Measurement and modeling of the kinetics of catalyst decay in fixed beds: The Eurokin survey

被引:15
作者
Birtill, John J. [1 ]
机构
[1] Univ Glasgow, Dept Chem, Glasgow G12 8QQ, Lanark, Scotland
关键词
DEACTIVATION KINETICS; SOLID CATALYSTS; COKE FORMATION; REACTORS; MICROBALANCE; EQUATION; NICKEL; COKING;
D O I
10.1021/ie060590v
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Experimental techniques for the practical measurement of catalyst decay are reviewed, and some gaps and needs are suggested for future progress. Catalyst decay kinetics in fixed beds can be modeled according to a hierarchy of techniques, from purely empirical to rigorously fundamental. Empirical modeling is usually preferred for practical industrial purposes. Besides the need to decouple reaction kinetics, decay kinetics, and any influence of pore diffusion, for slowly decaying catalysts, the slow rate of data acquisition is a limiting factor. Hence, there is a need for better equipment design and better procedures for the efficient and informative testing of catalyst decay.
引用
收藏
页码:2392 / 2398
页数:7
相关论文
共 40 条
[11]   MODELING OF THE DEACTIVATION KINETICS OF SOLID CATALYSTS BY 2 OR MORE SIMULTANEOUS AND DIFFERENT CAUSES [J].
CORELLA, J ;
MONZON, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1988, 27 (03) :369-374
[12]   DEACTIVATION OF A PLATINUM REFORMING CATALYST IN A TUBULAR REACTOR [J].
DEPAUW, RP ;
FROMENT, GF .
CHEMICAL ENGINEERING SCIENCE, 1975, 30 (08) :789-801
[13]   COKE FORMATION ON SILICA-ALUMINA CRACKING CATALYSTS [J].
EBERLY, PE ;
KIMBERLI.CN ;
MILLER, WH ;
DRUSHEL, HV .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1966, 5 (02) :193-&
[14]   Modeling of catalyst deactivation [J].
Froment, GF .
APPLIED CATALYSIS A-GENERAL, 2001, 212 (1-2) :117-128
[15]   NON-STEADY STATE BEHAVIOUR OF FIXED BED CATALYTIC REACTORS DUE TO CATALYST FOULING [J].
FROMENT, GF ;
BISCHOFF, KB .
CHEMICAL ENGINEERING SCIENCE, 1961, 16 (3-4) :189-201
[16]   KINETIC DATA AND PRODUCT DISTRIBUTIONS FROM FIXED BED CATALYTIC REACTORS SUBJECT TO CATALYST FOULING [J].
FROMENT, GF ;
BISCHOFF, KB .
CHEMICAL ENGINEERING SCIENCE, 1962, 17 (02) :105-&
[17]  
FROMENT GF, 1977, CHEM REACTOR ANAL DE, pCH5
[18]   CATALYST DEACTIVATION AND STEADY-STATE ACTIVITY - A GENERALIZED POWER-LAW EQUATION MODEL [J].
FUENTES, GA .
APPLIED CATALYSIS, 1985, 15 (01) :33-40
[19]  
FUNG SC, 1994, STUD SURF SCI CATAL, V88, P305
[20]   Kinetics of the irreversible deactivation of the HZSM-5 catalyst in the MTO process [J].
Gayubo, AG ;
Aguayo, AT ;
Olazar, M ;
Vivanco, R ;
Bilbao, J .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (23-24) :5239-5249