Modelling sorption and diffusion in activated carbon: a novel low pressure pulse-response technique

被引:13
作者
Linders, MJG
van den Broeke, LJP
Nijhuis, TA
Kapteijn, F
Moulijn, JA
机构
[1] TNO, Prins Maurits Lab, NL-2280 AA Rijswijk, Netherlands
[2] Tech Univ Eindhoven, Dept Chem Engn & Chem, NL-5600 MB Eindhoven, Netherlands
[3] Delft Univ Technol, Dept Chem Engn, Ind Catalysis Sect, NL-2628 BL Delft, Netherlands
关键词
activated carbon; adsorption; modeling; adsorption properties; diffusion;
D O I
10.1016/S0008-6223(01)00030-6
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
A novel low pressure pulse-response technique, referred to as Multitrack, was applied for the simultaneous determination of the adsorption and diffusion parameters of gases in porous materials in a packed bed. Measurements were performed on two different carbons, Kureha and Sorbonorit B3, in the temperature range between 473 and 700 K. The modelling procedure of the pulse responses consisted of two parts. The transport parameters through the packed bed were determined from the pulse responses of non-adsorbing argon. Adsorption and diffusion parameters were determined for the adsorbing gases n-butane and hexafluoropropylene. As a general rule it is concluded that microporous materials must be described with a basic three-parameter model, while macroporous materials must be described with a simplified two-parameter model. The heats of adsorption, determined from the adsorption equilibrium constant, agree well with the values determined independently from uptake experiments. With Multitrack a single value for the diffusivity is obtained at a given temperature, valid for the low pressure limit, whereas with uptake a range of diffusivities is found, covering a wide concentration range. The values were of the same order of magnitude. Multitrack is a promising method for the simultaneous determination of adsorption and diffusion parameters. (C) 2001 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:2113 / 2130
页数:18
相关论文
共 19 条
[1]   CONCENTRATION-DEPENDENCE OF SURFACE-DIFFUSION AND ZEOLITIC DIFFUSION [J].
CHEN, YD ;
YANG, RT .
AICHE JOURNAL, 1991, 37 (10) :1579-1582
[2]  
Do D.D., 1998, ADSORPTION ANAL EQUI
[3]   TEMPORAL ANALYSIS OF PRODUCTS (TAP) - A UNIQUE CATALYST EVALUATION SYSTEM WITH SUBMILLISECOND TIME RESOLUTION [J].
GLEAVES, JT ;
EBNER, JR ;
KUECHLER, TC .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1988, 30 (01) :49-116
[4]  
GREGG SJ, 1982, ADSORPTION SURFACE
[5]   KNUDSEN DIFFUSION IN RANDOM ASSEMBLAGES OF UNIFORM SPHERES [J].
HUIZENGA, DG ;
SMITH, DM .
AICHE JOURNAL, 1986, 32 (01) :1-6
[6]   CONTRIBUTION OF CONCENTRATION-DEPENDENT SURFACE-DIFFUSION TO RATE OF ADSORPTION [J].
KAPOOR, A ;
YANG, RT .
CHEMICAL ENGINEERING SCIENCE, 1991, 46 (08) :1995-2002
[7]  
Karger J., 1992, Diffusion in zeolites and other microporous solids
[8]  
Krishna R., 1993, Gas Sep. Purify, V7, P91, DOI DOI 10.1016/0950-4214(93)85006-H
[9]   On the theory of surface diffusion: kinetic versus lattice gas approach [J].
Krylov, SY ;
Beenakker, JJM ;
Tringides, MC .
SURFACE SCIENCE, 1999, 420 (2-3) :233-249
[10]   Difference of diffusivities in zeolites measured by the non-steady-state and the steady-state methods [J].
Liang, WG ;
Chen, SY ;
Peng, SY .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (05) :1882-1886