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The Reaction kinetics of Dimethyl Ether. I: High-Temperature pyrolysis and Oxidation in Flow Reactors

机译:二甲醚的反应动力学。 I:流动反应器中的高温热解和氧化

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Dimethyl ether reaction kinetics at high temperature were studied in two different flow reactors under highly dilute conditios. Pyrolysis of dimethyl ether was studied in a variable-pressure flow reactor at 2.5 atm and 1118 K. Studies were also conducter in an atmospheric pressure flow reactor at about 1085 K. These experiments included trace-oxygen-assisted pyrolysis, as well as full oxidation experiments, with the equivalence ratio (#PHI#) varying from 0.32<=#PHI#<=3.4. On-line, continuous, extractive sampling in conjunction with Fourier Transform infra-Red, No-Dispersive Infra-Red (for CO and CO_2) and electrochemical (for O_2) analyses were performed to quantify species at specific locations along the axis of the turbulent flow reactors. Species concentrations were correlated against residence time in the reactor and species evolution profiles were compared to the predictions of a previously published detailed kinetic mechanism. Some changs were made to the model in order to improve agreement with the present experimental data. However, the revised model continues to reproduce previously reported high-temperature jet-stirred reactor and shock tube results.
机译:在高度稀释的条件下,在两个不同的流动反应器中研究了高温下的二甲醚反应动力学。在2.5 atm和1118 K的变压流动反应器中研究了二甲醚的热解。还在大气压流动反应器中在约1085 K的温度下进行了导体研究。这些实验包括微量氧辅助热解以及完全氧化实验中,当量比(#PHI#)从0.32 <=#PHI#<= 3.4不等。在线,连续,提取采样与傅里叶变换红外,无色散红外(用于CO和CO_2)和电化学(用于O_2)结合进行分析,以定量确定湍流轴上特定位置的物种流动反应器。将物种浓度与反应器中的停留时间相关联,并将物种演化曲线与先前公布的详细动力学机制的预测进行比较。为了改善与当前实验数据的一致性,对模型进行了一些更改。但是,修改后的模型继续复制了先前报道的高温喷射搅拌反应堆和激波管结果。

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