Some Energetic Aspects of Gas Phase Adsorption Systems

Mersmann, Alfons; Schweighart, Peter J.; Sievers, W.

doi:10.1007/978-94-011-1454-7_35

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Tsa Processes1

The Energy-saving Potential1

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2000

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“…This result has been confirmed by calculations carried out for a case study which refers to the desorption of CO 2 from MS 5A by hot air [10]. The desorption temperature has been varied between 60 C and 200 C and became independent of the gas velocity at a temperature of 200 C.…”

Section: Tsa Processessupporting

confidence: 58%

“…Dealing with purge gas regeneration, the energy is proportional to the purge gas volume Vand in PSA the compression work increases with the gas volume handled. The energy input H is the sum of the (here assumed) isothermal compressor work which is necessary to overcome the pressure drop or pressure increase Dp of the gas volume V and the heat (neglecting kinetic and potential energies) [9,10]:…”

Section: The Energy-saving Potentialmentioning

confidence: 99%

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