fiber membranes;
gas separation;
membrane modeling;
D O I:
10.1016/0376-7388(96)00128-7
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
Corrected solutions for analytical models, originally presented by Rautenbach and Dahm [1], for membrane-based binary gas separation are presented. These models are based on constant pressure in the feed and permeate streams and perfect-mixing in the permeate stream. A comparison of these models with more complete numerical solutions suggests that the analytical models provide excellent short-cut, preliminary design information. The analytical solutions may also be used to assist convergence of more complete numerical methods.