Efficiency of heat recovery versus maximum catalyst temperature in a reverse-flow combustion of methane

被引：35

作者：

Gosiewski, K ^{[1
]}

机构：

[1] Jan Dlugosz Univ Czestochowa, Inst Chem & Environm Protect, PL-42201 Czestochowa, Poland

来源：

CHEMICAL ENGINEERING JOURNAL | 2005年 / 107卷 / 1-3期

关键词：

chemical reactors; combustion; dynamic simulation; heat recovery; mathematical modeling; reverse-flow reactors;

D O I：

10.1016/j.cej.2004.12.005

中图分类号：

X [环境科学、安全科学];

学科分类号：

08 ; 0830 ;

摘要：

Results of simulations are presented concerning a reverse-flow reactor for the catalytic combustion of methane that occurs in coal-mine ventilation air. The simulations were performed for two types of catalyst: 12% MnO2/gamma-Al2O3 and 0.5% Pd/gamma-Al2O3. A special attention is given to maximum temperature of the catalyst bed in order to minimize occurrence of homogeneous combustion. The simulations revealed that there is a visible contradiction between efficiency of heat recovery aimed to high-pressure steam production and efforts to constraint maximum temperature in the bed. (c) 2004 Elsevier B.V. All rights reserved.

引用

页码：19 / 25

页数：7

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