首页> 外文期刊>Journal of Analytical & Applied Pyrolysis >Thermal cracking of n-butylcyclohexane at high pressure (100 bar)-Part 2: Mechanistic modeling
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Thermal cracking of n-butylcyclohexane at high pressure (100 bar)-Part 2: Mechanistic modeling

机译:正丁基环己烷在高压(100 bar)下的热裂解-第2部分:力学建模

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A detailed kinetic model consisting of 833 reactions has been developed to describe the thermal cracking of n-butylcyclohexane at high pressure (100 bar). A primary Mechanism was written in an exhaustive manner whereas a partial secondary mechanism was considered to describe the formation and the consumption reactions of aromatic compounds. The model was tested against our experimental data for BCH pyrolysis at 100 bar in the temperature range 375-425 degrees C. A global agreement was reached for BCH conversion up to 50% for both conversion and product yields e.g. propane, cyclohexane and toluene. Flow analysis of the proposed mechanism at a conversion of 35% shows that both alkanes (i.e. methane, ethane, propane and n-butane) and cycloalkanes (i.e. cyclohexane, methylcyclohexane and ethylcyclohexane) mainly come from the breaking of the side alkyl chain. The production of butylbenzene is due to the direct dehydrogenation of BCH whereas other alkylaromatic compounds i.e. benzene, toluene and ethylbenzene seem to come from the breaking of the side alkyl chain of butylbenzene rather than aromatization of cycloalkanes or alkylcyclohexenes. At 100 bar and around 400 degrees C, breaking of alkyl side chain reactions prevail on dehydrogenation reactions and ring opening. (C) 2016 Elsevier B.V. All rights reserved.
机译:已开发出由833个反应组成的详细动力学模型,以描述正丁基环己烷在高压(100 bar)下的热裂解。主要机制以详尽的方式撰写,而部分次要机制被认为描述了芳族化合物的形成和消耗反应。针对我们在375-425摄氏度的温度范围内在100 bar下进行BCH热解的实验数据,对该模型进行了测试。就转化率和产物收率而言,BCH转化率均达到50%的全球协议,例如丙烷,环己烷和甲苯。所提出机理的转化率为35%的流动分析表明,烷烃(即甲烷,乙烷,丙烷和正丁烷)和环烷烃(即环己烷,甲基环己烷和乙基环己烷)均主要来自烷基侧链的断裂。丁基苯的产生是由于BCH的直接脱氢作用,而其他烷基芳族化合物(即苯,甲苯和乙苯)似乎来自丁基苯侧链的断裂,而不是环烷烃或烷基环己烯的芳构化。在100巴和大约400摄氏度下,脱氢反应和开环中烷基侧链反应的断裂占主导。 (C)2016 Elsevier B.V.保留所有权利。

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