丙酸和丙酸甲酯与甲醛和甲醇复合多相催化缩合酯化反应的动力学模型

V. Ivasiv, R. Nebesnyi, S. V. Maykova
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引用次数: 0

摘要

在钨和锆氧化物促进的二氧化硅负载的硼磷氧化物催化剂存在下,丙酸甲酯和丙酸与甲醛和甲醇进行缩合和酯化反应合成甲基丙烯酸甲酯和甲基丙烯酸的动力学模型。研究了丙酸甲酯、丙酸、甲醛和甲醇浓度对甲基丙烯酸甲酯、甲基丙烯酸和二乙基酮生成速率的依赖关系,并确定了每种试剂对每种产物生成的反应顺序。甲基丙烯酸主要由丙酸甲酯与甲醛缩合而成,甲基丙烯酸甲酯水解作用不显著。甲基丙烯酸甲酯生成反应速率受丙酸甲酯在催化剂表面吸附速率的限制,甲醛、丙酸和甲醇的吸附均抑制了甲基丙烯酸甲酯和甲基丙烯酸的生成反应。根据得到的数据,给出了反应方案,包括生成3-羟基-2-甲基丙烷酸及其甲酯和3,3-二羟基-2-甲基戊酸等中间体。在此基础上,利用稳态近似导出了反应动力学模型。根据实验数据计算了该模型的反应速率常数及其活化能。通过实验数据与理论计算数据的对比,验证了模型的有效性。因此,所建立的动力学模型较好地描述了丙酸甲酯和丙酸与甲醛和甲醇的复合缩合酯化反应过程,以及丙酸甲酯与甲醛和丙酸与甲醛的部分缩合反应情况,适合工艺优化和工艺计算。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
The kinetic model of the combined heterogeneously catalyzed condensation and esterification of propionic acid and methyl propionate with formaldehyde and methanol
In this work we aim for developing a kinetic model for the methyl methacrylate and methacrylic acid synthesis by the combined condensation and esterification of methyl propionate and propionic acid with formaldehyde and methanol in the presence of the silica-supported boron-phosphorus-oxide catalyst promoted by oxides of tungsten and zirconium. The dependencies of the formation rates of methyl methacrylate, methacrylic acid and diethyl ketone from the concentrations of methyl propionate, propionic acid, formaldehyde and methanol were studied, and reaction orders of every product formation with respect to each reagent were determined. Methacrylic acid is formed predominantly by condensation of methyl propionate with formaldehyde, and methyl methacrylate hydrolysis is insignificantly. The methyl methacrylate formation reaction rate is limited by the methyl propionate adsorption rate on the catalyst surface, and both reactions of methyl methacrylate and methacrylic acid formation are inhibited due to adsorption of formaldehyde, propionic acid and methanol. Based on obtained data, the reaction scheme was offered, which includes formation of intermediates such as 3-hydroxy-2-methylpropanoic acid, its methyl ester and 3,3-dihydroxy-2-methylpentanoic acid. From this reaction scheme the kinetic model was derived using steady state approximation. The reaction rate constants and their activation energies for this model were calculated from experimental data. Validity of the model was experimentally confirmed by the correlation between experimental and theoretically calculated data. Therefore, the developed kinetic model satisfactorily describes the process of the combined condensation and esterification of methyl propionate and propionic acid with formaldehyde and methanol as well as partial cases of condensation of methyl propionate with formaldehyde and propionic acid with formaldehyde, and is suitable for process optimization and technological calculations.
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