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Experimental and kinetic modeling study of butene isomer pyrolysis: Part I. 1-and 2-Butene

机译:丁烯异构体热解的实验和动力学建模研究:第一部分1-和2-丁烯

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1- and 2-Butene pyrolysis experiments were performed using a tubular flow reactor at an absolute pressure of similar to 0.82 atm over a temperature range of 535-810 degrees C with residence times ranging from similar to 0.5-similar to 2.4 s. The initial concentration of the fuel ranged from 5 to 50 mol%. These data were compared to the predictions of a fundamentally based detailed kinetic modeL For both sets of experiments, the model accurately predicts the observed fuel conversion, production of light products, and the formation of several important molecular weight growth species. The primary pathways that lead to the fuel decay and major product formation are discussed. One of the important kinetic features of 1-and 2-butene pyrolysis is that significant amounts of 1,3-butadiene are produced. The addition reactions of vinyl, allyl, and methyl allyl radicals to 1,3-butadiene are all energetically favorable, leading to substantial production of higher molecular weight species. The model was also applied to published pyrolysis and oxidation data for 1-and 2-butene that were collected under significantly different conditions. The comparison to the latter data sets illustrate that, even under oxidation conditions, it is important to properly account for the pyrolysis kinetics. (C) 2016 The Combustion Institute. Published by Elsevier Inc. All rights reserved.
机译:使用管状流动反应器在535-810摄氏度的温度范围内,以类似于0.82 atm的绝对压力进行1-和2-丁烯的热解实验,其停留时间为0.5到2.4 s。燃料的初始浓度为5至50摩尔%。将这些数据与基于基本原理的详细动力学模式的预测进行了比较。对于这两组实验,该模型均准确地预测了观察到的燃料转化率,轻产物的产生以及几种重要的分子量增长物质的形成。讨论了导致燃料衰减和主要产物形成的主要途径。 1-和2-丁烯热解的重要动力学特征之一是产生大量的1,3-丁二烯。乙烯基,烯丙基和甲基烯丙基自由基与1,3-丁二烯的加成反应在能量上都是有利的,从而导致大量生产更高分子量的物质。该模型还应用于公开发布的在不同条件下收集的1-和2-丁烯的热解和氧化数据。与后面数据集的比较表明,即使在氧化条件下,正确考虑热解动力学也很重要。 (C)2016年燃烧研究所。由Elsevier Inc.出版。保留所有权利。

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