利用量子化学模型对沸石型催化剂布氏酸性位点上的常烷烃(C4C6)单分子裂解进行动力学分析,并对过渡态进行能量评估

Saba Foroutan Ghazvini, Elena Ivashkina Nikolaevna
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引用次数: 0

摘要

这项工作旨在利用量子化学计算,根据过渡态的能量特征,确定通过 C4-C6 正构烷烃催化裂解反应生产轻烯烃的反应动力学参数。C4-C6 正构烷烃的裂解反应是在含沸石催化剂的布氏酸位点上通过原解机理进行的。在动力学研究中,首先确定了中间阶段的热化学参数,包括碳氢化合物吸附和过渡态,然后确定了催化裂解过程温度范围为 773 至 903 K(500 至 630 ℃)的活化能和速率常数。结果表明,结合 B3LYP 和 ωB97X-D 函数以及 3-21 G 基的 DFT 方法在确定热化学参数(包括吸附和过渡态两个能级的焓、熵和吉布斯自由能)方面具有相当高的准确性。然后,通过计算反应的活化能和速率常数继续进行建模。获得的动力学参数使得确定不同链长碳氢化合物的反应性成为可能。结果表明,丁烷裂解反应生成乙烯的速率常数比生成丙烯的速率常数高 54-90 倍。戊烷裂解反应生成丁烯的速率常数平均比生成丙烯的速率常数高 5 倍。形成丁烯的己烷裂解反应的速率常数比形成丙烯的速率常数高 2.9-3.7 倍。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Kinetic analysis of monomolecular cracking of normal Alkanes (C4C6) over Brønsted Acid site of Zeolitic type catalyst with energetic evaluation of transition states using Quantum-Chemical modeling

The work aims to determine the kinetic parameters of reactions for production of light olefins via catalytic cracking reactions of C4–C6 n-alkanes based on the energy characteristics of the transition state using quantum chemical calculations. Cracking reactions of C4–C6 n-alkanes proceed via protolytic mechanism on the Brønsted acid sites of zeolite-containing catalysts. For kinetic studies in this work, the thermochemical parameters of the intermediate stages, including hydrocarbon adsorption and transition state were determined, then the activation energies and rate constants were determined over the temperature range of catalytic cracking process from 773 to 903 K (500–630 °C).

The results showed that DFT method in combination with B3LYP and ωB97X-D functionals, and 3–21 G basis demonstrated quite high accuracy in determining thermochemical parameters, including enthalpy, entropy and Gibbs free energy at both energetic levels of adsorption and transition state. Then, modeling continued by calculations of activation energies and rate constants of reactions. Obtained kinetic parameters made it possible to determine the reactivity of hydrocarbons with different chain length. It was obtained that the rate constants of butane cracking reactions with the formation of ethylene are 54–90 times higher than the formation of propylene. The rate constants of pentane cracking reactions with the formation of butylene are on average 5 times higher than the formation of propylene. The rate constants for hexane cracking reactions with the formation of butylene are 2.9–3.7 times higher compared to the formation of propylene.

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