NONISOTHERMAL REACTOR DESIGN FOR VARIABLE-DENSITY SYSTEMS

被引:1
|
作者
ADESINA, AA [1 ]
机构
[1] UNIV WATERLOO,DEPT CHEM ENGN,WATERLOO N2L 3G1,ONTARIO,CANADA
来源
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL | 1991年 / 47卷 / 01期
基金
加拿大自然科学与工程研究理事会;
关键词
D O I
10.1016/0300-9467(91)85003-E
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this paper, we present the necessary equations which describe the rate-temperature-conversion (r-T-X) behaviour and the optimum temperature progression (OTP) profile for a general class of reversible reactions which admits density changes. The utility of these equations is demonstrated by examples. Analysis reveals that if the sums of the orders of the reactants and products are equal, then the OTP path is independent of the density parameter. Interestingly, this implies that the ideal reactor size would be the same as if there was no density change. For other situations, however, the density parameter can have a substantial effect on the position of the OTP and this has been investigated.
引用
收藏
页码:17 / 24
页数:8
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