THE USE OF MATHEMATICAL-MODELING TO INVESTIGATE THE EFFECT OF CHEMISORPTION ON THE DYNAMIC BEHAVIOR OF CATALYTIC REACTORS - PARTIAL OXIDATION OF ORTHO-XYLENE IN FLUIDIZED-BEDS

被引：13

作者：

ELNASHAIE, SSEH ^{[1
]}

FOUAD, MMK ^{[1
]}

ELSHISHINI, SS ^{[1
]}

机构：

[1] UNIV CAIRO,FAC ENGN,DEPT CHEM ENGN,CAIRO,EGYPT

来源：

MATHEMATICAL AND COMPUTER MODELLING | 1990年 / 13卷 / 05期

关键词：

D O I：

10.1016/0895-7177(90)90039-P

中图分类号：

TP39 [计算机的应用];

学科分类号：

081203 ; 0835 ;

摘要：

The effect of catalyst surface adsorption mass capacity and heat of adsorption on the dynamic behavior of the o-xylene catalytic partial oxidation reaction is investigated using a simple fluidized-bed reactor model developed previously. The chemisorption process, though assumed at equilibrium, is shown to have a strong influence upon the dynamic behavior of the system. © 1990.

引用

页码：11 / 21

页数：11

共 37 条

[1]

[Anonymous], 1991, FLUID ENG, DOI DOI 10.1016/B978-0-08-050664-7.50009-3

[2]

ARIS R, 1975, MATH THEORY DIFFUSIO, V2, P162

[3] INVESTIGATION OF A FIXED-BED PILOT-PLANT REACTOR BY DYNAMIC EXPERIMENTATION .2. SIMULATION OF REACTOR BEHAVIOR [J].