Fabrication of lab-scale hollow fiber membrane modules with high packing density

被引:79
作者
Li, DF
Wang, R
Chung, TS
机构
[1] Natl Univ Singapore, Dept Chem & Environm Engn, Singapore 119260, Singapore
[2] Nanyang Technol Univ, Inst Biomol Sci & Engn, Innovat Ctr, Singapore 637723, Singapore
关键词
module fabrication; hollow fiber membrane; gas separation;
D O I
10.1016/j.seppur.2003.12.019
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Module fabrication has always been treated as proprietary know-how. Systematic teaching and scientific study on module design and fabrication in academic journals are lacking. Small membrane modules consisting of 10-20 pieces of hollow fibers made simply for performance evaluation in laboratories normally cannot provide sufficient information for industrial applications because of the negligence of the effects of temperature change. different flow patterns and fiber variability. Thus a simple approach to fabricate lab-scale hollow fiber membrane modules with high packing density of 45-60%, which is around the level of commercial modules, by using commercially available standard parts was demonstrated. The detailed procedure of fabrication was described step by step. Verification tests show that the resultant lab-scale hollow fiber modules have high packing density of 49.3% and can withstand high pressure up to 500 psi with good separation properties. This know-how-based technique may provide a close linkage in terms of performance prediction, system modeling, and scaling-up between the lab-scale research and industrial-scale membrane systems for gas separation. (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:15 / 30
页数:16
相关论文
共 68 条
[1]   ANALYSIS OF GAS SEPARATION BY PERMEATION IN HOLLOW FIBERS [J].
ANTONSON, CR ;
GARDNER, RJ ;
KING, CF ;
KO, DY .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1977, 16 (04) :463-469
[2]   Future directions of membrane gas separation technology [J].
Baker, RW .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (06) :1393-1411
[3]   Effect of random fiber packing on the performance of shell-fed hollow-fiber gas separation modules [J].
Bao, LH ;
Lipscomb, GG .
DESALINATION, 2002, 146 (1-3) :243-248
[4]  
BIKSON B, 1989, Patent No. 4881955
[5]  
BOGART MC, 1982, Patent No. 4308654
[6]   HOLLOW FIBER GAS PERMEATOR WITH COUNTERCURRENT OR COCURRENT FLOW - SERIES SOLUTIONS [J].
BOUCIF, N ;
SENGUPTA, A ;
SIRKAR, KK .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1986, 25 (02) :217-228
[7]   Experimental study of the Joule-Thomson effect in carbon dioxide [J].
Burnett, ES .
PHYSICAL REVIEW, 1923, 22 (06) :0590-0616
[8]   Modeling and optimizing submerged hollow fiber membrane modules [J].
Chang, S ;
Fane, AG ;
Vigneswaran, S .
AICHE JOURNAL, 2002, 48 (10) :2203-2212
[9]  
CHEN H, 1995, CHINESE J CHEM ENG, V3, P72
[10]   SIMULATION OF A HOLLOW-FIBER GAS SEPARATOR - THE EFFECTS OF PROCESS AND DESIGN VARIABLES [J].
CHERN, RT ;
KOROS, WJ ;
FEDKIW, PS .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1985, 24 (04) :1015-1022