苯酚与1-甲基环戊二烯环烷基化反应动力学规律及机理研究

F. I. Gasimova, Ch. K. Rasulov, R. Jafarov, Z. Z. Aghamali̇yev
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引用次数: 0

摘要

本文介绍了苯酚与1-甲基环戊二烯在KU-23催化剂作用下的反应结果。在实验室装置上进行了苯酚的环烷基化反应。反应结束后,烷基酸盐与催化剂分离并精馏。首先,在常压精馏过程中蒸馏出未进入反应的MCP和苯酚(高达200℃),然后在真空(666.5 Pa)下分离目标反应产物,并测定其纯度和理化参数。研究了反应的动力学规律,建立了反应发生的可能机理。建立了苯酚环烷基化反应的动力学模型,该模型由一组微分方程组成,描述了初始物质和反应产物的浓度随时间的变化。采用改进的自动步长选择随机搜索方法估计微分方程的动力学常数。为此,使用了已开发的应用程序包。确定了各个阶段的阶数、活化能和速率常数。结果表明,该模型能较好地描述实验数据。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Study of the kinetic regularities and mechanism of the cycloalkylation reaction of phenol with 1-methylcyclopentadiene
The article presents the results of the reaction of phenol with 1-methylcyclopentadiene in the presence of the KU-23 catalyst. Cycloalkylation of phenol have been carried out in a batch laboratory installation. After the reaction, the alkylate is separated from the catalyst and rectified. Firstly, during rectification at atmospheric pressure MCP and phenol that did not enter into the reaction were distilled off (up to 200° C), and then, under vacuum (666.5 Pa) the target reaction product was isolated and its purity and physicochemical parameters were determined. The kinetic regularities of the reaction were studied, and the probable mechanism of its occurrence was established. A kinetic model of the phenol cycloalkylation reaction, consisting of a system of differential equations, that describes the change in the concentration of the initial substances and reaction products over time has been developed. The kinetic constants of differential equations were estimated using a modified random search method with automatic step selection. For this purpose, the developed package of applied programs was used. The orders, activation energies, and rate constants of individual stages are determined. It is shown that the proposed model adequately describes the experimental data.
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