INCREASED SEPARATION BY VARIABLE-TEMPERATURE STEPWISE DESORPTION IN MULTICOMPONENT ADSORPTION PROCESSES

被引:23
作者
KULVARANON, S
FINDLEY, ME
LIAPIS, AI
机构
[1] UNIV MISSOURI,DEPT CHEM ENGN,ROLLA,MO 65401
[2] UNIV MISSOURI,INST BIOCHEM PROC,ROLLA,MO 65401
关键词
D O I
10.1021/ie00097a016
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
When more components than desired are adsorbed, adsorption-desorption separation processes may not be satisfactory. However, in the cases of ethanol and water adsorption on activated carbon, propane and propylene adsorption on molecular sieves, and hydrogen sulfide, carbon dioxide, and propane adsorption on molecular sieves, it has been found that a variable-temperature stepwise desorption (VTSD) procedure following the adsorption stage can significantly increase the degree of separation achieved compared to a complete desorption of all adsorbed components. Studies indicate that these increased separations are in part due to nonequilibrium effects. An estimation of economic factors in separating low concentration propylene in propane indicates VTSD is favorable compared to distillation, because of lower energy costs. It appears that the VTSD method could be useful in bulk separations of mutlicomponent mixtures. © 1990, American Chemical Society. All rights reserved.
引用
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页码:106 / 115
页数:10
相关论文
共 10 条
[1]  
GUTHRIE KM, 1969, CHEM ENG-NEW YORK, V76, P114
[2]   A NONEQUILIBRIUM MODEL FOR FIXED-BED MULTICOMPONENT ADIABATIC ADSORPTION [J].
HARWELL, JH ;
LIAPIS, AI ;
LITCHFIELD, R ;
HANSON, DT .
CHEMICAL ENGINEERING SCIENCE, 1980, 35 (11) :2287-2296
[3]  
KEMBALL C, 1948, T FARADAY SOC, V44, P952
[4]  
KULVARANON S, 1988, THESIS U MISSOURI RO
[5]  
LIAPIS AI, 1989, Patent No. 4874524
[6]  
RUTHVEN DM, 1984, PRINCIPLES ADSORPTIO, pCH1
[7]  
VALENZUELA PP, 1989, ADSORPTION EQUILIBRI
[8]  
WALSH PK, 1983, BIOTECHNOL BIOENG S, V13, P629
[9]  
YANG RT, 1987, GAS SEPARATION ADSOR, pCH3
[10]  
1985, ASPEN PLUS INTRO MAN