Modeling of gas permeation in hollow-fiber or spiral wound modules nec
essitates considering the effect of permeate pressure variation along
the module length which could have a significant effect on the predict
ion of the exit compositions and membrane area requirements depending
on the membrane characteristics and module geometry. The transport equ
ations governing the permeator performance are a set of coupled nonlin
ear differential equations. The complexity of the solution procedure f
or these equations increases with the number of components in the mixt
ure and consideration of pressure variation. Thus, there is a need for
simplified solution methodologies which could reduce the computationa
l efforts. This paper presents a solution methodology to solve the mul
ticomponent gas permeator transport equations in a countercurrent flow
pattern, taking the permeate pressure variation into consideration. T
he present method yields analytical expressions for flow rates, permea
te pressure, membrane area, and compositions along the length of the p
ermeator.