Modelling a reverse flow reactor for the catalytic combustion of fugitive methane emissions

被引:76
作者
Salomons, S
Hayes, RE
Poirier, M
Sapoundjiev, H
机构
[1] Univ Alberta, Dept Chem & Mat Sci, Edmonton, AB T6G 2G6, Canada
[2] Nat Resources Canada, CANMET Energy Technol Ctr Varennes, Varennes, PQ J3X 1S6, Canada
关键词
catalytic combustion; methane; reverse flow;
D O I
10.1016/j.compchemeng.2003.12.006
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
This paper describes the development and validation of a computer simulator for the modelling of a reverse flow catalytic reactor for the combustion of lean mixtures of methane in air. The simulator uses a heterogeneous two dimensional model for the reactor. The reactor uses a packed bed for catalytic sections and ceramic monoliths for inert sections, although the simulator is written in a general fashion so that any combination of packing can be used, in any desired variety. Validation is performed using a 200 mm internal diameter reactor over various flowrates and methane concentrations. The reverse flow reactor is observed to yield stable auto-thermal operation even for low methane concentrations. Higher methane concentrations are observed to give dual temperature peaks in the reactor. The transfer of energy is observed to be a significant factor in the reactor operation, which is shown by comparison of the heterogeneous model to a pseudo-homogeneous reactor model. The simulator can model the pilot reactor in real time for typical operating conditions. (C) 2004 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1599 / 1610
页数:12
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