Porous PES and PEI hollow fiber membranes in a gas-liquid contacting process-A comparative study

被引:50
作者
Bakeri, Gh [1 ]
Ismail, A. F. [2 ]
DashtArzhandi, M. Rezaei [2 ]
Matsuura, T. [2 ,3 ]
机构
[1] Babol Noshirvani Univ Technol, Fac Chem Engn, Adv Membrance & Biotechnol Res Ctr, Babol Sar, Iran
[2] Univ Teknol Malaysia, Adv Membrance Technol Res Ctr AMTEC, Skudai 81310, Johor, Malaysia
[3] Univ Ottawa, Ind Membrane Res Inst, Dept Chem & Biol Engn, Ottawa, ON K1N 6N5, Canada
关键词
Polyetherimide; Polyethersulfone; Membrane contactor; CO2; absorption; PHASE-INVERSION; ULTRAFILTRATION MEMBRANES; POLY(ETHER IMIDE); MORPHOLOGY TRANSITION; POLYETHYLENE-GLYCOL; MASS-TRANSFER; FLAT SHEET; PERFORMANCE; SEPARATION; ADDITIVES;
D O I
10.1016/j.memsci.2014.09.037
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
Porous polyetherimide (PEI) and polyethersullone (PES) hollow fiber membranes were spun under the same spinning conditions and the fabricated membranes were characterized using various analytical methods. The membranes were then subjected to gas-liquid contactor experiments. While the PEI casing solution was thermodynamically less stable, the PES casting solution was less viscous which resulted in a more porous membrane structure. The mean pore size and effective surface porosity obtained by the gas permeation test showed superior properties of the PES membrane. Both PEI and PES membranes had sufficiently high LEPw values even though both polymers were known to be relatively hydrophilic, most likely clue to their small pore sizes. The absorption flux of the PES membrane was 4.4 x 10(-3) mol m(-2) s(-1) at the liquid flow velocity V-liquid of 1.8 m s(-1), which was 267% higher than that of the PEI membrane 1.2 x 10(-3) mol m(-2) s(-1)) clue to the larger pore size and smaller tortuosity of the PES membrane. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:57 / 64
页数:8
相关论文
共 38 条
[1]
Formation of hollow fiber membranes from poly(ether imide) at wet phase inversion using binary mixtures of solvents for the preparation of the dope [J].
Albrecht, W ;
Weigel, T ;
Schossig-Tiedemann, M ;
Kneifel, K ;
Peinemann, KN ;
Paul, D .
JOURNAL OF MEMBRANE SCIENCE, 2001, 192 (1-2) :217-230
[2]
Performance of Surface-Modified Poly(ether imide) Hollow-Fiber Membranes in a Membrane Gas-Liquid Contacting Process with Response Surface Methodology [J].
Bakeri, G. ;
Rana, D. ;
Ismail, A. F. ;
Matsuura, T. ;
Ghaee, A. .
JOURNAL OF APPLIED POLYMER SCIENCE, 2013, 128 (02) :1313-1325
[3]
Porous polyethersulfone hollow fiber membrane in gas-liquid contacting processes [J].
Bakeri, Gh ;
Ismail, A. F. ;
Rahimnejad, M. ;
Matsuura, T. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2014, 92 (07) :1381-1390
[4]
The effect of bore fluid type on the structure and performance of polyetherimide hollow fiber membrane in gas-liquid contacting processes [J].
Bakeri, Gh. ;
Ismail, A. F. ;
Rahimnejad, M. ;
Matsuura, T. ;
Rana, D. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2012, 98 :262-269
[5]
Effect of polymer concentration on the structure and performance of polyetherimide hollow fiber membranes [J].
Bakeri, Gh. ;
Ismail, A. F. ;
Shariaty-Niassar, M. ;
Matsuura, T. .
JOURNAL OF MEMBRANE SCIENCE, 2010, 363 (1-2) :103-111
[6]
Preparation of poly(vinylidene fluoride) hollow fiber membranes for microfiltration using modified TIPS process [J].
Cha, Bong Jun ;
Yang, Jung Mok .
JOURNAL OF MEMBRANE SCIENCE, 2007, 291 (1-2) :191-198
[7]
Drioli E., 2005, MEMBRANE SCI TECHNOL
[8]
Recent progresses in polymeric hollow fiber membrane preparation, characterization and applications [J].
Feng, C. Y. ;
Khulbe, K. C. ;
Matsuura, T. ;
Ismail, A. F. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2013, 111 :43-71
[9]
Effect of additives in the casting solution on the formation of PVDF membranes [J].
Fontananova, E ;
Jansen, JC ;
Cristiano, A ;
Curcio, E ;
Drioli, E .
DESALINATION, 2006, 192 (1-3) :190-197
[10]
Hollow fiber membrane contactors [J].
Gabelman, A ;
Hwang, ST .
JOURNAL OF MEMBRANE SCIENCE, 1999, 159 (1-2) :61-106