Multicomponent sorption of hexane isomers in zeolite BETA

被引:35
作者
Barcia, Patrick S.
Silva, Jose A. C.
Rodrigues, Alirio E.
机构
[1] Univ Porto, Fac Ingn, Dept Engn Quim, Lab Separat & React Engn, P-4200465 Oporto, Portugal
[2] Inst Politecn Braganca, Escola Super Tecnol & Gestao, P-5301857 Braganca, Portugal
关键词
zeolite BETA; hexane isomers separation; multicomponent adsorption; breakthrough curves; dynamic adsorption model;
D O I
10.1002/aic.11233
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Breakthrough curves of single, binary, ternary, and quaternary mixtures of hexane (C-6) isomers n-hexane (nHEX), 3-methylpentane (3MP), 2,3-dimethylbutane (23DMB), and 2,2-dimethylbutane (22DMB) were performed in commercial pellets of zeolite BETA (BEA structure), covering the temperature range between 423 and 523 K and partial pressures up to 30 kPa. From these data, single and multicomponent adsorption equilibrium isotherms were collected. A tri-site Langmuir model (TSL) was developed to interpret the equilibrium data based on considerations about zeolite structure, and a dynamic adsorption model was tested predicting with a good accuracy the behavior of multicomponent fixed-bed experiments. At the partial pressures studied, the sorption hierarchy in the zeolite BETA is nHEX >>> 3MP > 23DMB >> 22DMB. BEA structure demonstrates a significant selectivity between C-6 isomers, especially at low coverage, giving a good perspective regarding their separation by adsorption processes. (c) 2007 American Institute of Chemical Engineers.
引用
收藏
页码:1970 / 1981
页数:12
相关论文
共 13 条
[1]   Separation by fixed-bed adsorption of hexane isomers in zeolite BETA pellets [J].
Barcia, Patrick. S. ;
Silva, Jose A. C. ;
Rodrigues, Alirio E. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (12) :4316-4328
[2]   Adsorption equilibrium and kinetics of branched hexane isomers in pellets of BETA zeolite [J].
Bárcia, PS ;
Silva, JAC ;
Rodrigues, AE .
MICROPOROUS AND MESOPOROUS MATERIALS, 2005, 79 (1-3) :145-163
[3]   A general package for the simulation of cyclic adsorption processes [J].
Da Silva, FA ;
Silva, JA ;
Rodrigues, AE .
ADSORPTION-JOURNAL OF THE INTERNATIONAL ADSORPTION SOCIETY, 1999, 5 (03) :229-244
[4]  
DAVIS ME, 1996, SYNTHESIS POROUS MAT
[5]   Separation of branched hexane isomers using zeolite molecular sieves [J].
Huddersman, K ;
Klimczyk, M .
AICHE JOURNAL, 1996, 42 (02) :405-408
[6]   Separation of mono- and dibranched hydrocarbons on silicalite [J].
Jolimaitre, E ;
Ragil, K ;
Tayakout-Fayolle, M ;
Jallut, C .
AICHE JOURNAL, 2002, 48 (09) :1927-1937
[7]   Influence of isotherm inflection on diffusion in silicalite [J].
Krishna, R ;
Vlugt, TJH ;
Smit, B .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (12) :1751-1757
[8]   Modelling issues in zeolite based separation processes [J].
Krishna, R ;
Baur, R .
SEPARATION AND PURIFICATION TECHNOLOGY, 2003, 33 (03) :213-254
[9]   HEAT AND MASS-TRANSFER IN PACKED-BEDS .3. AXIAL MASS DISPERSION [J].
LANGER, G ;
ROETHE, A ;
ROETHE, KP ;
GELBIN, D .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1978, 21 (06) :751-759
[10]   Separation of alkane isomers by exploiting entropy effects during adsorption on silicalite-1: A configurational-bias Monte Carlo simulation study [J].
Schenk, M ;
Vidal, SL ;
Vlugt, TJH ;
Smit, B ;
Krishna, R .
LANGMUIR, 2001, 17 (05) :1558-1570