Equilibrium and kinetic analysis of CO2-N2 adsorption separation by concentration pulse chromatography

被引:29
作者
Li, Peiyuan [1 ]
Tezel, F. Handan [1 ]
机构
[1] Univ Ottawa, Fac Engn, Dept Chem Engn, Ottawa, ON K1N 6N5, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
adsorption of carbon dioxide; adsorption of nitrogen; flue gas separation; silicalite; NaY; 13X; Henry's Law constant;
D O I
10.1016/j.jcis.2007.04.015
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
CO2 and N-2 adsorption kinetics and equilibrium behaviours have been studied with silicalite, NaY and 13X by using concentration pulse chromatography for the separation of these gases in the present study. Adsorption Henry's Law constants, the heat of adsorption values, micropore diffusion coefficients and corresponding activation energies are determined experimentally and the three different mass transfer mechanisms are discussed. From the equilibrium data, the corresponding separation factors are obtained for the adsorption separation processes. The heat of adsorption values as well as the Henry's Law adsorption equilibrium constants Of CO2 are much higher than those of N2 for all the adsorbents studied. 13X, NaY and silicalite all have good separation factors for CO2/N-2 system based on equilibrium processes. The order of the equilibrium separation factors is 13X (Ceca) > 13X (Zeochem) > NaY (UOP) >> silicalite (UOP). Equilibrium selectivity favours CO2 over N2. Micropore diffusion resistance is the definite dominant mass transfer mechanism for CO2 with silicalite and NaY. (c) 2007 Elsevier Inc. All rights reserved.
引用
收藏
页码:12 / 17
页数:6
相关论文
共 30 条
[1]  
BIRD RB, 1960, DIFFUSIVITY MECHANIS, P495
[2]  
CHAPMAN S, 1951, MATH THEORY NONUNIFO, pCH10
[3]   ADSORPTION OF METHANE, ETHANE, ETHYLENE, AND CARBON-DIOXIDE ON HIGH-SILICA PENTASIL ZEOLITES AND ZEOLITE-LIKE MATERIALS USING GAS-CHROMATOGRAPHY PULSE TECHNIQUE [J].
CHOUDHARY, VR ;
MAYADEVI, S .
SEPARATION SCIENCE AND TECHNOLOGY, 1993, 28 (13-14) :2197-2209
[4]   The Petlyuk PSA process for the separation of ternary gas mixtures:: exemplification by separating a mixture of CO2-CH4N2 [J].
Dong, F ;
Lou, HM ;
Kodama, A ;
Goto, M ;
Hirose, T .
SEPARATION AND PURIFICATION TECHNOLOGY, 1999, 16 (02) :159-166
[5]   High pressure adsorption data of methane, nitrogen, carbon dioxide and their binary and ternary mixtures on activated carbon [J].
Dreisbach, F ;
Staudt, R ;
Keller, JU .
ADSORPTION-JOURNAL OF THE INTERNATIONAL ADSORPTION SOCIETY, 1999, 5 (03) :215-227
[6]   Calorimetric heats of adsorption and adsorption isotherms .1. O-2, N-2, Ar, CO2, CH4, C2H6 and SF6 on silicalite [J].
Dunne, JA ;
Mariwals, R ;
Rao, M ;
Sircar, S ;
Gorte, RJ ;
Myers, AL .
LANGMUIR, 1996, 12 (24) :5888-5895
[7]   GAS-ADSORPTION ON SILICALITE [J].
GOLDEN, TC ;
SIRCAR, S .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 1994, 162 (01) :182-188
[8]   GLOBAL CLIMATE CHANGES AS FORECAST BY GODDARD INSTITUTE FOR SPACE STUDIES 3-DIMENSIONAL MODEL [J].
HANSEN, J ;
FUNG, I ;
LACIS, A ;
RIND, D ;
LEBEDEFF, S ;
RUEDY, R ;
RUSSELL, G ;
STONE, P .
JOURNAL OF GEOPHYSICAL RESEARCH-ATMOSPHERES, 1988, 93 (D8) :9341-9364
[9]   Use of concentration pulse chromatography for determining binary isotherms:: Comparison with statically determined binary isotherms [J].
Harlick, PJE ;
Tezel, FH .
ADSORPTION-JOURNAL OF THE INTERNATIONAL ADSORPTION SOCIETY, 2003, 9 (03) :275-286
[10]   Adsorption of carbon dioxide, methane and nitrogen:: pure and binary mixture adsorption for ZSM-5 with SiO2/Al2O3 ratio of 280 [J].
Harlick, PJE ;
Tezel, FH .
SEPARATION AND PURIFICATION TECHNOLOGY, 2003, 33 (02) :199-210