Design and Operation of Pressure Swing Adsorption Processes

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Design and Operation of Pressure Swing Adsorption Processes ( design-and-operation-pressure-swing-adsorption-processes )

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Greek Letters α fraction of the heavy product going as a bottom reflux β fraction of the light product going as a top reflux εb bulk void fraction εp adsorbent particle void fraction γ heat capacity ratio (=1.4) μ gas viscosity (kg m−1 sec−1 ) ηc efficiency of the feed compressor ηfg efficiency of the flue gas compressor ηh efficiency of the heavy product compressor ηv efficiency of the vacuum generator φ fraction of the feed going to the co-current bed ρb bulk density (kg m−3 ) ρg average gas density (kg m−3 ) ρs adsorbent density (kg m−3) τ Tortuosity factor Subscripts des desorption step pres pressurization step Chapter A. Nomenclature 208

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