Abstract
In this chapter, the first real-world scenario is simulated using the model developed in Chap. 2.
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- 1.
Except for the variations in temperature and pressure, arising from the nonisothermal formulation and the adsorption processes, that can lead to variations of the fluid velocity across the bed cross section.
- 2.
For thermal energy storage. We thought that thermochemical heat storage is so important that it must become the thermal energy storage process in OGS-6.
- 3.
As long as it stays below some sensible limit, of course. The equilibrium vapour pressure (i.e. 100% relative humidity) is such a sensible upper limit.
- 4.
Notwithstanding the fact that the equation system assembly is not parallelized, yet.
- 5.
For a surface whose normal points along the z-direction (i.e. y-direction inside OGS-6).
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Lehmann, C., Kolditz, O., Nagel, T. (2018). Laboratory-Scale Adsorption Chamber Simulation. In: Models of Thermochemical Heat Storage. SpringerBriefs in Energy(). Springer, Cham. https://doi.org/10.1007/978-3-319-71523-0_4
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DOI: https://doi.org/10.1007/978-3-319-71523-0_4
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