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Kinetic modeling of ethane pyrolysis at high conversion

机译:高转化率乙烷热解的动力学模型

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The primary objective of this study is to develop an improved first-principle-based mechanism that describes the molecular weight growth kinetics observed during ethane pyrolysis. A proper characterization of the kinetics of ethane pyrolysis is a prerequisite for any analysis of hydrocarbon pyrolysis and oxidation. Flow reactor experiments were performed with ~50/50 ethaneitrogen mixtures with temperatures ranging from 550 to 850 °C at an absolute pressure of ~0.8 atm and a residence time of ~5 s. These conditions result in ethane conversions ranging from virtually no reaction to ~90%. Comparisons of predictions using our original mechanism to these data yielded very satisfactory results in terms of the temperature dependence of ethane conversion and prediction of the major products ethylene and hydrogen. However, there were discrepancies in some of the minor species concentrations that are involved in the molecular weight growth kinetics. We performed a series of CBS-QB3 analyses for the C_3H_7, C_4H_7, and C_4H_9 potential energy surfaces to better characterize the radical addition reactions that lead to molecular weight growth. We also extended a published C_6H_9 PES to include addition of vinyl to butadiene. The results were then used to calculate pressure-dependent rate constants for the multiple reaction pathways of these addition reactions. Inclusion of the unadjusted rate constants resulting from these analyses in the mechanism significantly improved the description of several of the species involved in molecular weight growth kinetics. We compare the predictions of this improved model to those obtained with a consensus model recently published as well as to ethane steam cracking data. We find that a particularly important reaction is that of vinyl addition to butadiene. Another important observation is that several radical addition reactions are partially equilibrated. Not only does this mean that reliable thermodynamic parameters are essential for an accurate model, but also that the reaction set describing molecular weight growth chemistry must include a final product that is sufficiently stable to shift the equilibrium toward this product despite the decrease in entropy that accompanies molecular weight growth. Another reaction, H addition to olefins, was found to inhibit molecular weight growth by leading to the production of a lower olefin plus methyl radicals.
机译:这项研究的主要目的是开发一种改进的基于第一原理的机制,该机制描述了乙烷热解过程中观察到的分子量增长动力学。乙烷热解动力学的正确表征是烃热解和氧化分析的前提。使用〜50/50的乙烷/氮气混合物进行流动反应器实验,温度范围为550至850°C,绝对压力为〜0.8 atm,停留时间为〜5 s。这些条件导致乙烷转化率从无反应到约90%不等。就乙烷转化率的温度依赖性以及主要产物乙烯和氢的预测而言,使用我们原始机制与这些数据进行的预测比较得出了非常令人满意的结果。但是,分子量增长动力学中涉及的一些次要物种浓度存在差异。我们对C_3H_7,C_4H_7和C_4H_9势能面进行了一系列CBS-QB3分析,以更好地表征导致分子量增长的自由基加成反应。我们还扩展了已发布的C_6H_9 PES,将乙烯基添加到丁二烯中。然后将结果用于计算这些加成反应的多个反应路径的压力依赖性速率常数。由这些分析得出的未调整的速率常数包括在机理中,极大地改善了对涉及分子量增长动力学的几种物质的描述。我们将这种改进模型的预测与最近发布的共识模型获得的预测以及乙烷蒸汽裂解数据进行了比较。我们发现特别重要的反应是乙烯基向丁二烯的加成反应。另一个重要的观察结果是,几个自由基加成反应是部分平衡的。这不仅意味着可靠的热力学参数对于精确的模型必不可少,而且描述分子量增长化学的反应组必须包含最终产物,该产物必须足够稳定,以使平衡向该产物转移,尽管伴随的熵降低分子量增长。发现另一种反应,除了烯烃中的H,通过导致产生低级烯烃加甲基基团来抑制分子量的增长。

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