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Feed NF m oles Aftercooler Compressor mole fraction yo J ^ Wp Cooling Water Twi mole fraction yE Figure 4.1 System used byBanerjee etal. with Adiabatic Compressor andAftercooler. As the current work is more concerned with the energy losses during the PSA process itself, we assume that the entire process is isothermal, which combines the function of the adiabatic compressor and the aftercooler into one isothermal compressor. This isothermal system is shown in Figure 4.2, and is similar to Figure 4.1 in that the availability of the gases at points 1, 3, 4 and 5 are identical. -*• Product Np2 moles m ole fraction y p Exhaust NE moles mole fraction yE Figure 4.2 Isothermal System toCompare theBanerjee etal. Exergy Analysis totheCurrentAnalysis. WF Feed —r- NF moles 1 ••T-• + mole fraction y 0 isothermal Compressor, T|T= 1 i—'-n i — i Product Np2 moles mole fraction yp Exhaust NE moles 98PDF Image | Energy Efficiency of Gas Separation Pressure Swing Adsorption
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