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Appendix A Nomenclature BRi flux of ith component in the bottom reflux stream (gmol m−2 sec−1) Ci gas-phase concentration of ith component (gmol m−3) Cpig heat capacity of ith component (J gmol−1 K−1) Cps heat capacity of the adsorbent (J kg−1 K−1) D Adsorbent bed diameter (m) DK Knudsen diffusivity of ith component (m2/s) DL Axial dispersion (m2/s) Dm,i Bulk diffusivity of ith component (m2/s) Dp,i Macropore diffusivity of ith component (m2/s) dp particle diameter (m) Fi input flux of ith component to the co-current bed (gmol m−2 sec−1) h total gas-phase enthalpy (J m−3) hw fluid-to-wall heat transfer coefficient (J m−2 sec−1 K−1) ∆Hads isosteric heat of adsorption (J gmol−1) i HPi flux of ith component in the heavy product stream (gmol m−2 sec−1) KL effective axial thermal conductivity (J m−1 sec−1 K−1) ki lumped mass transfer coefficient for ith component (sec−1) kiH Henry’s constant (gmol kg−1 kPa−1) L bed length (m) LPi flux of ith component in the light product stream (gmol m−2 sec−1) Chapter A. Nomenclature 206PDF Image | Design and Operation of Pressure Swing Adsorption Processes
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