STEADY-STATE MODELS FOR SO2 OXIDATION IN A TRICKLE-BED REACTOR

被引：10

作者：

HAURE, PM ^{[1
]}

HUDGINS, RR ^{[1
]}

SILVESTON, PL ^{[1
]}

机构：

[1] UNIV WATERLOO,DEPT CHEM ENGN,WATERLOO N2L 3G1,ONTARIO,CANADA

来源：

CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL | 1990年 / 43卷 / 03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(90)80013-3

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

Published mathematical models for the steady-state operation of integral trickle-bed reactors are not all capable of predicting experimental results obtained for the catalytic oxidation of sulfur dioxide over activated carbon. Only the model of Mata and Smith (Chem. Eng. J., 22 (1981) 229), which considers variable gas composition within the reactor as well as the variability of the wetting efficiency with the liquid flow rate was successful. An empirical relationship between the wetting and the liquid flow rate was derived from steady-state data and found to coincide with that of Herskowitz (Chem. Eng. J., 22 (1981) 167). © 1990.

引用

页码：121 / 125

页数：5

共 20 条

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