IPA purification for lens cleaning by vapor permeation using zeolite membrane

被引:40
作者
Kondo, M
Yamamura, T
Yukitake, T
Matsuo, Y
Kita, H
Okamoto, K
机构
[1] Tsukuba Ctr Inc, Bio Nanotec Res Inc, Tsukuba, Ibaraki 3050047, Japan
[2] Mitsui Engn & Shipbldg Co Ltd, Dept Ind Machinery Design, Okayama 7068651, Japan
[3] Yamaguchi Univ, Dept Adv Mat Sci & Engn, Ube, Yamaguchi 7558611, Japan
关键词
vapor permeation; zeolite NaA membrane; double tube-type module; dehydration; isopropanol;
D O I
10.1016/S1383-5866(03)00033-9
中图分类号
TQ [化学工业];
学科分类号
0817 [化学工程与技术];
摘要
Vapor permeation (VP) properties of commercial NaA-type zeolite membranes were examined using the alcohol/ water systems, before equipments to purify isopropanol (IPA) from lens cleaning process were designed. The membranes displayed excellent water-permselective performance for water/organic solutions in the VP. With an increase in feed temperature, both the permeation flux Q and the separation factor a increased, and the membrane performance was the same for pervaporation as for VP over 0.7 relative vapor pressure p/p(s). In VP of alcohol mixtures with 5 wt.% water over p/ps = 0.7 at 120 degreesC, Q values were 2.64, 4.3 and 5.6 kg m(-2) h(-1) and a value were 4000, 5600 and 6000 for the water/methanol (MeOH), water/ethanol (EtOH) and water/IPA solutions, respectively. The repeated experiment of IPA purification by VP with a zeolite NaA membrane was carried out in waste IPA liquid. The substances (acids, particles, etc.) in the waste IPA hardly influenced membrane performance in the VP. The IPA purification plant with approximately 0.72 m(2) membrane areas was composed of 24 double tube-type modules. This plant which can purify 101 h(-1) of IPA at less than 0.5 wt.% water from 88.6 wt.% IPA at 120 C has been put into lens cleaning operation. (C) 2003 Published by Elsevier Science B.V.
引用
收藏
页码:191 / 198
页数:8
相关论文
共 15 条
[1]
[Anonymous], [No title captured], Patent No. 5554286
[2]
Athayde AL, 1997, CHEMTECH, V27, P34
[3]
FLEMING HL, 1992, CHEM ENG PROG JUL, P46
[4]
Huang R. Y., 1991, Pervaporation Membrane Separation Processes
[5]
METHODS TO IMPROVE FLUX DURING ALCOHOL WATER AZEOTROPE SEPARATION BY VAPOR PERMEATION [J].
JANSEN, AE ;
VERSTEEG, WF ;
VANENGELENBURG, B ;
HANEMAAIJER, JH ;
TERMEULEN, BP .
JOURNAL OF MEMBRANE SCIENCE, 1992, 68 (03) :229-239
[6]
SYNTHESIS OF A ZEOLITE NAA MEMBRANE FOR PERVAPORATION OF WATER-ORGANIC LIQUID-MIXTURES [J].
KITA, H ;
HORII, K ;
OHTOSHI, Y ;
TANAKA, K ;
OKAMOTO, KI .
JOURNAL OF MATERIALS SCIENCE LETTERS, 1995, 14 (03) :206-208
[7]
KITA H, 1995, P 7 INT C PERV PROC, P364
[8]
Kita Hidetoshi, 1998, Membrane, V23, P62
[9]
Kita Hidetoshi, 1995, Membrane, V20, P169
[10]
Tubular-type pervaporation module with zeolite NaA membrane [J].
Kondo, M ;
Komori, M ;
Kita, H ;
Okamoto, K .
JOURNAL OF MEMBRANE SCIENCE, 1997, 133 (01) :133-141