MODELING OF MULTICOMPONENT COUNTERCURRENT GAS PERMEATORS

被引:32
作者
KOVVALI, AS [1 ]
VEMURY, S [1 ]
ADMASSU, W [1 ]
机构
[1] UNIV IDAHO,DEPT CHEM ENGN,MOSCOW,ID 83843
关键词
D O I
10.1021/ie00028a016
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Modeling of gas permeation in hollow-fiber or spiral wound modules necessitates considering the effect of permeate pressure variation along the module length which could have a significant effect on the prediction of the exit compositions and membrane area requirements depending on the membrane characteristics and module geometry. The transport equations governing the permeator performance are a set of coupled nonlinear differential equations. The complexity of the solution procedure for these equations increases with the number of components in the mixture and consideration of pressure variation. Thus, there is a need for simplified solution methodologies which could reduce the computational efforts. This paper presents a solution methodology to solve the multicomponent gas permeator transport equations in a countercurrent flow pattern, taking the permeate pressure variation into consideration. The present method yields analytical expressions for flow rates, permeate pressure, membrane area, and compositions along the length of the permeator.
引用
收藏
页码:896 / 903
页数:8
相关论文
共 30 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]   ASYMPTOTIC ANALYSIS OF GAS SEPARATION BY A MEMBRANE MODULE [J].
BASARAN, OA ;
AUVIL, SR .
AICHE JOURNAL, 1988, 34 (10) :1726-1731
[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]   SEPARATION OF GASES BY PLASTIC MEMBRANES - PERMEATION RATES AND EXTENT OF SEPARATION [J].
BRUBAKER, DW ;
KAMMERMEYER, K .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1954, 46 (04) :733-739
[7]   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
[8]  
Ho W.S.W., 1992, MEMBRANE HDB
[9]  
KESTING R.E., 1985, SYNTHETIC POLYM MEMB
[10]   MODELS AND ANALYSES OF MEMBRANE GAS PERMEATORS [J].
KOVVALI, AS ;
VEMURY, S ;
KROVVIDI, KR ;
KHAN, AA .
JOURNAL OF MEMBRANE SCIENCE, 1992, 73 (01) :1-23