HOLLOW FIBER AIR DRYING

被引:104
作者
WANG, KL
MCCRAY, SH
NEWBOLD, DD
CUSSLER, EL
机构
[1] UNIV MINNESOTA,DEPT CHEM ENGN & MAT SCI,421 WASHINGTON AVE SE,MINNEAPOLIS,MN 55455
[2] BEND RES INC,BEND,OR 97701
基金
美国国家科学基金会;
关键词
HOLLOW FIBER MODULES; AIR DRYING; FIBER MEMBRANES; GAS SEPARATIONS; WATER SORPTION AND DIFFUSION;
D O I
10.1016/0376-7388(92)85051-J
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Compressed air can easily be dried with hollow fiber modules made with water permeable membranes. The selectivity of these membranes for water over air is high, over 4000: 1; the water permeability per membrane thickness is also high, over 5 cm/sec (6 X 10(7) barrers per cm). As a result, the mass transfer is influenced not only by the membrane resistance, but also by the resistances in the feed and the permeate streams in the module. This mass transfer can often be enhanced by recycling some of the retentate as a sweep stream on the permeate side. These mass transfer resistances and the sweep stream interact in subtle ways which can be quantitatively predicted using correlations and models in the literature. For example, both experiments and predictions show that under some conditions, the module with the smallest membrane area for a given task may have a less selective membrane.
引用
收藏
页码:231 / 244
页数:14
相关论文
共 23 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]  
BABCOCK WC, 1989, Patent No. 4781733
[3]   COUNTERCURRENT AND CO-CURRENT GAS SEPARATION [J].
BLAISDEL.CT ;
KAMMERME.K .
CHEMICAL ENGINEERING SCIENCE, 1973, 28 (06) :1249-1255
[4]   SERIES SOLUTIONS FOR A GAS PERMEATOR WITH COUNTERCURRENT AND COCURRENT FLOW [J].
BOUCIF, N ;
MAJUMDAR, S ;
SIRKAR, KK .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1984, 23 (04) :470-480
[5]   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
[6]   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
[7]   INTERACTIONS OF POLYETHER POLYURETHANES WITH WATER-VAPOR AND WATER METHANE SEPARATION SELECTIVITY [J].
DILANDRO, L ;
PEGORARO, M ;
BORDOGNA, L .
JOURNAL OF MEMBRANE SCIENCE, 1991, 64 (03) :229-236
[8]   HEAT TRANSFER AND PRESSURE DROP IN HEAT EXCHANGERS [J].
DONOHUE, DA .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1949, 41 (11) :2499-2511
[9]   EFFECT OF DIFFUSION ON THE MODEL OF A CAPILLARY GAS PERMEATOR [J].
KAO, YK ;
CHEN, SH ;
HWANG, ST .
JOURNAL OF MEMBRANE SCIENCE, 1987, 32 (2-3) :139-157
[10]  
Leveque M. A., 1928, ANN MINES, V13, p[201, 305, 381]