Pervaporation separation of ethylene glycol/water mixtures through surface crosslinked PVA membranes: Coupling effect and separation performance analysis

被引:99
作者
Guo, Ruili [1 ]
Hu, Changlai [1 ]
Li, Ben [1 ]
Jiang, Zhongyi [1 ]
机构
[1] Tianjin Univ, Key Lab Green Chem Technol, Sch Chem Engn & Technol, Tianjin 300072, Peoples R China
关键词
pervaporation; poly(vinyl alcohol); glutaraldehyde; ethylene glycol; dehydration;
D O I
10.1016/j.memsci.2006.11.055
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Dehydration of ethylene glycol (EG) aqueous solution by pervaporation was studied by surface crosslinked poly(vinyl alcohol) membrane using glutaraldehyde as crosslinking reagent. The membrane shows desirable thermal stability, mechanical stability and pervaporation performance (for 80 wt.% EG aqueous solution at 70 degrees C, the permeation flux and separation factor are 211 g m(-2) h(-1) and 933). The remarkable dependence of water and EG concentration in permeate side as well as their activity coefficients within the membrane on feed concentration indicate that a strong coupling effect exists between water and EG, which effectively inhibits the permeation of EG and thus considerably enhances the separation selectivity of membrane. With feed temperature increasing, the permeation flux increases but separation factor decreases significantly due to the difference of activation energies between water and EG. With feed flow rate increasing, both the permeation flux and separation factor increase correspondingly. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:191 / 198
页数:8
相关论文
共 33 条
[1]   Pervaporation separation of water-acetic acid mixtures using polymeric membranes [J].
Aminabhavi, TM ;
Toti, US .
DESIGNED MONOMERS AND POLYMERS, 2003, 6 (03) :211-236
[2]   APPLICATION OF UNIQUAC EQUATION TO CALCULATION OF MULTICOMPONENT PHASE-EQUILIBRIA .2. LIQUID-LIQUID EQUILIBRIA [J].
ANDERSON, TF ;
PRAUSNITZ, JM .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1978, 17 (04) :561-567
[3]   Sorption and permeation of binary water-alcohol systems through PVA membranes crosslinked with multifunctional crosslinking agents [J].
Burshe, MC ;
Sawant, SB ;
Joshi, JB ;
Pangarkar, VG .
SEPARATION AND PURIFICATION TECHNOLOGY, 1997, 12 (02) :145-156
[4]   Pervaporation separation of ethylene glycol/water mixtures using crosslinked PVA/PES composite membranes .2. The swelling equilibrium model of the dense active layer in ethylene glycol/water mixtures [J].
Chen, FR ;
Chen, HF .
JOURNAL OF MEMBRANE SCIENCE, 1996, 118 (02) :169-176
[5]   Pervaporation separation of isopropanol/water mixtures through crosslinked chitosan membranes [J].
Devi, DA ;
Smitha, B ;
Sridhar, S ;
Aminabhavi, TM .
JOURNAL OF MEMBRANE SCIENCE, 2005, 262 (1-2) :91-99
[6]   Temperature polarization in pervaporation [J].
Favre, E .
DESALINATION, 2003, 154 (02) :129-138
[7]   CONCENTRATION POLARIZATION IN PERVAPORATION SEPARATION PROCESSES [J].
FENG, XS ;
HUANG, RYM .
JOURNAL OF MEMBRANE SCIENCE, 1994, 92 (03) :201-208
[8]  
Flory PJ, 1953, PRINCIPLES POLYM CHE
[9]   Heat supply and reduction of polarization effects in pervaporation by two-phase feed [J].
Fontalvo, J. ;
Vorstman, M. A. G. ;
Wijers, J. G. ;
Keurentjes, J. T. F. .
JOURNAL OF MEMBRANE SCIENCE, 2006, 279 (1-2) :156-164
[10]   MASS-TRANSFER IN THE MEMBRANE CONCENTRATION POLARIZATION LAYER UNDER TURBULENT CROSS FLOW .1. CRITICAL LITERATURE-REVIEW AND ADAPTATION OF EXISTING SHERWOOD CORRELATIONS TO MEMBRANE OPERATIONS [J].
GEKAS, V ;
HALLSTROM, B .
JOURNAL OF MEMBRANE SCIENCE, 1987, 30 (02) :153-170