Poly(vinylalcohol)/poly(ethyleneglycol)/poly(ethyleneimine) blend membranes - structure and CO2 facilitated transport

被引:56
作者
Ben Hamouda, Sofiane [1 ]
NguyenB, Quang Trong [2 ]
Langevin, Dominique [2 ]
Roudesli, Sadok [3 ]
机构
[1] CERTE, Lab Traitement Eaux Nat, Soliman 8020, Tunisia
[2] Univ Rouen, CNRS, FRE 3103, Lab Polymeres Biopolymeres Surfaces, F-76821 Mont St Aignan, France
[3] Univ Monastir, Lab Polymeres, Monastir 5019, Tunisia
关键词
Blend membranes; Poly(ethyleneimine); CO2/N-2; separation; Ideal selectivity; Facilitated transport; POLY(VINYL ALCOHOL); GAS SEPARATION; PERMEATION;
D O I
10.1016/j.crci.2009.10.009
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Poly(vinylalcohol) (PVA)/poly(ethyleneimine) (PEI)/poly(ethyleneglycol) (PEG) blend membranes were prepared by solution casting followed by solvent evaporation. The effects of the blend polymer composition on the membrane structure and CO2/N-2 permeation characteristics were investigated. IR spectroscopy evidenced strong hydrogen bonding interactions between amorphous PVA and PEI, and weaker interactions between PVA and PEG. DSC studies showed that PVA crystallization was partially inhibited by the interactions between amorphous PVA and PEI blend, in which PEG separated into nodules. The CO2 permeability decreased with an increase in CO2 partial pressure in feed gas, while the N-2 permeability remained constant. This result indicated that only CO2 was transported by the facilitated transport mechanism. The CO2 and N-2 permeabilities increased monotonically with the PEI content in the blend membranes, whereas the ideal selectivity of CO2 to N-2 transport showed a maximum. When CO2 is humidified, its permeability through the blend membranes is much higher than that of dry CO2, but the change in permeability due to the presence of humidity is reversible. (C) 2009 Academie des sciences. Published by Elsevier Masson SAS. All rights reserved.
引用
收藏
页码:372 / 379
页数:8
相关论文
共 28 条
[1]   Future directions of membrane gas separation technology [J].
Baker, RW .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (06) :1393-1411
[2]  
Bondar VI, 2000, J POLYM SCI POL PHYS, V38, P2051, DOI 10.1002/1099-0488(20000801)38:15<2051::AID-POLB100>3.0.CO
[3]  
2-D
[4]   Gas transport property of polyallylamine-poly(vinyl alcohol)/polysulfone composite membranes [J].
Cai, Yan ;
Wang, Zhi ;
Yi, Chunhai ;
Bai, Yunhua ;
Wang, Jixiao ;
Wang, Shichang .
JOURNAL OF MEMBRANE SCIENCE, 2008, 310 (1-2) :184-196
[5]   Membranes comprising of alkanolamines incorporated into poly(vinyl alcohol) matrix for CO2/N2 separation [J].
Francisco, Gil J. ;
Chakma, Amit ;
Feng, Xianshe .
JOURNAL OF MEMBRANE SCIENCE, 2007, 303 (1-2) :54-63
[6]   GAS PERMEABILITIES AND PERMSELECTIVITIES OF AMORPHOUS SEGMENTED 6F POLY(ARYLENE THIOETHER IMIDE)S AND THE CORRESPONDING POLY(ARYLENE SULFONE IMIDE)S [J].
GLATZ, FP ;
MULHAUPT, R ;
SCHULTZE, JD ;
SPRINGER, J .
JOURNAL OF MEMBRANE SCIENCE, 1994, 90 (1-2) :151-159
[7]   TRANSPORT-PROPERTIES OF POLY(VINYL ALCOHOL) MEMBRANES OF DIFFERENT DEGREES OF CRYSTALLINITY .1. PERVAPORATION RESULTS [J].
GREF, R ;
NGUYEN, QT ;
SCHAETZEL, P ;
NEEL, J .
JOURNAL OF APPLIED POLYMER SCIENCE, 1993, 49 (02) :209-218
[8]  
Jegal J, 1999, J APPL POLYM SCI, V72, P1755, DOI 10.1002/(SICI)1097-4628(19990624)72:13<1755::AID-APP11>3.0.CO
[9]  
2-R
[10]   Residual solvent effect on the permeation properties of fluorinated polyimide films [J].
Joly, C ;
Le Cerf, D ;
Chappey, C ;
Langevin, D ;
Muller, G .
SEPARATION AND PURIFICATION TECHNOLOGY, 1999, 16 (01) :47-54