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Catalytic oxidation of coal mine ventilation air methane in a preheat catalytic reaction reactor

机译:预热催化反应器中煤矿通风甲烷的催化氧化

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The results of experimental investigations on catalytic oxidation of coal mine ventilation air methane in a preheat catalytic reaction reactor is presented in this paper. The experimental system was located in the Energy Research Institute of Shandong University of Technology, which has been applied to investigate the effects of startup conditions such as the startup flow coefficient (0.3-0.5) and the startup power (10 kW-20 kW) on the startup process within the preheat catalytic reaction reactor. The average temperature distribution of catalytic oxidation bed and the minimal startup power were measured and the effects of operating conditions such as the space velocity (2600 h(-1) to 11,500 h(-1)) and the methane concentration (0.8%-1.2%) were experimentally investigated. Moreover, the methane conversion rate and the average temperature of the catalytic oxidation bed were discussed and the critical space velocity value and the critical methane concentration value were determined. Copyright (C) 2015, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
机译:给出了预热催化反应器中煤矿通风甲烷催化氧化的实验研究结果。该实验系统位于山东工业大学能源研究所,用于研究启动条件如启动流量系数(0.3-0.5)和启动功率(10 kW-20 kW)的影响。预热催化反应器中的启动过程。测量了催化氧化床的平均温度分布和最小启动功率,并研究了诸如空速(2600 h(-1)至11,500 h(-1))和甲烷浓度(0.8%-1.2 %)进行了实验研究。此外,讨论了甲烷转化率和催化氧化床的平均温度,并确定了临界空速值和临界甲烷浓度值。 Hydrogen Energy Publications,LLC版权所有(C)2015。由Elsevier Ltd.出版。保留所有权利。

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