Ab. Hinchliffe et Ke. Porter, GAS SEPARATION USING MEMBRANES .1. OPTIMIZATION OF THE SEPARATION PROCESS USING NEW COST PARAMETERS, Industrial & engineering chemistry research, 36(3), 1997, pp. 821-829
This is the first in a series of papers presenting new concepts for th
e development of membranes for gas separation. In this paper two new c
ost parameters, which are useful for costing and optimization of membr
ane gas separation systems, are described. The new parameters, cost pe
rmeability and effective selectivity, can be used to show the directio
n to be taken in membrane research and development. The new parameters
are shown to predict accurately the cost of membrane separation plant
by correlating bids from membrane plant suppliers using the new param
eters with cross-flow design equations. The parameters are used to opt
imize the membrane gas separation of hydrogen and carbon monoxide for
two commercially available membrane systems in a process to manufactur
e acetic acid. The membrane separation is compared with the currently
used method, cryogenic flash distillation. Economic evaluation methods
are developed to compare different separation methods so that the pro
cess as a whole can be optimized. The evaluation shows that, for membr
ane gas separation, it is important to find the optimum degree of sepa
ration; when membrane separation is evaluated at the separation specif
ication for the established cryogenic method, membranes are not compet
itive; however, when the process is optimized for membrane separation,
the cost of separation reduces to less than 60% of the cryogenic sepa
ration.