首页|钛酸四丁酯催化甲基丙烯酸甲酯与正丁醇酯交换反应动力学研究

钛酸四丁酯催化甲基丙烯酸甲酯与正丁醇酯交换反应动力学研究

Kinetics of the transesterification of methyl methacrylate and n-butanol with tetrabutyl titanate as catalyst

扫码查看
由于设备腐蚀和环境污染等问题,甲基丙烯酸丁酯生产工艺逐渐倾向于更为经济环保的酯交换生产工艺.以钛酸四丁酯为催化剂,甲基丙烯酸甲酯与正丁醇通过酯交换法合成甲基丙烯酸丁酯的反应及机理进行了初步研究.首先,根据路易斯酸催化理论,在合理假设和简化的基础上对该反应的机理进行了分析,在此基础上分别建立了基于理想溶液和非理想溶液的动力学模型.通过酯交换反应实验,主要研究了反应温度、反应物初始物质的量之比和催化剂量等因素对反应速率的影响,并根据实验数据回归得到了动力学模型参数和反应的基本热力学数据.结果显示,该酯交换反应为吸热反应,标准摩尔反应焓为14.406 kJ·mol-1,正、逆反应活化能分别为70.2和51.1 kJ·mol-1.通过模型计算值与实验数据的比较,证明了推导得到的动力学模型具有较高的可靠性,将为钛酸四丁酯催化甲基丙烯酸甲酯与正丁醇酯交换合成甲基丙烯酸丁酯反应提供一定的理论指导.
Due to the problems such as the equipment corrosion and environmental pollution,the produc-tion process of butyl methacrylate is gradually replaced with the more environment-friendly transesterifica-tion process.In this paper,the reaction and mechanism of the synthesis of butyl methacrylate by transes-terification of methyl methacrylate and n-butanol with tetrabutyl titanate as catalyst were initially investi-gated.Based on the Lewis acid catalysis theory,the mechanism of the reaction was proposed through the reasonable assumptions and simplifications,and the kinetic models based on idea solutions(IS)and non-ideal solutions(NIS)were established,respectively.Through the transesterification experiments,the effects of factors such as reaction temperature,initial molar ratio of reactants and the catalyst amount on the reaction rate were studied,and the model parameters of the kinetic model and the thermodynamic data were obtained from the regression of the experimental data.The results show that the transesterification re-action is an endothermic reversible reaction,the standard molar reaction enthalpy is 14.406 kJ·mol-1,and the activation energies of the forward and reverse reactions are 70.2 and 51.1 kJ·mol-1,respectively.The comparison between the calculated values and the experimental data demonstrates that the derived ki-netic model is highly reliable and will provide some theoretical guidance for the synthesis of butyl methac-rylate by transesterification of methyl methacrylate and n-butanol with tetrabutyl titanate catalyst.

transesterification reactionmethyl methacrylatereaction kineticsbutyl methacrylate1-bu-tanoltetrabutyl titanate

彭世仁、王燕、蔡旺锋

展开 >

天津大学化工学院,天津 300350

酯交换反应 甲基丙烯酸甲酯 反应动力学 甲基丙烯酸丁酯 正丁醇 钛酸四丁酯

2024

化学工业与工程
天津化工学会 天津大学

化学工业与工程

CSTPCD北大核心
影响因子:0.406
ISSN:1004-9533
年,卷(期):2024.41(1)
  • 38