component/VDBC_num_ana_comp.png b/web/content/docs/benchmarks/hydro-component/vdbc/VDBC_num_ana_comp.png
similarity index 100%
rename from web/content/docs/benchmarks/hydro-component/VDBC_num_ana_comp.png
rename to web/content/docs/benchmarks/hydro-component/vdbc/VDBC_num_ana_comp.png
diff --git a/web/content/docs/benchmarks/hydro-component/vdbc.md b/web/content/docs/benchmarks/hydro-component/vdbc/index.md
similarity index 55%
rename from web/content/docs/benchmarks/hydro-component/vdbc.md
rename to web/content/docs/benchmarks/hydro-component/vdbc/index.md
index 43732ec288d4b8287d639ab8af7dc0086e8fa030..e4a4e23b266b18b9998ee1494438591a43b6fa59 100644
--- a/web/content/docs/benchmarks/hydro-component/vdbc.md
+++ b/web/content/docs/benchmarks/hydro-component/vdbc/index.md
@@ -16,10 +16,10 @@ title = "Variable Dependent Boundary Condition"
## Overview
The component transport process is used for the benchmark setup. Here, a analytical solution of a simple setup is derived and compared to the numerical results.
-This Benchmark is described in [this PDF](../HC-VDBCTest.pdf).
+This Benchmark is described in [this PDF](HC-VDBCTest.pdf).
For the setup and parameterization, see the chapter "Density dependent flow - The Goswami Problem" in Kolditz et al. (2012).
## Results
-{{< img src="../VDBC_num_ana_comp.png" title="UPPER PART: Analytical solution on the right boundary in dependence of time $t$ of the problem indicated with red dashed line in comparison to numerical solution indicated by blue crosses; LOWER PART: development of relative error in dependence of time $t$. Grid spacing for simulations: 0.1; widest timestep 10. The relative error is below $5 \times 10^{-5}$ for all simulation times.">}}
+{{< img src="VDBC_num_ana_comp.png" title="UPPER PART: Analytical solution on the right boundary in dependence of time $t$ of the problem indicated with red dashed line in comparison to numerical solution indicated by blue crosses; LOWER PART: development of relative error in dependence of time $t$. Grid spacing for simulations: 0.1; widest timestep 10. The relative error is below $5 \times 10^{-5}$ for all simulation times.">}}
diff --git a/web/content/docs/benchmarks/python-bc/elder-benchmark/elder/index.md b/web/content/docs/benchmarks/python-bc/elder-benchmark/elder/index.md
index 3c6225747974f3cbc3244c3c4598aae47b27cba5..4b9f6319bb43b9499cffb5ad4b4921c61b659475 100644
--- a/web/content/docs/benchmarks/python-bc/elder-benchmark/elder/index.md
+++ b/web/content/docs/benchmarks/python-bc/elder-benchmark/elder/index.md
@@ -23,5 +23,5 @@ The aim of this test is:
## Details
-This test is a copy of [this test case]({{< ref "../../Hydro-Component/elder" >}}).
+This test is a copy of [this test case]({{< ref "docs/benchmarks/hydro-component/elder" >}}).
Please check the original test case for any details.
diff --git a/web/content/docs/benchmarks/reactive-transport/ThermalDiffusion/DiffusionThermalGradient.pdf b/web/content/docs/benchmarks/reactive-transport/ThermalDiffusion/ThermalDiffusion/DiffusionThermalGradient.pdf
similarity index 100%
rename from web/content/docs/benchmarks/reactive-transport/ThermalDiffusion/DiffusionThermalGradient.pdf
rename to web/content/docs/benchmarks/reactive-transport/ThermalDiffusion/ThermalDiffusion/DiffusionThermalGradient.pdf
diff --git a/web/content/docs/benchmarks/reactive-transport/ThermalDiffusion/ThermalDiffusion.md b/web/content/docs/benchmarks/reactive-transport/ThermalDiffusion/ThermalDiffusion/index.md
similarity index 97%
rename from web/content/docs/benchmarks/reactive-transport/ThermalDiffusion/ThermalDiffusion.md
rename to web/content/docs/benchmarks/reactive-transport/ThermalDiffusion/ThermalDiffusion/index.md
index 3e3c5b832c55c8b8e8666c679e459ab5670ace56..4725bb77710da87bb41246eaeaa38798ab523bb4 100644
--- a/web/content/docs/benchmarks/reactive-transport/ThermalDiffusion/ThermalDiffusion.md
+++ b/web/content/docs/benchmarks/reactive-transport/ThermalDiffusion/ThermalDiffusion/index.md
@@ -30,4 +30,4 @@ Both models `TemperatureField.prj` and `TemperatureField_transport.prj` run inde
## Model setup and results
-See [this PDF](../DiffusionThermalGradient.pdf).
+See [this PDF](DiffusionThermalGradient.pdf).
diff --git a/web/content/docs/benchmarks/reactive-transport/calcite-Figures/ResultComparison.png b/web/content/docs/benchmarks/reactive-transport/calcite/ResultComparison.png
similarity index 100%
rename from web/content/docs/benchmarks/reactive-transport/calcite-Figures/ResultComparison.png
rename to web/content/docs/benchmarks/reactive-transport/calcite/ResultComparison.png
diff --git a/web/content/docs/benchmarks/reactive-transport/calcite-Figures/ResultComparisonPH.png b/web/content/docs/benchmarks/reactive-transport/calcite/ResultComparisonPH.png
similarity index 100%
rename from web/content/docs/benchmarks/reactive-transport/calcite-Figures/ResultComparisonPH.png
rename to web/content/docs/benchmarks/reactive-transport/calcite/ResultComparisonPH.png
diff --git a/web/content/docs/benchmarks/reactive-transport/calcite-Figures/Scheme.png b/web/content/docs/benchmarks/reactive-transport/calcite/Scheme.png
similarity index 100%
rename from web/content/docs/benchmarks/reactive-transport/calcite-Figures/Scheme.png
rename to web/content/docs/benchmarks/reactive-transport/calcite/Scheme.png
diff --git a/web/content/docs/benchmarks/reactive-transport/calcite.md b/web/content/docs/benchmarks/reactive-transport/calcite/index.md
similarity index 92%
rename from web/content/docs/benchmarks/reactive-transport/calcite.md
rename to web/content/docs/benchmarks/reactive-transport/calcite/index.md
index 27d1cf952653e0028663ba0a918737b41786b8dc..dd89e866bfa5cd9b853df8243c8fb5ee884be3ff 100644
--- a/web/content/docs/benchmarks/reactive-transport/calcite.md
+++ b/web/content/docs/benchmarks/reactive-transport/calcite/index.md
@@ -56,7 +56,7 @@ where $\alpha_L$ (m) and $\alpha_T$ (m) are the longitudinal and transversal dis
A one-dimensional (1D) model domain of 0.5 m discretized into 100 uniform elements has been selected for the spatial discretization of the system. Dirichlet (constant concentration) and Neumannn (no flux) boundary condition are defined for the upstream inflow and the downstream, respectively. A longitudinal dispersivity of 0.0067 m and a time step size of 100 s have been taken into account in the simulation. See Figure below:
-{{< img src="../calcite-Figures/Scheme.png" title="Schematic representation of the model setup and parameters.">}}
+{{< img src="Scheme.png" title="Schematic representation of the model setup and parameters.">}}
Thermodynamic data for hydrolysis, aqueous speciation, and dissolution/precipitation reactions between Mg, Ca, Cl, and carbonate were selected from version 12/07 of the PSI/NAGRA chemical thermodynamic database (Thoenen *et al.* 2014). Although several other minerals containing Mg and Ca were available in the PSI/NAGRA database (*i.e.* magnesite), only two solids were allowed to precipitate or dissolve in the studied system (calcite and dolomite (CaMg(CO$_3$)$_2$)).
@@ -66,9 +66,9 @@ A comparison of the results obtained with OGS-6#IPhreeqc and OGS-5#IPhreeqc at t
At the simulated time, it can be clearly seen that the MgCl$_2$ solution front has penetrated ~0.3m of the column resulting in the dissolution of calcite and dolomite precipitation. Total aqueous concentration and solid profiles obtained of OGS-6 are in good agreement with those of OGS-5. The absolute error in terms of component concentrations is $2.15\times10^{-5}$ (Cl), $1.13\times10^{-5}$ (Mg), and $4.57\times10^{-6}$ (Ca). Additionally, pH profiles calculated with both codes are in good agreement.
-{{< img src="../calcite-Figures/ResultComparison.png" title="Total aqueous concentration and solid profiles obtained with OGS-6#IPhreeqc (empty triangle symbol) and OGS-5#IPhreeqc (empty circle symbol) at 350 min. (C(4) = total carbonate)">}}
+{{< img src="ResultComparison.png" title="Total aqueous concentration and solid profiles obtained with OGS-6#IPhreeqc (empty triangle symbol) and OGS-5#IPhreeqc (empty circle symbol) at 350 min. (C(4) = total carbonate)">}}
-{{< img src="../calcite-Figures/ResultComparisonPH.png" title="pH value profiles obtained with OGS-6#IPhreeqc (empty triangle symbol) and OGS-5#IPhreeqc (empty circle symbol) at 350 min.">}}
+{{< img src="ResultComparisonPH.png" title="pH value profiles obtained with OGS-6#IPhreeqc (empty triangle symbol) and OGS-5#IPhreeqc (empty circle symbol) at 350 min.">}}
{{< data-link >}}
diff --git a/web/content/docs/benchmarks/reactive-transport/exchange/fig1.png b/web/content/docs/benchmarks/reactive-transport/exchange/exchange/fig1.png
similarity index 100%
rename from web/content/docs/benchmarks/reactive-transport/exchange/fig1.png
rename to web/content/docs/benchmarks/reactive-transport/exchange/exchange/fig1.png
diff --git a/web/content/docs/benchmarks/reactive-transport/exchange/fig2.png b/web/content/docs/benchmarks/reactive-transport/exchange/exchange/fig2.png
similarity index 100%
rename from web/content/docs/benchmarks/reactive-transport/exchange/fig2.png
rename to web/content/docs/benchmarks/reactive-transport/exchange/exchange/fig2.png
diff --git a/web/content/docs/benchmarks/reactive-transport/exchange/exchange.md b/web/content/docs/benchmarks/reactive-transport/exchange/exchange/index.md
similarity index 83%
rename from web/content/docs/benchmarks/reactive-transport/exchange/exchange.md
rename to web/content/docs/benchmarks/reactive-transport/exchange/exchange/index.md
index bc53d0b20c67014a7dc9ccf5d6b197d259da4fca..6fc30cfaa986ef08d9267c418a4c1d3ca9893c85 100644
--- a/web/content/docs/benchmarks/reactive-transport/exchange/exchange.md
+++ b/web/content/docs/benchmarks/reactive-transport/exchange/exchange/index.md
@@ -18,7 +18,7 @@ title = "Transport and Cation Exchange"
This benchmark simulates the chemical composition of the effluent from a column containing a cation exchanger (Example 11 in the PHREEQC 3 documentation).
The following setup is used for the simulation:
-{{< img src="../fig1.png" title="Model setup for the simulation of the column with a cation exchanger in OGS6.">}}
+{{< img src="fig1.png" title="Model setup for the simulation of the column with a cation exchanger in OGS6.">}}
Full details of the model setup and parameters are given in the PHREEQC3 example (consulted MAY-2021):
@@ -26,7 +26,7 @@ https://water.usgs.gov/water-resources/software/PHREEQC/documentation/phreeqc3-h
The benchmark uses the `ComponentTransport` process in OGS-6 coupled with the IPhreeqc software (Parkhurst and Appelo,2013). The results show good agreement between codes. More details about the implementation of the `ComponentTransport` process in OGS-6 can be found in [HC-Process.pdf](/docs/benchmarks/hydro-component/HC-Process.pdf).
-{{< img src="../fig2.png" title="Comparison between PHREEQC and OGS6 of simulated concentrations of solutes at time = 18,000 s reacting with an exchanger.">}}
+{{< img src="fig2.png" title="Comparison between PHREEQC and OGS6 of simulated concentrations of solutes at time = 18,000 s reacting with an exchanger.">}}
{{< data-link >}}
diff --git a/web/content/docs/benchmarks/reactive-transport/kineticreactant_allascomponents/KineticReactant2_domain.png b/web/content/docs/benchmarks/reactive-transport/kineticreactant_allascomponents/KineticReactant2/KineticReactant2_domain.png
similarity index 100%
rename from web/content/docs/benchmarks/reactive-transport/kineticreactant_allascomponents/KineticReactant2_domain.png
rename to web/content/docs/benchmarks/reactive-transport/kineticreactant_allascomponents/KineticReactant2/KineticReactant2_domain.png
diff --git a/web/content/docs/benchmarks/reactive-transport/kineticreactant_allascomponents/KineticReactant2.md b/web/content/docs/benchmarks/reactive-transport/kineticreactant_allascomponents/KineticReactant2/index.md
similarity index 98%
rename from web/content/docs/benchmarks/reactive-transport/kineticreactant_allascomponents/KineticReactant2.md
rename to web/content/docs/benchmarks/reactive-transport/kineticreactant_allascomponents/KineticReactant2/index.md
index beb4913d266949fe8c337bf65101e08de3801d0f..414428f91abe5459cf0a261b9568b0c2a7120712 100644
--- a/web/content/docs/benchmarks/reactive-transport/kineticreactant_allascomponents/KineticReactant2.md
+++ b/web/content/docs/benchmarks/reactive-transport/kineticreactant_allascomponents/KineticReactant2/index.md
@@ -37,7 +37,7 @@ Respective material properties, initial and boundary conditions are listed in th
The 2d--scenario only differs in the domain geometry and assignment of the boundary conditions.
The horizontal domain is 0.5 m in x and 0.5 m in y direction, and, discretized into 10374 quadratic elemtents with an edge size of 0.0025 m.
-
+
-----------------------------------------
diff --git a/web/content/docs/benchmarks/reactive-transport/radionuclide/Fig1.png b/web/content/docs/benchmarks/reactive-transport/radionuclide/radionuclide/Fig1.png
similarity index 100%
rename from web/content/docs/benchmarks/reactive-transport/radionuclide/Fig1.png
rename to web/content/docs/benchmarks/reactive-transport/radionuclide/radionuclide/Fig1.png
diff --git a/web/content/docs/benchmarks/reactive-transport/radionuclide/domain.png b/web/content/docs/benchmarks/reactive-transport/radionuclide/radionuclide/domain.png
similarity index 100%
rename from web/content/docs/benchmarks/reactive-transport/radionuclide/domain.png
rename to web/content/docs/benchmarks/reactive-transport/radionuclide/radionuclide/domain.png
diff --git a/web/content/docs/benchmarks/reactive-transport/radionuclide/radionuclide.md b/web/content/docs/benchmarks/reactive-transport/radionuclide/radionuclide/index.md
similarity index 93%
rename from web/content/docs/benchmarks/reactive-transport/radionuclide/radionuclide.md
rename to web/content/docs/benchmarks/reactive-transport/radionuclide/radionuclide/index.md
index 92475255f5b31886347ef8fef2bd6cdc33a95e49..6801dfc261d1a3391721c7103371207d61422b30 100644
--- a/web/content/docs/benchmarks/reactive-transport/radionuclide/radionuclide.md
+++ b/web/content/docs/benchmarks/reactive-transport/radionuclide/radionuclide/index.md
@@ -19,7 +19,7 @@ This benchmark is focused on the simulation of the migration of $U(VI)$ in a por
The benchmark uses the `ComponentTransport` process in OGS-6 (see [HC-Process.pdf](/docs/benchmarks/hydro-component/HC-Process.pdf)) coupled with the IPhreeqc interface (Parkhurst and Appelo,2013) for the chemical speciation calculations. The porewater initial composition and injected for the first 10 000 s is shown in Table 1. The porewater solution is equilibrated with Calcite.
-{{< img src="../domain.png" title="Spatial and temporal discretization of the 1D model. Solution concentrations with/without U(VI) are applied at the inflow boundary. Initial concentration of U(VI) in the domain is 0.">}}
+{{< img src="domain.png" title="Spatial and temporal discretization of the 1D model. Solution concentrations with/without U(VI) are applied at the inflow boundary. Initial concentration of U(VI) in the domain is 0.">}}
-----------------------------------------
@@ -60,7 +60,7 @@ Table 2: **Surface parameters and characterization used in the simulations.**
Four different combinations can be simulated taking the albite and orthoclase phases of the Feldspars group and the goethite and hematite phases for the Fe(III)-oxids/-hydroxids group. Mineral combinations from 1 to 4 (see Fig. 2) are as follows: 1) albite-goethite, 2) albite-hematite, 3) orthoclase-goethite and 4) orthoclase-hematite. From the concentration profiles in Fig. 2, it is clear that the combination 2 approximates better the profile obtained with the ESTRAL database. We choose this combination for the next part of our simulations. Furthermore, this combination is written in the `RadionuclideSorption.prj` file of this benchmark.
-{{< img src="../Fig1.png" title="Comparison of concentration profiles at final simulation time (115 000 s) for various representative minerals of the Feldspar and Fe(III)-oxids/-hydroxids groups. The mineral combinations profiles are obtained using the PSI/Nagra database version 12/07 and the dashed profile is obtained with the ESTRAL database.">}}
+{{< img src="Fig1.png" title="Comparison of concentration profiles at final simulation time (115 000 s) for various representative minerals of the Feldspar and Fe(III)-oxids/-hydroxids groups. The mineral combinations profiles are obtained using the PSI/Nagra database version 12/07 and the dashed profile is obtained with the ESTRAL database.">}}
The temporal evolution of the concentration profiles of the chosen mineral combination (albite-hematite) compared to the ESTRAL database is shown in Fig. 3. In addition, a simulation of the reactive transport treating $U(VI)$ as a non-sorbing radionuclide is presented. Recall that the contaminated solution with $U(VI)$ is injected only for the first 10 000 s of simulation. On the one hand, we note the difference between the profile with the augmented PSI/Nagra database and with the ESTRAL database. This is expected, since different reactions and significant differences in *log K* values are considered for each simulation. However, we note that the trend is similar enough to capture the relevant sorption process happening at the surface.
diff --git a/web/content/docs/benchmarks/reactive-transport/wetland/Wetland_cwm1.png b/web/content/docs/benchmarks/reactive-transport/wetland/Wetland/Wetland_cwm1.png
similarity index 100%
rename from web/content/docs/benchmarks/reactive-transport/wetland/Wetland_cwm1.png
rename to web/content/docs/benchmarks/reactive-transport/wetland/Wetland/Wetland_cwm1.png
diff --git a/web/content/docs/benchmarks/reactive-transport/wetland/Wetland_domain.png b/web/content/docs/benchmarks/reactive-transport/wetland/Wetland/Wetland_domain.png
similarity index 100%
rename from web/content/docs/benchmarks/reactive-transport/wetland/Wetland_domain.png
rename to web/content/docs/benchmarks/reactive-transport/wetland/Wetland/Wetland_domain.png
diff --git a/web/content/docs/benchmarks/reactive-transport/wetland/Wetland.md b/web/content/docs/benchmarks/reactive-transport/wetland/Wetland/index.md
similarity index 98%
rename from web/content/docs/benchmarks/reactive-transport/wetland/Wetland.md
rename to web/content/docs/benchmarks/reactive-transport/wetland/Wetland/index.md
index 79dfa3d7158bbb623a448a607bb7a59e68317aa4..6ea67f1ac8a187484e00a4d6339b9be45fb1261a 100644
--- a/web/content/docs/benchmarks/reactive-transport/wetland/Wetland.md
+++ b/web/content/docs/benchmarks/reactive-transport/wetland/Wetland/index.md
@@ -34,7 +34,7 @@ The domain is saturated at start--up with an initial hydrostatic pressure of ($p
For the water mass influx a constant Neumann boundary condition (BC) is set at the left side ($g_{N,\text{in}}^p$).
For the water efflux, a constant pressure is defined as boundary ($g_{D,\text{out}}^p$).
-
+
The microbiological processes are modeled by a complex network of kinetic reactions based on the Constructed Wetland Model No. 1 (CWM1) described in Langergraber (2009).
The network includes dissolved oxygen ($So$) and nine different soluble and particulated components ("pollutants") that some of them can be metabolized by six bacterial groups resulting in 17 kinetic reactions (Figure 2).
@@ -42,7 +42,7 @@ A "clean" system is assumed at start-up in the basin, therefore, initial concent
For the wastewater components ("pollutants" and oxygen) entering the system, time-dependent Dirichlet BC are defined at the influx point.
Respective material properties, initial and boundary conditions are listed in Table 1--2.
-{width=60%}
+{width=60%}
-----------------------------------------
diff --git a/web/content/docs/benchmarks/richards-flow/RichardsComponentTransport_Equations.pdf b/web/content/docs/benchmarks/richards-flow/richards-component-transport/RichardsComponentTransport_Equations.pdf
similarity index 100%
rename from web/content/docs/benchmarks/richards-flow/RichardsComponentTransport_Equations.pdf
rename to web/content/docs/benchmarks/richards-flow/richards-component-transport/RichardsComponentTransport_Equations.pdf
diff --git a/web/content/docs/benchmarks/richards-flow/RichardsComponentTransport_Padilla.png b/web/content/docs/benchmarks/richards-flow/richards-component-transport/RichardsComponentTransport_Padilla.png
similarity index 100%
rename from web/content/docs/benchmarks/richards-flow/RichardsComponentTransport_Padilla.png
rename to web/content/docs/benchmarks/richards-flow/richards-component-transport/RichardsComponentTransport_Padilla.png
diff --git a/web/content/docs/benchmarks/richards-flow/richards-component-transport.md b/web/content/docs/benchmarks/richards-flow/richards-component-transport/index.md
similarity index 89%
rename from web/content/docs/benchmarks/richards-flow/richards-component-transport.md
rename to web/content/docs/benchmarks/richards-flow/richards-component-transport/index.md
index a29168f9ee2ebe801ac0b36ef7968398ac7ce0e4..42d5aaa65c5f222a1deb1769a9a6dffa792f9abd 100644
--- a/web/content/docs/benchmarks/richards-flow/richards-component-transport.md
+++ b/web/content/docs/benchmarks/richards-flow/richards-component-transport/index.md
@@ -17,7 +17,7 @@ title = "Unsaturated Mass Transport"
The Richards equation is often used to describe water movement in the unsaturated zone, while the mass transport equation describes solute movement in the liquid phase. Here, we use a monolithic approach to simulate mass transport in an unsaturated medium.
-The development of the equation system is given in [this PDF](../RichardsComponentTransport_Equations.pdf). In the following, we present a numerical benchmark that uses experimental data as reference.
+The development of the equation system is given in [this PDF](RichardsComponentTransport_Equations.pdf). In the following, we present a numerical benchmark that uses experimental data as reference.
## Problem description
@@ -38,7 +38,7 @@ Initial conditions are $c = 0$ and hydrostatic pressure conditions with steady s
The figure below shows breakthrough curves vs experimental result at the bottom of the simulation domain, together with averaged saturation values at the two observation points with distance of 0.075 cm from both ends of the column (as stated in Padilla et al., 1999) over pore volume.
-{{< img src="../RichardsComponentTransport_Padilla.png" title="Comparison between numerical (lines) and experimental (squares) results for cases 'NaCl1' and 'NaCl6' from Padilla et al. (1999).">}}
+{{< img src="RichardsComponentTransport_Padilla.png" title="Comparison between numerical (lines) and experimental (squares) results for cases 'NaCl1' and 'NaCl6' from Padilla et al. (1999).">}}
It can be seen, that with decreasing saturation, breakthrough curves exhibit stronger dispersion through the decreased angle of the breakthrough curve. Both simulation results follow the experimental observations closely; deviations, especially in the unsaturated case, can be attributed to known tailing effects from secondary porosity.
diff --git a/web/content/docs/benchmarks/richards-flow/richards-flow.md b/web/content/docs/benchmarks/richards-flow/richards-flow/index.md
similarity index 87%
rename from web/content/docs/benchmarks/richards-flow/richards-flow.md
rename to web/content/docs/benchmarks/richards-flow/richards-flow/index.md
index 513f5a1a893a18fa50f624099c6fdaf55a8f9d42..12fabbcae3e74ed3fbad535f74801c594b5cd97f 100644
--- a/web/content/docs/benchmarks/richards-flow/richards-flow.md
+++ b/web/content/docs/benchmarks/richards-flow/richards-flow/index.md
@@ -19,4 +19,4 @@ The Richards equation is often used to mathematically describe water movement in
## Problem setting
-See [this PDF](../richards-2.pdf) for the problem setting.
+See [this PDF](richards-2.pdf) for the problem setting.
diff --git a/web/content/docs/benchmarks/richards-flow/richards-2.pdf b/web/content/docs/benchmarks/richards-flow/richards-flow/richards-2.pdf
similarity index 100%
rename from web/content/docs/benchmarks/richards-flow/richards-2.pdf
rename to web/content/docs/benchmarks/richards-flow/richards-flow/richards-2.pdf
diff --git a/web/content/docs/benchmarks/richards-mechanics/BishopsEffectiveStress.png b/web/content/docs/benchmarks/richards-mechanics/bishops-effective-stress/BishopsEffectiveStress.png
similarity index 100%
rename from web/content/docs/benchmarks/richards-mechanics/BishopsEffectiveStress.png
rename to web/content/docs/benchmarks/richards-mechanics/bishops-effective-stress/BishopsEffectiveStress.png
diff --git a/web/content/docs/benchmarks/richards-mechanics/bishops-effective-stress.md b/web/content/docs/benchmarks/richards-mechanics/bishops-effective-stress/index.md
similarity index 95%
rename from web/content/docs/benchmarks/richards-mechanics/bishops-effective-stress.md
rename to web/content/docs/benchmarks/richards-mechanics/bishops-effective-stress/index.md
index b35e15f13ad572add18e702c6e354f9d02ea696c..6099c1c30efb0bb99c519d35bc7efadcea197627 100644
--- a/web/content/docs/benchmarks/richards-mechanics/bishops-effective-stress.md
+++ b/web/content/docs/benchmarks/richards-mechanics/bishops-effective-stress/index.md
@@ -30,4 +30,4 @@ displacement. In the test the medium is desaturated and then saturated again,
which causes shrinkage and expansion of the domain. Power law with exponents 1,
1/5, and 5 and saturation cut-off at maximum liquid saturation of 0.95 are
compared.
-{{< img src="../BishopsEffectiveStress.png" >}}
+{{< img src="BishopsEffectiveStress.png" >}}
diff --git a/web/content/docs/benchmarks/richards-mechanics/liakopoulos.md b/web/content/docs/benchmarks/richards-mechanics/liakopoulos/index.md
similarity index 90%
rename from web/content/docs/benchmarks/richards-mechanics/liakopoulos.md
rename to web/content/docs/benchmarks/richards-mechanics/liakopoulos/index.md
index a2430fcd99fdfa7451c6b2b5426a11ef8c93d743..fff34a3750b79fa4f0c566b40dc34a1d46726da1 100644
--- a/web/content/docs/benchmarks/richards-mechanics/liakopoulos.md
+++ b/web/content/docs/benchmarks/richards-mechanics/liakopoulos/index.md
@@ -17,9 +17,9 @@ This benchmark simulates the Liakopoulos experiment
{{< data-link >}}
* Saturation profile:
-{{< img src="../liak_S.png" >}}
+{{< img src="liak_S.png" >}}
* Vertical displacement profile:
-{{< img src="../liak_uy.png" >}}
+{{< img src="liak_uy.png" >}}
## References
diff --git a/web/content/docs/benchmarks/richards-mechanics/liak_S.png b/web/content/docs/benchmarks/richards-mechanics/liakopoulos/liak_S.png
similarity index 100%
rename from web/content/docs/benchmarks/richards-mechanics/liak_S.png
rename to web/content/docs/benchmarks/richards-mechanics/liakopoulos/liak_S.png
diff --git a/web/content/docs/benchmarks/richards-mechanics/liak_uy.png b/web/content/docs/benchmarks/richards-mechanics/liakopoulos/liak_uy.png
similarity index 100%
rename from web/content/docs/benchmarks/richards-mechanics/liak_uy.png
rename to web/content/docs/benchmarks/richards-mechanics/liakopoulos/liak_uy.png
diff --git a/web/content/docs/benchmarks/small-deformations/ModifiedCamClay_report.pdf b/web/content/docs/benchmarks/small-deformations/ModifiedCamClay/ModifiedCamClay_report.pdf
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/ModifiedCamClay_report.pdf
rename to web/content/docs/benchmarks/small-deformations/ModifiedCamClay/ModifiedCamClay_report.pdf
diff --git a/web/content/docs/benchmarks/small-deformations/ModifiedCamClay.md b/web/content/docs/benchmarks/small-deformations/ModifiedCamClay/index.md
similarity index 90%
rename from web/content/docs/benchmarks/small-deformations/ModifiedCamClay.md
rename to web/content/docs/benchmarks/small-deformations/ModifiedCamClay/index.md
index 765d0c6b03814663cf64fb7334a528e1d937fd93..785a25a291ab6e1db505f516ef9c36208736081b 100644
--- a/web/content/docs/benchmarks/small-deformations/ModifiedCamClay.md
+++ b/web/content/docs/benchmarks/small-deformations/ModifiedCamClay/index.md
@@ -23,4 +23,4 @@ Three tests are presented:
We perform plane strain and axisymmetric mechanical tests using
the modified Cam clay model revealing both the features and
the limitations of this material model.
-See [this PDF](../ModifiedCamClay_report.pdf) for the detailed description.
+See [this PDF](ModifiedCamClay_report.pdf) for the detailed description.
diff --git a/web/content/docs/benchmarks/small-deformations/arehs-salt-T_elements.png b/web/content/docs/benchmarks/small-deformations/arehs_salt_dome_creep_hete_T_ref/arehs-salt-T_elements.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/arehs-salt-T_elements.png
rename to web/content/docs/benchmarks/small-deformations/arehs_salt_dome_creep_hete_T_ref/arehs-salt-T_elements.png
diff --git a/web/content/docs/benchmarks/small-deformations/arehs_saltdome_creep_S.png b/web/content/docs/benchmarks/small-deformations/arehs_salt_dome_creep_hete_T_ref/arehs_saltdome_creep_S.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/arehs_saltdome_creep_S.png
rename to web/content/docs/benchmarks/small-deformations/arehs_salt_dome_creep_hete_T_ref/arehs_saltdome_creep_S.png
diff --git a/web/content/docs/benchmarks/small-deformations/arehs_saltdome_creep_u.png b/web/content/docs/benchmarks/small-deformations/arehs_salt_dome_creep_hete_T_ref/arehs_saltdome_creep_u.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/arehs_saltdome_creep_u.png
rename to web/content/docs/benchmarks/small-deformations/arehs_salt_dome_creep_hete_T_ref/arehs_saltdome_creep_u.png
diff --git a/web/content/docs/benchmarks/small-deformations/arehs_salt_dome_creep_hete_T_ref.md b/web/content/docs/benchmarks/small-deformations/arehs_salt_dome_creep_hete_T_ref/index.md
similarity index 89%
rename from web/content/docs/benchmarks/small-deformations/arehs_salt_dome_creep_hete_T_ref.md
rename to web/content/docs/benchmarks/small-deformations/arehs_salt_dome_creep_hete_T_ref/index.md
index 5d9605d6c4e4e94105dc5538ee6391d2eb09f1c9..46cc0ff14fff8954e1023315eb90baca25af0ef5 100644
--- a/web/content/docs/benchmarks/small-deformations/arehs_salt_dome_creep_hete_T_ref.md
+++ b/web/content/docs/benchmarks/small-deformations/arehs_salt_dome_creep_hete_T_ref/index.md
@@ -33,7 +33,7 @@ The other material parameters are listed in the following table:
The reference temperature is shown in the following figure:
<p align="center">
-<img src="../arehs-salt-T_elements.png" alt="drawing" width="400"/>
+<img src="arehs-salt-T_elements.png" alt="drawing" width="400"/>
</p>
The initial stresses were obtained by conducting a simulation of the pure elastic
deformation in the same domain under the gravitational force.
@@ -43,10 +43,10 @@ As a benchmark, only one thousand years' creep with six time steps is considere
The following two figures shown the results of stress magnitude and displacement
magnitude at the last time step:
<p align="center">
-<img src="../arehs_saltdome_creep_S.png" alt="drawing" width="600"/>
+<img src="arehs_saltdome_creep_S.png" alt="drawing" width="600"/>
</p>
<p align="center">
-<img src="../arehs_saltdome_creep_u.png" alt="drawing" width="600"/>
+<img src="arehs_saltdome_creep_u.png" alt="drawing" width="600"/>
</p>
## References
diff --git a/web/content/docs/benchmarks/small-deformations/LIE_SD_m_result_uy.png b/web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture/LIE_SD_m_result_uy.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/LIE_SD_m_result_uy.png
rename to web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture/LIE_SD_m_result_uy.png
diff --git a/web/content/docs/benchmarks/small-deformations/LIE_fracture_incompressibility.pdf b/web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture/LIE_fracture_incompressibility.pdf
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/LIE_fracture_incompressibility.pdf
rename to web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture/LIE_fracture_incompressibility.pdf
diff --git a/web/content/docs/benchmarks/small-deformations/LIE_small_deformation.pdf b/web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture/LIE_small_deformation.pdf
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/LIE_small_deformation.pdf
rename to web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture/LIE_small_deformation.pdf
diff --git a/web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture.md b/web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture/index.md
similarity index 75%
rename from web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture.md
rename to web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture/index.md
index c0b34a153fd3cd6d4bdb2e4550882b32f7056e59..d209b40ddbcb8725c07a8cbf6b8fa80610574297 100644
--- a/web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture.md
+++ b/web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture/index.md
@@ -17,21 +17,21 @@ title = "Linear; Single fracture"
We solve a linear elastic small deformation problem with a pre-existing fracture using the lower-dimensional interface element (LIE) approach.
-See [this PDF](../LIE_small_deformation.pdf) for detailed problem description.
+See [this PDF](LIE_small_deformation.pdf) for detailed problem description.
The one-sided incompressibility constraint for fracture models is described in
-[this PDF](../LIE_fracture_incompressibility.pdf).
+[this PDF](LIE_fracture_incompressibility.pdf).
## Results and evaluation
Result showing sliding of the upper part of the domain along the fracture:
-{{< img src="../LIE_SD_m_result_uy.png" >}}
+{{< img src="LIE_SD_m_result_uy.png" >}}
Same benchmark setup with plane strain conditions in 3D:
-{{< img src="../single_joint_3D.png" >}}
+{{< img src="single_joint_3D.png" >}}
Comparison with 2D setup yields identical results (up to numerical differences
in order of 1e-15); Resulting displacement on the left axis, and error on the
right:
-{{< img src="../single_joint_3D_2D_results.png" >}}
+{{< img src="single_joint_3D_2D_results.png" >}}
diff --git a/web/content/docs/benchmarks/small-deformations/single_joint_3D.png b/web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture/single_joint_3D.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/single_joint_3D.png
rename to web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture/single_joint_3D.png
diff --git a/web/content/docs/benchmarks/small-deformations/single_joint_3D_2D_results.png b/web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture/single_joint_3D_2D_results.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/single_joint_3D_2D_results.png
rename to web/content/docs/benchmarks/small-deformations/lie-m-linear-single-fracture/single_joint_3D_2D_results.png
diff --git a/web/content/docs/benchmarks/small-deformations/Circular_hole.pdf b/web/content/docs/benchmarks/small-deformations/mechanics-linear-disc-with-hole/Circular_hole.pdf
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/Circular_hole.pdf
rename to web/content/docs/benchmarks/small-deformations/mechanics-linear-disc-with-hole/Circular_hole.pdf
diff --git a/web/content/docs/benchmarks/small-deformations/disc_with_hole_pcs_0_ts_4_t_1.000000.png b/web/content/docs/benchmarks/small-deformations/mechanics-linear-disc-with-hole/disc_with_hole_pcs_0_ts_4_t_1.000000.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/disc_with_hole_pcs_0_ts_4_t_1.000000.png
rename to web/content/docs/benchmarks/small-deformations/mechanics-linear-disc-with-hole/disc_with_hole_pcs_0_ts_4_t_1.000000.png
diff --git a/web/content/docs/benchmarks/small-deformations/mechanics-linear-disc-with-hole.md b/web/content/docs/benchmarks/small-deformations/mechanics-linear-disc-with-hole/index.md
similarity index 75%
rename from web/content/docs/benchmarks/small-deformations/mechanics-linear-disc-with-hole.md
rename to web/content/docs/benchmarks/small-deformations/mechanics-linear-disc-with-hole/index.md
index 70ca56aab1d74e8ef74c6fb45fd17d7173ab7697..8235477b640a5ae9b33c68b5ff60c5a2dc6ff9f5 100644
--- a/web/content/docs/benchmarks/small-deformations/mechanics-linear-disc-with-hole.md
+++ b/web/content/docs/benchmarks/small-deformations/mechanics-linear-disc-with-hole/index.md
@@ -17,10 +17,10 @@ weight = 111
We solve a linear elastic small deformation problem on a quarter of a plate with hole put under tension on the top boundary.
-See [this PDF](../Circular_hole.pdf) for detailed problem description.
+See [this PDF](Circular_hole.pdf) for detailed problem description.
## Results and evaluation
-
+
<!-- {{< vis path="Mechanics/Linear/disc_with_hole_pcs_0_ts_4_t_1.000000.vtu" >}} -->
diff --git a/web/content/docs/benchmarks/small-deformations/element_deactivation_2D.png b/web/content/docs/benchmarks/small-deformations/mechanics-linear-element_deactivation/element_deactivation_2D.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/element_deactivation_2D.png
rename to web/content/docs/benchmarks/small-deformations/mechanics-linear-element_deactivation/element_deactivation_2D.png
diff --git a/web/content/docs/benchmarks/small-deformations/element_deactivation_2D_3D_mesh.png b/web/content/docs/benchmarks/small-deformations/mechanics-linear-element_deactivation/element_deactivation_2D_3D_mesh.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/element_deactivation_2D_3D_mesh.png
rename to web/content/docs/benchmarks/small-deformations/mechanics-linear-element_deactivation/element_deactivation_2D_3D_mesh.png
diff --git a/web/content/docs/benchmarks/small-deformations/element_deactivation_3D.png b/web/content/docs/benchmarks/small-deformations/mechanics-linear-element_deactivation/element_deactivation_3D.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/element_deactivation_3D.png
rename to web/content/docs/benchmarks/small-deformations/mechanics-linear-element_deactivation/element_deactivation_3D.png
diff --git a/web/content/docs/benchmarks/small-deformations/mechanics-linear-element_deactivation.md b/web/content/docs/benchmarks/small-deformations/mechanics-linear-element_deactivation/index.md
similarity index 91%
rename from web/content/docs/benchmarks/small-deformations/mechanics-linear-element_deactivation.md
rename to web/content/docs/benchmarks/small-deformations/mechanics-linear-element_deactivation/index.md
index 09234961cc48c601e2fb4088a783554297847349..6d17da499d1ab8c4804e174aedc82eb3dcbbbd88 100644
--- a/web/content/docs/benchmarks/small-deformations/mechanics-linear-element_deactivation.md
+++ b/web/content/docs/benchmarks/small-deformations/mechanics-linear-element_deactivation/index.md
@@ -42,10 +42,10 @@ The input data set of the element deactivation approach is specified inside the
## Mesh
-
+
## Results and evaluation
-
+
-
+
diff --git a/web/content/docs/benchmarks/small-deformations/mechanics-linear-nonequilibrium-states.md b/web/content/docs/benchmarks/small-deformations/mechanics-linear-nonequilibrium-states/index.md
similarity index 82%
rename from web/content/docs/benchmarks/small-deformations/mechanics-linear-nonequilibrium-states.md
rename to web/content/docs/benchmarks/small-deformations/mechanics-linear-nonequilibrium-states/index.md
index b0f596aad3cb3ccf438864e3fd0a27d2dfcf71bf..5ebc949af4b25220b8be0c6d97c11f325d906957 100644
--- a/web/content/docs/benchmarks/small-deformations/mechanics-linear-nonequilibrium-states.md
+++ b/web/content/docs/benchmarks/small-deformations/mechanics-linear-nonequilibrium-states/index.md
@@ -16,7 +16,7 @@ weight = 111
## Overview
For detailed description see [technical note
-PDF](../non-equilibrium_initial_states.pdf); here only excerpts from the
+PDF](non-equilibrium_initial_states.pdf); here only excerpts from the
document are shown.
In certain conditions we want to drive changes in the process only by a change
@@ -24,4 +24,4 @@ in the external driving forces and suppress the initial equilibration.
Three test cases are showing a full simulation from equilibrium initial state,
a restart with equilibrium, and calculation from non-equilibrium initial state.
-
+
diff --git a/web/content/docs/benchmarks/small-deformations/non-equilibrium_initial_states.pdf b/web/content/docs/benchmarks/small-deformations/mechanics-linear-nonequilibrium-states/non-equilibrium_initial_states.pdf
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/non-equilibrium_initial_states.pdf
rename to web/content/docs/benchmarks/small-deformations/mechanics-linear-nonequilibrium-states/non-equilibrium_initial_states.pdf
diff --git a/web/content/docs/benchmarks/small-deformations/non-equilibrium_initial_states.png b/web/content/docs/benchmarks/small-deformations/mechanics-linear-nonequilibrium-states/non-equilibrium_initial_states.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/non-equilibrium_initial_states.png
rename to web/content/docs/benchmarks/small-deformations/mechanics-linear-nonequilibrium-states/non-equilibrium_initial_states.png
diff --git a/web/content/docs/benchmarks/small-deformations/mechanics-lubby2-shear-traction.md b/web/content/docs/benchmarks/small-deformations/mechanics-lubby2-shear-traction/index.md
similarity index 82%
rename from web/content/docs/benchmarks/small-deformations/mechanics-lubby2-shear-traction.md
rename to web/content/docs/benchmarks/small-deformations/mechanics-lubby2-shear-traction/index.md
index b83440b7e9c2be618fb171393acbf4fa72e14d39..b17dbb2eb2721a078ccd5bf200e747502499df96 100644
--- a/web/content/docs/benchmarks/small-deformations/mechanics-lubby2-shear-traction.md
+++ b/web/content/docs/benchmarks/small-deformations/mechanics-lubby2-shear-traction/index.md
@@ -17,14 +17,14 @@ weight = 112
We solve a non-linear small deformation problem on a cube with shear traction on the top boundary face. The 3D problem is setup identical to the corresponding 2D problem.
-See [this PDF](../lubby2.pdf) for detailed problem description.
+See [this PDF](lubby2.pdf) for detailed problem description.
## Results and evaluation
Result showing the displacement field and distortion relative to the initial configuration:
-{{< img src="../lubby2.png" >}}
+{{< img src="lubby2.png" >}}
Displacement of the top surface in the direction of the shear traction over time showing the elastic and viscous deformations (creep):
-{{< img src="../lubby2_creep_over_time.png" >}}
+{{< img src="lubby2_creep_over_time.png" >}}
diff --git a/web/content/docs/benchmarks/small-deformations/lubby2.pdf b/web/content/docs/benchmarks/small-deformations/mechanics-lubby2-shear-traction/lubby2.pdf
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/lubby2.pdf
rename to web/content/docs/benchmarks/small-deformations/mechanics-lubby2-shear-traction/lubby2.pdf
diff --git a/web/content/docs/benchmarks/small-deformations/lubby2.png b/web/content/docs/benchmarks/small-deformations/mechanics-lubby2-shear-traction/lubby2.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/lubby2.png
rename to web/content/docs/benchmarks/small-deformations/mechanics-lubby2-shear-traction/lubby2.png
diff --git a/web/content/docs/benchmarks/small-deformations/lubby2_creep_over_time.png b/web/content/docs/benchmarks/small-deformations/mechanics-lubby2-shear-traction/lubby2_creep_over_time.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/lubby2_creep_over_time.png
rename to web/content/docs/benchmarks/small-deformations/mechanics-lubby2-shear-traction/lubby2_creep_over_time.png
diff --git a/web/content/docs/benchmarks/small-deformations/dp_test.png b/web/content/docs/benchmarks/small-deformations/mechanics-plasticity-ehlers-specialcase-drucker-prager/dp_test.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/dp_test.png
rename to web/content/docs/benchmarks/small-deformations/mechanics-plasticity-ehlers-specialcase-drucker-prager/dp_test.png
diff --git a/web/content/docs/benchmarks/small-deformations/mechanics-plasticity-ehlers-specialcase-drucker-prager.md b/web/content/docs/benchmarks/small-deformations/mechanics-plasticity-ehlers-specialcase-drucker-prager/index.md
similarity index 92%
rename from web/content/docs/benchmarks/small-deformations/mechanics-plasticity-ehlers-specialcase-drucker-prager.md
rename to web/content/docs/benchmarks/small-deformations/mechanics-plasticity-ehlers-specialcase-drucker-prager/index.md
index 46f4fcdb685b5f56882c6ee3d89245b6e119f6d6..c4337fdb90e334cc610ec044c74c00bd22b11ead 100644
--- a/web/content/docs/benchmarks/small-deformations/mechanics-plasticity-ehlers-specialcase-drucker-prager.md
+++ b/web/content/docs/benchmarks/small-deformations/mechanics-plasticity-ehlers-specialcase-drucker-prager/index.md
@@ -21,8 +21,8 @@ The Ehlers material model can be reduced to the well-known criteria, such as the
Triaxial compression test:
-{{< img src="../ss_load.png" >}}
+{{< img src="ss_load.png" >}}
Variations of the stress states and the plastic volumetric strain with a monotonic loading process:
-{{< img src="../dp_test.png" >}}
+{{< img src="dp_test.png" >}}
diff --git a/web/content/docs/benchmarks/small-deformations/ss_load.png b/web/content/docs/benchmarks/small-deformations/mechanics-plasticity-ehlers-specialcase-drucker-prager/ss_load.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/ss_load.png
rename to web/content/docs/benchmarks/small-deformations/mechanics-plasticity-ehlers-specialcase-drucker-prager/ss_load.png
diff --git a/web/content/docs/benchmarks/small-deformations/Plasticity.pdf b/web/content/docs/benchmarks/small-deformations/mechanics-plasticity-single-surface/Plasticity.pdf
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/Plasticity.pdf
rename to web/content/docs/benchmarks/small-deformations/mechanics-plasticity-single-surface/Plasticity.pdf
diff --git a/web/content/docs/benchmarks/small-deformations/mechanics-plasticity-single-surface.md b/web/content/docs/benchmarks/small-deformations/mechanics-plasticity-single-surface/index.md
similarity index 80%
rename from web/content/docs/benchmarks/small-deformations/mechanics-plasticity-single-surface.md
rename to web/content/docs/benchmarks/small-deformations/mechanics-plasticity-single-surface/index.md
index 76f806fb4d06599c54590385bd7501e6b15a1e1f..83ecd9a511f5cdab8e731bd6524ff377f6673320 100644
--- a/web/content/docs/benchmarks/small-deformations/mechanics-plasticity-single-surface.md
+++ b/web/content/docs/benchmarks/small-deformations/mechanics-plasticity-single-surface/index.md
@@ -18,14 +18,14 @@ title = "Ehlers; Single-surface yield function"
We use a seven-parametric yield function for geomaterials to describe the plastic response. The traixial compression test is setup.
-See [this PDF](../Plasticity.pdf) for detailed problem description.
+See [this PDF](Plasticity.pdf) for detailed problem description.
## Results and evaluation
Triaxial compression test:
-{{< img src="../ss_load.png" >}}
+{{< img src="ss_load.png" >}}
Variations of the stress states and the plastic volumetric strain with a monotonic loading process:
-{{< img src="../plasticity_ss.png" >}}
+{{< img src="plasticity_ss.png" >}}
diff --git a/web/content/docs/benchmarks/small-deformations/plasticity_ss.png b/web/content/docs/benchmarks/small-deformations/mechanics-plasticity-single-surface/plasticity_ss.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/plasticity_ss.png
rename to web/content/docs/benchmarks/small-deformations/mechanics-plasticity-single-surface/plasticity_ss.png
diff --git a/web/content/docs/benchmarks/small-deformations/mechanics-plasticity-single-surface/ss_load.png b/web/content/docs/benchmarks/small-deformations/mechanics-plasticity-single-surface/ss_load.png
new file mode 120000
index 0000000000000000000000000000000000000000..848945c294176348e61f97b111a19ade8f98f433
--- /dev/null
+++ b/web/content/docs/benchmarks/small-deformations/mechanics-plasticity-single-surface/ss_load.png
@@ -0,0 +1 @@
+../mechanics-plasticity-ehlers-specialcase-drucker-prager/ss_load.png
\ No newline at end of file
diff --git a/web/content/docs/benchmarks/small-deformations/mechanics-slope-stability.md b/web/content/docs/benchmarks/small-deformations/mechanics-slope-stability/index.md
similarity index 83%
rename from web/content/docs/benchmarks/small-deformations/mechanics-slope-stability.md
rename to web/content/docs/benchmarks/small-deformations/mechanics-slope-stability/index.md
index 852357f671286846a0a7049fddb20b8bec3f03d0..6313c98c976d7ba11dbada6546fbbb1a6aeadf8f 100644
--- a/web/content/docs/benchmarks/small-deformations/mechanics-slope-stability.md
+++ b/web/content/docs/benchmarks/small-deformations/mechanics-slope-stability/index.md
@@ -17,4 +17,4 @@ title = "Strength reduction for slope stability"
## Problem description
We perform a strength reduction to determine the factor of safety of a slope.
-See [this PDF](../slope_stability.pdf) for detailed problem description.
+See [this PDF](slope_stability.pdf) for detailed problem description.
diff --git a/web/content/docs/benchmarks/small-deformations/slope_stability.pdf b/web/content/docs/benchmarks/small-deformations/mechanics-slope-stability/slope_stability.pdf
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/slope_stability.pdf
rename to web/content/docs/benchmarks/small-deformations/mechanics-slope-stability/slope_stability.pdf
diff --git a/web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC.md b/web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/index.md
similarity index 74%
rename from web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC.md
rename to web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/index.md
index 8e67734af15f3e8c23328cd54e8878f3179f2eae..3ba065bb2405a6767889e8383e29c9429e62c31a 100644
--- a/web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC.md
+++ b/web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/index.md
@@ -13,24 +13,24 @@ weight = 117
## Problem description
Five different benchmarks are reported in which pressure boundary conditions are tested: an axisymmetric elastic cylinder, a plain strain elastic cylinder, an axisymmetric elastic sphere, a tri-dimensional elastic sphere and an axisymmetric elasto-plastic sphere.
-See [this PDF](../pressure_bc.pdf) for detailed problem description.
+See [this PDF](pressure_bc.pdf) for detailed problem description.
## Results and evaluation
Plain strain elastic cylinder comparison between numerical and analytical results:
-{{< img src="../pipe_plane_strain.png" >}}
+{{< img src="pipe_plane_strain.png" >}}
Axisymmetric elastic cylinder comparison between numerical and analytical results.
-{{< img src="../pipe_axisymmetric.png" >}}
+{{< img src="pipe_axisymmetric.png" >}}
Axisymmetric elastic sphere comparison between numerical and analytical results:
-{{< img src="../sphere_axisymmetric.png" >}}
+{{< img src="sphere_axisymmetric.png" >}}
Tri-dimensional elastic sphere comparison between numerical and analytical results:
-{{< img src="../sphere_3d.png" >}}
+{{< img src="sphere_3d.png" >}}
Axisymmetric plastic sphere comparison between numerical and analytical results:
-{{< img src="../sphere_axisymmetric_pl.png" >}}
+{{< img src="sphere_axisymmetric_pl.png" >}}
Axisymmetric plastic sphere residuals of stress:
-{{< img src="../sphere_axisymmetric_pl_residual_stress.png" >}}
+{{< img src="sphere_axisymmetric_pl_residual_stress.png" >}}
diff --git a/web/content/docs/benchmarks/small-deformations/pressure_bc/pipe_axisymmetric.png b/web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/pipe_axisymmetric.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/pressure_bc/pipe_axisymmetric.png
rename to web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/pipe_axisymmetric.png
diff --git a/web/content/docs/benchmarks/small-deformations/pressure_bc/pipe_plane_strain.png b/web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/pipe_plane_strain.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/pressure_bc/pipe_plane_strain.png
rename to web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/pipe_plane_strain.png
diff --git a/web/content/docs/benchmarks/small-deformations/pressure_bc/pressure_bc.pdf b/web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/pressure_bc.pdf
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/pressure_bc/pressure_bc.pdf
rename to web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/pressure_bc.pdf
diff --git a/web/content/docs/benchmarks/small-deformations/pressure_bc/sphere_3d.png b/web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/sphere_3d.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/pressure_bc/sphere_3d.png
rename to web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/sphere_3d.png
diff --git a/web/content/docs/benchmarks/small-deformations/pressure_bc/sphere_axisymmetric.png b/web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/sphere_axisymmetric.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/pressure_bc/sphere_axisymmetric.png
rename to web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/sphere_axisymmetric.png
diff --git a/web/content/docs/benchmarks/small-deformations/pressure_bc/sphere_axisymmetric_pl.png b/web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/sphere_axisymmetric_pl.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/pressure_bc/sphere_axisymmetric_pl.png
rename to web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/sphere_axisymmetric_pl.png
diff --git a/web/content/docs/benchmarks/small-deformations/pressure_bc/sphere_axisymmetric_pl_residual_stress.png b/web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/sphere_axisymmetric_pl_residual_stress.png
similarity index 100%
rename from web/content/docs/benchmarks/small-deformations/pressure_bc/sphere_axisymmetric_pl_residual_stress.png
rename to web/content/docs/benchmarks/small-deformations/pressure_bc/Pressure_BC/sphere_axisymmetric_pl_residual_stress.png
diff --git a/web/content/docs/benchmarks/stokes-flow/Fig1_SchematicDiagram.png b/web/content/docs/benchmarks/stokes-flow/parallel-plate-flow/Fig1_SchematicDiagram.png
similarity index 100%
rename from web/content/docs/benchmarks/stokes-flow/Fig1_SchematicDiagram.png
rename to web/content/docs/benchmarks/stokes-flow/parallel-plate-flow/Fig1_SchematicDiagram.png
diff --git a/web/content/docs/benchmarks/stokes-flow/Fig2_SimulationResults.png b/web/content/docs/benchmarks/stokes-flow/parallel-plate-flow/Fig2_SimulationResults.png
similarity index 100%
rename from web/content/docs/benchmarks/stokes-flow/Fig2_SimulationResults.png
rename to web/content/docs/benchmarks/stokes-flow/parallel-plate-flow/Fig2_SimulationResults.png
diff --git a/web/content/docs/benchmarks/stokes-flow/parallel-plate-flow.md b/web/content/docs/benchmarks/stokes-flow/parallel-plate-flow/index.md
similarity index 86%
rename from web/content/docs/benchmarks/stokes-flow/parallel-plate-flow.md
rename to web/content/docs/benchmarks/stokes-flow/parallel-plate-flow/index.md
index eb5f011022044f9f7ebc2316097a28944535519e..75e3e30ee8aba473021177a24350d35652bf8e97 100644
--- a/web/content/docs/benchmarks/stokes-flow/parallel-plate-flow.md
+++ b/web/content/docs/benchmarks/stokes-flow/parallel-plate-flow/index.md
@@ -17,7 +17,7 @@ title = "Fluid flow through an open parallel-plate channel"
This benchmark deals with fluid flow through an open parallel-plate channel. The figure below gives a pictorial view of the considered scenario.
-{{< img src="../Fig1_SchematicDiagram.png" title="Schematic diagram of the parallel-plate flow channel in two-dimensional space.">}}
+{{< img src="Fig1_SchematicDiagram.png" title="Schematic diagram of the parallel-plate flow channel in two-dimensional space.">}}
The model parameters used in the simulation are summarized in the table below.
@@ -47,7 +47,7 @@ $$
v \left(y\right) = \frac{1}{2\mu} \frac{P_{\mathrm{in}} - P_{\mathrm{out}}}{l} y \left( b - y\right).
\end{equation}$$
-{{< img src="../Fig2_SimulationResults.png" title="Simulation results: (a) Hydrualic pressure profile through the parallel-plate flow channel; (b) Transverse velocity component profile over the cross-section of the plane flow channel.">}}
+{{< img src="Fig2_SimulationResults.png" title="Simulation results: (a) Hydrualic pressure profile through the parallel-plate flow channel; (b) Transverse velocity component profile over the cross-section of the plane flow channel.">}}
## References
diff --git a/web/content/docs/benchmarks/thermal-two-phase-flow/heat-pipe-problem.pdf b/web/content/docs/benchmarks/thermal-two-phase-flow/heat-pipe/heat-pipe-problem.pdf
similarity index 100%
rename from web/content/docs/benchmarks/thermal-two-phase-flow/heat-pipe-problem.pdf
rename to web/content/docs/benchmarks/thermal-two-phase-flow/heat-pipe/heat-pipe-problem.pdf
diff --git a/web/content/docs/benchmarks/thermal-two-phase-flow/heat-pipe.md b/web/content/docs/benchmarks/thermal-two-phase-flow/heat-pipe/index.md
similarity index 85%
rename from web/content/docs/benchmarks/thermal-two-phase-flow/heat-pipe.md
rename to web/content/docs/benchmarks/thermal-two-phase-flow/heat-pipe/index.md
index dd26136be4123bc1a70863aa96a369fb13c5abc4..047d220a48422a1b47dba87f526e116acbd33306 100644
--- a/web/content/docs/benchmarks/thermal-two-phase-flow/heat-pipe.md
+++ b/web/content/docs/benchmarks/thermal-two-phase-flow/heat-pipe/index.md
@@ -19,4 +19,4 @@ This benchmark is dedicated to simulating the non-isothermal two-phase flow in p
## Problem setting
-See [this PDF](../heat-pipe-problem.pdf) for the detailed problem setting.
+See [this PDF](heat-pipe-problem.pdf) for the detailed problem setting.
diff --git a/web/content/docs/benchmarks/thermo-hydro-mechanics/images/errordispl_vs_t.png b/web/content/docs/benchmarks/thermo-hydro-mechanics/consolidation_pointheatsource/errordispl_vs_t.png
similarity index 100%
rename from web/content/docs/benchmarks/thermo-hydro-mechanics/images/errordispl_vs_t.png
rename to web/content/docs/benchmarks/thermo-hydro-mechanics/consolidation_pointheatsource/errordispl_vs_t.png
diff --git a/web/content/docs/benchmarks/thermo-hydro-mechanics/images/errorpT_vs_t.png b/web/content/docs/benchmarks/thermo-hydro-mechanics/consolidation_pointheatsource/errorpT_vs_t.png
similarity index 100%
rename from web/content/docs/benchmarks/thermo-hydro-mechanics/images/errorpT_vs_t.png
rename to web/content/docs/benchmarks/thermo-hydro-mechanics/consolidation_pointheatsource/errorpT_vs_t.png
diff --git a/web/content/docs/benchmarks/thermo-hydro-mechanics/consolidation_pointheatsource.md b/web/content/docs/benchmarks/thermo-hydro-mechanics/consolidation_pointheatsource/index.md
similarity index 96%
rename from web/content/docs/benchmarks/thermo-hydro-mechanics/consolidation_pointheatsource.md
rename to web/content/docs/benchmarks/thermo-hydro-mechanics/consolidation_pointheatsource/index.md
index 146a3f0eb8de8ae07b2a2a694a902a23e6fa77d9..b47a4370772adf2cf43bbfee7b313d495a36f003 100644
--- a/web/content/docs/benchmarks/thermo-hydro-mechanics/consolidation_pointheatsource.md
+++ b/web/content/docs/benchmarks/thermo-hydro-mechanics/consolidation_pointheatsource/index.md
@@ -92,19 +92,19 @@ For the stress components the corrected expressions can be found in the work of
The analytical expressions (12-16) together with the numerical model can now be evaluated at different points as a function of time or for a given time as a function of their spatial coordinates.
The results below were taken from the benchmark published in Chaudhry et al. (2019) and might slightly differ from the benchmark in the OGS6 repo.
-{{< img src="../images/resp_vs_t_square.png" >}}
+{{< img src="resp_vs_t_square.png" >}}
In the pictures above, the analytical and numerical results for temperature ($T$), pressure ($p$), displacement ($u_i$) and stress ($\sigma_{ij}$) are plotted as function of time ($t$) at point $P=(1.3,0.682,0.0)$ and along the radial coordinate ($r$ ) at time $t=5\cdot 10^5$ (below).
-{{< img src="../images/resp_vs_x_square.png" >}}
+{{< img src="resp_vs_x_square.png" >}}
(Figures were taken from Chaudhry et al. (2019).)
The absolute errors between OGS6 and the analytical solution for temperature, pressure, and displacement are depicted below. For all three response variables, one observes that the error reaches its maximum around the same time when also the slope of the response variable is maximal.
-{{< img src="../images/errorpT_vs_t.png" >}}
+{{< img src="errorpT_vs_t.png" >}}
-{{< img src="../images/errordispl_vs_t.png" >}}
+{{< img src="errordispl_vs_t.png" >}}
## References
diff --git a/web/content/docs/benchmarks/thermo-hydro-mechanics/images/resp_vs_t_square.png b/web/content/docs/benchmarks/thermo-hydro-mechanics/consolidation_pointheatsource/resp_vs_t_square.png
similarity index 100%
rename from web/content/docs/benchmarks/thermo-hydro-mechanics/images/resp_vs_t_square.png
rename to web/content/docs/benchmarks/thermo-hydro-mechanics/consolidation_pointheatsource/resp_vs_t_square.png
diff --git a/web/content/docs/benchmarks/thermo-hydro-mechanics/images/resp_vs_x_square.png b/web/content/docs/benchmarks/thermo-hydro-mechanics/consolidation_pointheatsource/resp_vs_x_square.png
similarity index 100%
rename from web/content/docs/benchmarks/thermo-hydro-mechanics/images/resp_vs_x_square.png
rename to web/content/docs/benchmarks/thermo-hydro-mechanics/consolidation_pointheatsource/resp_vs_x_square.png
diff --git a/web/content/docs/benchmarks/thermo-mechanical-phase-field/thermo-mechanical-phase-field.md b/web/content/docs/benchmarks/thermo-mechanical-phase-field/thermo-mechanical-phase-field/index.md
similarity index 94%
rename from web/content/docs/benchmarks/thermo-mechanical-phase-field/thermo-mechanical-phase-field.md
rename to web/content/docs/benchmarks/thermo-mechanical-phase-field/thermo-mechanical-phase-field/index.md
index b681068a5a2ba8d86e1687d1853f6d0505e1918b..cf9e35c57f859d3d46e2fbeaf0922f93dcfcdf0d 100644
--- a/web/content/docs/benchmarks/thermo-mechanical-phase-field/thermo-mechanical-phase-field.md
+++ b/web/content/docs/benchmarks/thermo-mechanical-phase-field/thermo-mechanical-phase-field/index.md
@@ -24,9 +24,9 @@ The thermal expansion test was implemented by imposing a temperature increase to
Results show Phase-Field evolution in the thermo-mechanical case can follow the mechanical case, and both solutions correspond to the analytical solution:
-{{< img src="../uncon_com_bc.png" >}}
-{{< img src="../therm_exp_bc.png" >}}
-{{< img src="../t_pf.png" >}}
+{{< img src="uncon_com_bc.png" >}}
+{{< img src="therm_exp_bc.png" >}}
+{{< img src="t_pf.png" >}}
The analytical solution is: $$d = \dfrac{G\textrm{c}}{G\textrm{c}+4\epsilon \psi_\textrm{e}^+}$$
where due to negative (elastic) volume strains only the deviatoric energy drives the phase field.
diff --git a/web/content/docs/benchmarks/thermo-mechanical-phase-field/t_pf.png b/web/content/docs/benchmarks/thermo-mechanical-phase-field/thermo-mechanical-phase-field/t_pf.png
similarity index 100%
rename from web/content/docs/benchmarks/thermo-mechanical-phase-field/t_pf.png
rename to web/content/docs/benchmarks/thermo-mechanical-phase-field/thermo-mechanical-phase-field/t_pf.png
diff --git a/web/content/docs/benchmarks/thermo-mechanical-phase-field/therm_exp_bc.png b/web/content/docs/benchmarks/thermo-mechanical-phase-field/thermo-mechanical-phase-field/therm_exp_bc.png
similarity index 100%
rename from web/content/docs/benchmarks/thermo-mechanical-phase-field/therm_exp_bc.png
rename to web/content/docs/benchmarks/thermo-mechanical-phase-field/thermo-mechanical-phase-field/therm_exp_bc.png
diff --git a/web/content/docs/benchmarks/thermo-mechanical-phase-field/uncon_com_bc.png b/web/content/docs/benchmarks/thermo-mechanical-phase-field/thermo-mechanical-phase-field/uncon_com_bc.png
similarity index 100%
rename from web/content/docs/benchmarks/thermo-mechanical-phase-field/uncon_com_bc.png
rename to web/content/docs/benchmarks/thermo-mechanical-phase-field/thermo-mechanical-phase-field/uncon_com_bc.png
diff --git a/web/content/docs/benchmarks/thermo-mechanics/thermomechanics.md b/web/content/docs/benchmarks/thermo-mechanics/thermomechanics/index.md
similarity index 93%
rename from web/content/docs/benchmarks/thermo-mechanics/thermomechanics.md
rename to web/content/docs/benchmarks/thermo-mechanics/thermomechanics/index.md
index f40ab2db05523a014cc0becd363feaf5e52adcf6..08f1ac3673fddd021c6a30150c5d767a7f0bc9c1 100644
--- a/web/content/docs/benchmarks/thermo-mechanics/thermomechanics.md
+++ b/web/content/docs/benchmarks/thermo-mechanics/thermomechanics/index.md
@@ -25,8 +25,8 @@ al. \cite Kolditz2012 for detailed problem description.
Result showing temperature and stresses development with time in the centre node
of the model:
-{{< img src="../temperature.png" >}}
-{{< img src="../stress.png" >}}
+{{< img src="temperature.png" >}}
+{{< img src="stress.png" >}}
The analytical solution of stresses after heating is:
$$\begin{equation}
diff --git a/web/content/docs/benchmarks/thermo-mechanics/stress.png b/web/content/docs/benchmarks/thermo-mechanics/thermomechanics/stress.png
similarity index 100%
rename from web/content/docs/benchmarks/thermo-mechanics/stress.png
rename to web/content/docs/benchmarks/thermo-mechanics/thermomechanics/stress.png
diff --git a/web/content/docs/benchmarks/thermo-mechanics/temperature.png b/web/content/docs/benchmarks/thermo-mechanics/thermomechanics/temperature.png
similarity index 100%
rename from web/content/docs/benchmarks/thermo-mechanics/temperature.png
rename to web/content/docs/benchmarks/thermo-mechanics/thermomechanics/temperature.png
diff --git a/web/content/docs/benchmarks/thermo-richards-mechanics/CTF1_results_S.jpg b/web/content/docs/benchmarks/thermo-richards-mechanics/CTF1/CTF1_results_S.jpg
similarity index 100%
rename from web/content/docs/benchmarks/thermo-richards-mechanics/CTF1_results_S.jpg
rename to web/content/docs/benchmarks/thermo-richards-mechanics/CTF1/CTF1_results_S.jpg
diff --git a/web/content/docs/benchmarks/thermo-richards-mechanics/CTF1_results_T.jpg b/web/content/docs/benchmarks/thermo-richards-mechanics/CTF1/CTF1_results_T.jpg
similarity index 100%
rename from web/content/docs/benchmarks/thermo-richards-mechanics/CTF1_results_T.jpg
rename to web/content/docs/benchmarks/thermo-richards-mechanics/CTF1/CTF1_results_T.jpg
diff --git a/web/content/docs/benchmarks/thermo-richards-mechanics/CTF1.md b/web/content/docs/benchmarks/thermo-richards-mechanics/CTF1/index.md
similarity index 91%
rename from web/content/docs/benchmarks/thermo-richards-mechanics/CTF1.md
rename to web/content/docs/benchmarks/thermo-richards-mechanics/CTF1/index.md
index cd85497d153f64f3c89ce53cd72f63ca3c833861..921e43af4dcfebfa994f4ab0a939d2f63d4d4e83 100644
--- a/web/content/docs/benchmarks/thermo-richards-mechanics/CTF1.md
+++ b/web/content/docs/benchmarks/thermo-richards-mechanics/CTF1/index.md
@@ -26,8 +26,8 @@ specific heat capacity of solid phase has already taken account of
The following figures compare the results of this test against the results
presented in [[2]](#2):
-<img src="../CTF1_results_T.jpg" alt="drawing" width="400"/>
-<img src="../CTF1_results_S.jpg" alt="drawing" width="400"/>
+<img src="CTF1_results_T.jpg" alt="drawing" width="400"/>
+<img src="CTF1_results_S.jpg" alt="drawing" width="400"/>
## References
<a id="1">[1]</a>
diff --git a/web/content/docs/benchmarks/thermo-richards-mechanics/decovalex_2023_c.png b/web/content/docs/benchmarks/thermo-richards-mechanics/DECOVALEX2023-TaskC/decovalex_2023_c.png
similarity index 100%
rename from web/content/docs/benchmarks/thermo-richards-mechanics/decovalex_2023_c.png
rename to web/content/docs/benchmarks/thermo-richards-mechanics/DECOVALEX2023-TaskC/decovalex_2023_c.png
diff --git a/web/content/docs/benchmarks/thermo-richards-mechanics/decovalex_2023_c_S_t.png b/web/content/docs/benchmarks/thermo-richards-mechanics/DECOVALEX2023-TaskC/decovalex_2023_c_S_t.png
similarity index 100%
rename from web/content/docs/benchmarks/thermo-richards-mechanics/decovalex_2023_c_S_t.png
rename to web/content/docs/benchmarks/thermo-richards-mechanics/DECOVALEX2023-TaskC/decovalex_2023_c_S_t.png
diff --git a/web/content/docs/benchmarks/thermo-richards-mechanics/decovalex_2023_c_T_t.png b/web/content/docs/benchmarks/thermo-richards-mechanics/DECOVALEX2023-TaskC/decovalex_2023_c_T_t.png
similarity index 100%
rename from web/content/docs/benchmarks/thermo-richards-mechanics/decovalex_2023_c_T_t.png
rename to web/content/docs/benchmarks/thermo-richards-mechanics/DECOVALEX2023-TaskC/decovalex_2023_c_T_t.png
diff --git a/web/content/docs/benchmarks/thermo-richards-mechanics/DECOVALEX2023-TaskC.md b/web/content/docs/benchmarks/thermo-richards-mechanics/DECOVALEX2023-TaskC/index.md
similarity index 91%
rename from web/content/docs/benchmarks/thermo-richards-mechanics/DECOVALEX2023-TaskC.md
rename to web/content/docs/benchmarks/thermo-richards-mechanics/DECOVALEX2023-TaskC/index.md
index bd9a0010784b079292441f59cb8965b44047b0ed..251df7ef2aa02340587f1316c7fc3c3e04a739c7 100644
--- a/web/content/docs/benchmarks/thermo-richards-mechanics/DECOVALEX2023-TaskC.md
+++ b/web/content/docs/benchmarks/thermo-richards-mechanics/DECOVALEX2023-TaskC/index.md
@@ -35,13 +35,13 @@ The test is used to mainly verify the implementation of water vapour diffusion m
Task C. The following figure shows the distribution of temperature in the domain,
water saturation in the vicinity of the heater, and displacement magnitude
in the domain after nearly 3 years' heating:
-{{< img src="../decovalex_2023_c.png" >}}
+{{< img src="decovalex_2023_c.png" >}}
The following two figures show the temporal variations of temperature and water
saturation, respectively, at a node near the heater:
-<img src="../decovalex_2023_c_T_t.png" alt="drawing" width="450"/>
-<img src="../decovalex_2023_c_S_t.png" alt="drawing" width="450"/>
+<img src="decovalex_2023_c_T_t.png" alt="drawing" width="450"/>
+<img src="decovalex_2023_c_S_t.png" alt="drawing" width="450"/>
As shown the water saturation variation curve, the de-saturation -
re-saturation process is well captured by the numerical simulation.
diff --git a/web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-liakopoulos.md b/web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-liakopoulos/index.md
similarity index 95%
rename from web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-liakopoulos.md
rename to web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-liakopoulos/index.md
index 01d306ce99016bc282ec98570fac7cb4a920e016..acc84aa4f58d3386ee5b9cb9c0ae0ea8d28198fb 100644
--- a/web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-liakopoulos.md
+++ b/web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-liakopoulos/index.md
@@ -19,4 +19,4 @@ One benchmark -- Liakopoulos experiment is presented here. The benchmark is appl
## Results and evaluation
-See [this PDF](../main.pdf).
+See [this PDF](main.pdf).
diff --git a/web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-liakopoulos/main.pdf b/web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-liakopoulos/main.pdf
new file mode 120000
index 0000000000000000000000000000000000000000..6ce042b9c71d7723f4f29d14978ef576232c4d88
--- /dev/null
+++ b/web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-liakopoulos/main.pdf
@@ -0,0 +1 @@
+../two-phase-flow-pp-mcwhorter/main.pdf
\ No newline at end of file
diff --git a/web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-mcwhorter.md b/web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-mcwhorter/index.md
similarity index 96%
rename from web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-mcwhorter.md
rename to web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-mcwhorter/index.md
index 8805ac9059879ed9a6d94f1502b9a1a67bdc28a5..116699f3fd1e545415296e2e83710a8452d5f6e4 100644
--- a/web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-mcwhorter.md
+++ b/web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-mcwhorter/index.md
@@ -19,4 +19,4 @@ One benchmark -- McWhorter problem is presented here which is dedicated to simul
## Results and evaluation
-See [this PDF](../main.pdf).
+See [this PDF](main.pdf).
diff --git a/web/content/docs/benchmarks/two-phase-flow-pp-form/main.pdf b/web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-mcwhorter/main.pdf
similarity index 100%
rename from web/content/docs/benchmarks/two-phase-flow-pp-form/main.pdf
rename to web/content/docs/benchmarks/two-phase-flow-pp-form/two-phase-flow-pp-mcwhorter/main.pdf
diff --git a/web/content/docs/benchmarks/two-phase-flow/MoMaS.pdf b/web/content/docs/benchmarks/two-phase-flow/momas/MoMaS.pdf
similarity index 100%
rename from web/content/docs/benchmarks/two-phase-flow/MoMaS.pdf
rename to web/content/docs/benchmarks/two-phase-flow/momas/MoMaS.pdf
diff --git a/web/content/docs/benchmarks/two-phase-flow/momas.md b/web/content/docs/benchmarks/two-phase-flow/momas/index.md
similarity index 94%
rename from web/content/docs/benchmarks/two-phase-flow/momas.md
rename to web/content/docs/benchmarks/two-phase-flow/momas/index.md
index 41f736486029a51fc265b32e23dc161c531cba27..f69f429d95397e9937dccf3d3d9096316218b6af 100644
--- a/web/content/docs/benchmarks/two-phase-flow/momas.md
+++ b/web/content/docs/benchmarks/two-phase-flow/momas/index.md
@@ -19,4 +19,4 @@ This benchmark is dedicated to simulate the two-phase two-component flow in poro
## Results and evaluation
-See [this PDF](../MoMaS.pdf).
+See [this PDF](MoMaS.pdf).