Performances of poly (vinylpyrrolidone-co-vinyl acetate)-cellulose acetate blend membranes in the pervaporation of ethanol-ehyl tert-butyl ether mixtures - Simplified model for flux prediction

被引:18
作者
Nguyen, QT [1 ]
Clement, R [1 ]
Noezar, I [1 ]
Lochon, P [1 ]
机构
[1] Ecole Natl Super Ind Chim, LCPM, URA 494, F-54001 Nancy, France
关键词
blend membranes; solvent mixture sorption; pervaporation characteristics; copolymer;
D O I
10.1016/S1383-5866(98)00046-X
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
High performance pervaporation membranes for the selective removal of ethanol from ethyl t-butyl ether (ETBE) were prepared by blending cellulose acetate with poly (vinylpyrrolidone-co-vinyl acetate) in different proportions and studied in sorption and pervaporation of ethanol-ETBE mixtures of compositions ranging from 5 to 25 wt% ethanol. The membrane performances are improved when the copolymer content is higher due to strong flux enhancement. Both the ethanol and ETBE amounts sorbed by the membranes increase with the ethanol content in the mixture with which the membranes are in equilibrium, but that of ethanol is one order of magnitude higher than that of ETBE; this indicates an enhancement of ETBE sorption due to the interactions with ethanol sorbed by the membrane. We observed a similar behavior for the ethanol and ETBE fluxes. A simplified model with an ethanol flux increasing exponentially, and an ETBE flux increasing linearly with the ethanol content at the membrane upstream face, was developed and validated with the experimental data. (C) 1998 Elsevier Science B.V.
引用
收藏
页码:237 / 245
页数:9
相关论文
共 14 条
[1]   MODELING OF THE PERVAPORATION OF BINARY-MIXTURES THROUGH MODERATELY SWELLING, NON-REACTING MEMBRANES [J].
BRUN, JP ;
LARCHET, C ;
MELET, R ;
BULVESTRE, G .
JOURNAL OF MEMBRANE SCIENCE, 1985, 23 (03) :257-283
[2]  
DEPINHO M, 1990, J MEMBRANE SCI, V54, P134
[3]   PREDICTION OF FLUX AND SELECTIVITY IN PERVAPORATION THROUGH A MEMBRANE [J].
DOONG, SJ ;
HO, WS ;
MASTONDREA, RP .
JOURNAL OF MEMBRANE SCIENCE, 1995, 107 (1-2) :129-146
[4]   THEORETICAL INTERPRETATION OF EFFECT OF MIXTURE COMPOSITION ON SEPARATION OF LIQUIDS IN POLYMERS [J].
FELS, M ;
HUANG, RYM .
JOURNAL OF MACROMOLECULAR SCIENCE-PHYSICS, 1971, B 5 (01) :89-&
[5]   A GENERALIZED SOLUTION DIFFUSION-MODEL OF THE PERVAPORATION PROCESS THROUGH COMPOSITE MEMBRANES .1. PREDICTION OF MIXTURE SOLUBILITIES IN THE DENSE ACTIVE LAYER USING THE UNIQUAC MODEL [J].
HEINTZ, A ;
STEPHAN, W .
JOURNAL OF MEMBRANE SCIENCE, 1994, 89 (1-2) :143-151
[6]   MODELING OF MULTICOMPONENT PERVAPORATION FOR REMOVAL OF VOLATILE ORGANIC-COMPOUNDS FROM WATER [J].
JI, WC ;
SIKDAR, SK ;
HWANG, ST .
JOURNAL OF MEMBRANE SCIENCE, 1994, 93 (01) :1-19
[7]   LIQUID PERMEATION THROUGH PLASTIC FILMS [J].
LONG, RB .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1965, 4 (04) :445-&
[8]   ON THE MECHANISM OF SEPARATION OF ETHANOL WATER MIXTURES BY PERVAPORATION .1. CALCULATIONS OF CONCENTRATION PROFILES [J].
MULDER, MHV ;
SMOLDERS, CA .
JOURNAL OF MEMBRANE SCIENCE, 1984, 17 (03) :289-307
[9]   INFLUENCE OF DOWNSTREAM PRESSURE ON THE PERVAPORATION OF WATER - TETRAHYDROFURAN MIXTURES THROUGH A REGENERATED CELLULOSE MEMBRANE (CUPROPHAN) [J].
NEEL, J ;
NGUYEN, QT ;
CLEMENT, R ;
LIN, DJ .
JOURNAL OF MEMBRANE SCIENCE, 1986, 27 (02) :217-232
[10]   DIFFERENTIAL PERMEATION .1. A METHOD FOR THE STUDY OF SOLVENT DIFFUSION THROUGH MEMBRANES [J].
NGUYEN, QT ;
GREF, R ;
CLEMENT, R ;
LENDA, H .
COLLOID AND POLYMER SCIENCE, 1993, 271 (12) :1134-1142