Effect of polymer extrusion temperature on poly(vinylidene fluoride) hollow fiber membranes: Properties and performance used as gas-liquid membrane contactor for CO2 absorption

被引:47
作者
Ghasem, Nayef [1 ]
Al-Marzouqi, Mohamed [1 ]
Rahim, Nihmiya Abdul [1 ]
机构
[1] UAE Univ, Dept Chem & Petr Engn, Alain City, U Arab Emirates
关键词
Poly(vinylidene fluoride); PVDF; Hollow fiber membranes; Extrusion temperature; Membrane absorption; CO2; absorption; TIPS method; INDUCED PHASE-SEPARATION; MASS-TRANSFER; CAPTURE; MORPHOLOGY; REMOVAL; SO2;
D O I
10.1016/j.seppur.2012.07.021
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
In this study, poly(vinylidene fluoride) (PVDF) hollow fiber membranes were fabricated via thermally induced phase separation (TIPS) method using 28% PVDF polymer and 72% triacetin solvent. The dope solutions were prepared at four different extrusion temperatures (140 degrees C, 150 degrees C, 160 degrees C and 170 degrees C). The fabricated membranes were characterized using scanning electron microscopy (SEM), mercury porosimeter to measure membrane average pore diameter, gas permeation test was employed to measure membrane effective surface porosity. The separation of carbon dioxide (CO2) from methane (CH4) by using a gas-liquid membrane contactor was studied in order to confirm the potential of the process using the fabricated hollow fiber membranes. The experiments were performed in a membrane contactor constructed with the fabricated microporous PVDF hollow fibers. Aqueous sodium hydroxide (NaOH) solution was utilized as the liquid absorbent. The effect of the gas flow rate on the CO2 flux was investigated. It was found that the PVDF membranes exhibited increased pore size, water contact angle, membrane strength, membrane porosity, effective surface porosity with preparation temperature. Countercurrent flow mode was employed: the CO2 flux increased with membrane extrusion temperatures. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:91 / 103
页数:13
相关论文
共 49 条
[1]
Modeling of chemical absorption of CO2 in membrane contactors [J].
Al-Marzouqi, M. ;
El-Naas, M. ;
Marzouk, S. ;
Abdullatiff, N. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2008, 62 (03) :499-506
[2]
Mass transfer study and modeling of gas-liquid membrane contacting process by multistage cascade model for CO2 absorption [J].
Atchariyawut, Supakorn ;
Jiraratananon, Ratana ;
Wang, Rong .
SEPARATION AND PURIFICATION TECHNOLOGY, 2008, 63 (01) :15-22
[3]
Separation of CO2 from CH4 by using gas-liquid membrane contacting process [J].
Atchariyawut, Supakorn ;
Jiraratananon, Ratana ;
Wang, Rong .
JOURNAL OF MEMBRANE SCIENCE, 2007, 304 (1-2) :163-172
[4]
Effect of membrane structure on mass-transfer in the membrane gas-liquid contacting process using microporous PVDF hollow fibers [J].
Atchariyawut, Supakorn ;
Feng, Chunsheng ;
Wang, Rong ;
Jiraratananon, Ratana ;
Liang, D. T. .
JOURNAL OF MEMBRANE SCIENCE, 2006, 285 (1-2) :272-281
[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]
Bird R B., 2002, Transportphenomena
[7]
Chabot S, 1997, J APPL POLYM SCI, V65, P1263, DOI 10.1002/(SICI)1097-4628(19970815)65:7<1263::AID-APP4>3.0.CO
[8]
2-G
[9]
Cussler E.L., 2009, CAMBRIDGE SERIES CHE, Vthird
[10]
Membrane-solvent selection for CO2 removal using membrane gas-liquid contactors [J].
Dindore, VY ;
Brilman, DWF ;
Geuzebroek, FH ;
Versteeg, GF .
SEPARATION AND PURIFICATION TECHNOLOGY, 2004, 40 (02) :133-145