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CO 2 Plasticization of polyethersulfone/polyimide gas‐separation membranes
Author(s) -
Kapantaidakis G. C.,
Koops G. H.,
Wessling M.,
Kaldis S. P.,
Sakellaropoulos G. P.
Publication year - 2003
Publication title -
aiche journal
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.958
H-Index - 167
eISSN - 1547-5905
pISSN - 0001-1541
DOI - 10.1002/aic.690490710
Subject(s) - permeance , membrane , gas separation , polyimide , plasticizer , permeation , materials science , chemical engineering , membrane technology , selectivity , fiber , polymer chemistry , analytical chemistry (journal) , chemistry , chromatography , composite material , organic chemistry , layer (electronics) , biochemistry , engineering , catalysis
Abstract This work reports the CO 2 plasticization of gas‐separation hollow‐fiber membranes based on polyimide and polyethersulfone blends. The feed pressure effect on the permeance of pure gases (CO 2 , N 2 ) and the separation performance of a gaseous mixture (CO 2 /N 2 , 55/45%) is examined. Contrary to dense membranes, the permeance of CO 2 through ultrathin asymmetric fibers increases immediately with pressure resulting in pronounced apparent plasticization and reduction of the ideal CO 2 /N 2 selectivity. However, no evidence of plasticization was observed when a CO 2 /N 2 , 55/45% mixture was fed to the hollow‐fiber membranes. In all cases, CO 2 permeance decreased with pressure, while that of N 2 remained constant. Experimental results were validated by means of mathematical modeling. Membrane‐separation performance was overestimated when pressure‐independent permeabilities were used in the model, while pressure‐dependent permeabilities, due to the overall effect of plasticization and competition phenomena, explained excellently, the obtained stage‐cut and permeate purity.