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Chapter 6. Design and Environmental Impact Analysis of a Hybrid PSA-Membrane Separation System Figure 6.3: The hybrid PSA-membrane flow sheet chosen for the optimization studies 6. It is also assumed that tube side retentate is mixed with the usual PSA feed at PSA feed pressure and temperature. In practice, this requires a compressor and heat exchanger system. In the current simulation study, the model ignores calculating the heat and work load for these equipments. 7. The shell side permeate coming out of the membrane and the remaining off gases (as 2 SLPM is removed constantly) forms the off gas from the hybrid. Figure 6.3, depicts the graphical overview of the proposed hybrid PSA-membrane configuration considered in this study. 6.4.1 Parameter Selection and Performance Indicators Two important parameters are chosen for assessing the performance of the hybrid PSA-membrane separation system. First in the list is the area of membrane, as this plays an important role in achieving a desired CO2 purity and recovery from 150PDF Image | Operation and Control of Pressure Swing Adsorption Systems
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