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Commit 31fdc0fc authored by Boyan Meng's avatar Boyan Meng
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[web] Update URL in docu

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......@@ -31,4 +31,4 @@ Some remarks:
2\. The `TwoPhaseFlowWithPrho` process assumes that the main component of the gas phase can be dissolved in the liquid phase. Water evaporation is neglected here. The appearance/disappearance of the gas phase is controlled by the solubility (given by the Henry's Law) of the gaseous component, e.g. H2. It is therefore most suitable for nuclear waste repository (see the [MoMaS benchmark]({{< ref "docs/benchmarks/two-phase-flow/momas" >}})) or CO2 storage problems.
3\. The `ThermalTwoPhaseFlowWithPP` process simulates the temperature-dependent two-phase flow and moisture transport. Water evaporation and recondensation can be modeled thanks to that the gas phase is compositional. This process is most favorably used for shallow geothermal applications (e.g. borehole thermal energy storage), especially in unsaturated soils (see the [heat pipe benchmark]({{< ref "docs/benchmarks/thermal-two-phase-flow/heat-pipe" >}})).
3\. The `ThermalTwoPhaseFlowWithPP` process simulates the temperature-dependent two-phase flow and moisture transport. Water evaporation and recondensation can be modeled thanks to that the gas phase is compositional. This process is most favorably used for shallow geothermal applications (e.g. borehole thermal energy storage), especially in unsaturated soils (see the [heat pipe benchmark]({{< ref "docs/benchmarks/notebooks/heatpipe" >}})).
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