Review and comparisons of D/R models of equilibrium adsorption of binary mixtures of organic vapors on activated carbons

被引:33
作者
Wood, GO [1 ]
机构
[1] Los Alamos Natl Lab, Los Alamos, NM 87545 USA
关键词
activated carbons; adsorption; modelling; phase equilibria;
D O I
10.1016/S0008-6223(01)00090-2
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Published models and options for predicting equilibrium adsorption capacities of multicomponent mixtures using single component Dubinin/Radushkevich isotherm equations and parameters were reviewed. They were then tested for abilities to predict total and component capacities reported for 93 binary adsorbed mixtures. The best model for calculating molar distributions was the Ideal Adsorbed Solution Theory (IAST). which balances spreading pressures. Combined with the IAST, total and component capacities were best calculated using either the Lewis or original Bering equation with the Ideal Adsorbed Solution (Raoult's Law) assumption. (C) 2002 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:231 / 239
页数:9
相关论文
共 24 条
[1]  
Bering B.P., 1971, IAN SSSR KH, V12, P2641
[2]  
BERING BP, 1965, IAN SSSR KH, V5, P769
[3]   A SIMPLE POTENTIAL-THEORY MODEL FOR PREDICTING MIXED-GAS ADSORPTION [J].
DOONG, SJ ;
YANG, RT .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1988, 27 (04) :630-635
[4]  
DOONG SJ, 1987, AICHE S SER, V83, P87
[5]  
DUBININ MM, 1947, ZH FIZ KHIM+, V21, P1351
[6]  
DUBININ MM, 1971, B ACAD SCI USSR CH+, P5
[7]   ADSORPTION OF BINARY HYDROCARBON GAS MIXTURES ON ACTIVATED CARBON [J].
GRANT, RJ ;
MANES, M .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1966, 5 (04) :490-&
[8]  
HOPPE VH, 1982, Z PHYS CHEM-LEIPZIG, V6, P1169
[9]   PREDICTION OF ACTIVATED CARBON PERFORMANCE FOR BINARY VAPOR MIXTURES [J].
JONAS, LA ;
SANSONE, EB ;
FARRIS, TS .
AMERICAN INDUSTRIAL HYGIENE ASSOCIATION JOURNAL, 1983, 44 (10) :716-719
[10]  
KISAROV VM, 1969, RUSS J PHYS CH USSR, V43, P580