This paper presents various aspects of modeling, simulation, design, and op
timization of membrane-based gas separation systems. A model for counter- a
nd crosscurrent membrane modules and an efficient numerical solution proced
ure based on orthogonal collocation to solve the differential model equatio
ns have been developed. The model handles multicomponent mixtures and consi
ders effects of pressure drop and energy balance. The model and solution pr
ocedure are combined in a versatile unit which can be conveniently used in
a process simulator. The solution procedure allows analytical calculation o
f sensitivities. The membrane module has been implemented and tested in an
external process simulator, OPTISIM, which is based on the equation-oriente
d approach. The cost optimization features of OPTISIM have then been used t
o investigate hybrid schemes for CO pretreatment of steam reformer gas:The
traditional cold box has been modified with a membrane unit and the results
of the cost optimization calculations are presented. (C) 1999 Elsevier Sci
ence Ltd. All rights reserved.