A calculational model is proposed for the pore-diffusion based PSA. In prin
ciple the model is identical with that of the previous work on the surface-
diffusion based PSA, except for the diffusion coefficient being inversely p
roportional to pressure. From the calculation for a methane-activated carbo
n system it is found that the increase in the intraparticle diffusion coeff
icient in the depressurization stage increases desorption, but a considerab
le desorption still occurs in the purge stage. In this work we also show th
at the maximal discharge of sorbate mass increases when the depressurizatio
n is accomplished in a short time. The process consisted of the adsorption,
depressurization and purge stages is compared with the process having only
the adsorption and purge stages in terms of the discharge of sorbate mass
and the volume of gas leaving the column bottom.