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product is diverted into purging and repressurizing the other bed. The amount of product that is diverted to the purge and pressurization step is enough to keep the pressure constant during the feed step and to complete the purge and pressurization of the second bed. When w e calculate the number of moles used for purge and pressurization we can calculate the final number of moles still available as product. This calculation is done in section 3.2.5 after the number of moles required for purge (Npu) and pressurization (NPR) are known. We can now calculate the work done by the system during the feed step: Where: NFRT Upon mtegrating and substituting we find: B yPHJ PA Wf=1W2+2W3 (3.15) (3.16) (3.17) (3.18) 0)dV 50PDF Image | Energy Efficiency of Gas Separation Pressure Swing Adsorption
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