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Transesterification of cyclohexyl acrylate with n-butanol and 2-ethylhexanol: acid trated clay, ion exchange resins and tetrabutyl titanate as catalysts

机译:丙烯酸环己酯与正丁醇和2-乙基己醇的酯交换反应:酸处理的粘土,离子交换树脂和钛酸四丁酯作为催化剂

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摘要

Transesterification of cyclohexyl acrylate with n-butanol and 2-ethylhexanol was stuided in a batch reactor using an acid-treated clay, ion exchange resins and tetrabutyl titanates as catalysts. The effect of various parameters on the conversion of cyclohexyl acrylate and towards the selectivity of cyclohexanol were studied to optimise the reaction conditions. The transesterfied esters (n-butyl acrylate and 2-ethylhexyl) were separated from the reaction mixture by fractional vacuum distillation and were characterised by ~1H NMR. The experimental results were described by a kinetic model based on Langmuir-Hinshelhood-Hougen-Watson (LHHW) mechanism for the transesterification of cyclohexyl acrylate with n-butanol in the presence of Engelhard F-24 as catalyst and the kinetic parameters were evaluated.
机译:使用酸处理过的粘土,离子交换树脂和钛酸四丁酯作为催化剂,在间歇反应器中进行丙烯酸环己酯与正丁醇和2-乙基己醇的酯交换反应。为优化反应条件,研究了各种参数对丙烯酸环己酯转化率和对环己醇选择性的影响。通过分馏真空蒸馏从反应混合物中分离出酯交换的酯(丙烯酸正丁酯和2-乙基己基),并通过〜1 H NMR对其进行表征。通过基于Langmuir-Hinshelhood-Hougen-Watson(LHHW)机理的动力学模型描述了实验结果,该模型用于在Engelhard F-24作为催化剂存在下将丙烯酸环己酯与正丁醇进行酯交换反应,并评估了动力学参数。

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