AIR PURIFICATION BY CATALYTIC-OXIDATION IN A REACTOR WITH PERIODIC-FLOW REVERSAL

被引:38
作者
VANDEBELD, B
WESTERTERP, KR
机构
[1] Chemical Reaction Engineering Laboratories, Department of Chemical Engineering, University of Twente, Enschede, 7500 AE
关键词
D O I
10.1002/ceat.270170402
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The behaviour of an adiabatic packed bed reactor with periodic flow reversal has been studied by means of model calculations. A heterogeneous model as well as a pseudo-homogeneous model have been developed. It is shown that a high degree of conversion can be obtained in an autothermal process even with very low adiabatic temperature rises of some 10 to 20 K. The reactor is insensitive to fluctuations in inlet concentrations and in through put. Short-cut methods proposed in the literature for calculating the plateau temperature in the pseudo-steady state are studied. The so called countercurrent-flow reactor approach showed reasonable agreement with the plateau temperature obtained by dynamic calculations with the full reactor model.
引用
收藏
页码:217 / 226
页数:10
相关论文
共 31 条
[1]   DEEP CATALYTIC-OXIDATION KINETICS OF BENZENE-ETHENYLBENZENE MIXTURES [J].
BARRESI, AA ;
BALDI, G .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (08) :1943-1953
[2]   GAS-PHASE COMPLETE CATALYTIC-OXIDATION OF AROMATIC HYDROCARBON MIXTURES [J].
BARRESI, AA ;
MAZZARINO, I ;
BALDI, G .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1992, 70 (02) :286-293
[3]   ANALYSIS OF CATALYTIC REACTOR OPERATION WITH PERIODIC-FLOW REVERSAL [J].
BHATIA, SK .
CHEMICAL ENGINEERING SCIENCE, 1991, 46 (01) :361-367
[4]  
BORESKOV GK, 1982, KINET CATAL+, V23, P335
[5]  
BORESKOV GK, 1979, KINET CATAL+, V20, P636
[6]  
BORESKOV GK, 1986, DOKLADY CHEM TECH, V288, P55
[7]  
BORESKOV GK, 1982, DOKL CHEM TECHNOL, V268, P15
[8]  
BUNIMOVICH GA, 1990, JUN UNST STAT PROC C, P7
[9]  
CHUMACHENKO VA, 1990, JUN UNST STAT PROC C, P605
[10]  
CHUMAKOVA NA, 1990, JUN UNST STAT PROC C, P477