Title of article :
Pressure ratio and its impact on membrane gas separation processes
Author/Authors :
Yu Huang، نويسنده , , Tim C. Merkel، نويسنده , , Richard W. Baker، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2014
Pages :
8
From page :
33
To page :
40
Abstract :
The feed and permeate pressures achievable in most gas separations are limited by economics. As a result, commercial membrane separation processes usually operate with a feed-to-permeate pressure ratio (θ) in the range of 5–15. This limited pressure ratio means that the optimum membrane may not be the one with the highest selectivity; rather, a membrane with lower selectivity, but tailored to the pressure ratio, may result in a more economical process. In other words, when a process is pressure ratio limited, the useful selectivity is also limited. The balance between pressure ratio and selectivity is often ignored by membrane developers. The importance of this balance is illustrated with two applications of current interest: CO2 capture from power plant flue gas, and dehydration of azeotropic bioethanol.
Keywords :
PDMS , Grafting , Porous alumina , Vapor phase deposition , Solvent nanofiltration
Journal title :
Journal of Membrane Science
Serial Year :
2014
Journal title :
Journal of Membrane Science
Record number :
1360611
Link To Document :
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