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

机译:对逆流反应器建模以催化燃烧逃逸的甲烷排放

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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.
机译:本文介绍了计算机模拟器的开发和验证,该计算机模拟器用于建模逆流催化反应器,用于燃烧空气中稀薄的甲烷混合物。该模拟器对反应堆使用异质二维模型。尽管模拟器以一般方式编写,所以反应器使用填充床用于催化段,并使用陶瓷整体料用于惰性段,以便可以使用任何所需种类的填料的任何组合。使用200 mm内径反应器在各种流速和甲烷浓度下进行验证。观察到逆流反应器即使在低甲烷浓度下也能产生稳定的自热运行。观察到较高的甲烷浓度在反应器中产生双重温度峰。观察到能量转移是反应堆运行中的重要因素,通过将异质模型与伪均质反应堆模型进行比较可以看出这一点。模拟器可以针对典型运行条件实时模拟中试反应堆。

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