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乙烯氢酯基化合成丙酸甲酯催化反应动力学研究
引用本文:廖列文,崔英德,尹国强.乙烯氢酯基化合成丙酸甲酯催化反应动力学研究[J].天然气化工,2004,29(5):26-31.
作者姓名:廖列文  崔英德  尹国强
作者单位:1. 广东工业大学轻工化工学院,广州,510090
2. 仲恺农业技术学院,广州,510225
摘    要:采用以三氯化钌为主的催化体系,在高压釜中采用虹吸式涡轮搅拌器消除乙烯在气液两相中的传递因素对反应带来的影响,研究了以甲酸甲酯为原料,通过乙烯氢酯基化反应合成丙酸甲酯的催化反应动力学。探讨了该反应的机理,得到)(β-1)],反应速率常数k1=0 0668mol/(s·L),反应活化能CA/(1-1/β)]1-(CA/CA0反应的动力学数学模型为rp=k1CM0E=81 363kJ/mol。

关 键 词:三氯化钌  甲酸甲酯  丙酸甲酯  乙烯氢酯基化  动力学  叶轮
文章编号:1001-9219(2004)05-26-05

Kinetic Study of Catalytic Reaction for Hydroesterification of Ethylene to Propionic Ester
LIAO Lie-wen,CUI Ying-de,YIN Guo-qiang.Kinetic Study of Catalytic Reaction for Hydroesterification of Ethylene to Propionic Ester[J].Natural Gas Chemical Industry,2004,29(5):26-31.
Authors:LIAO Lie-wen  CUI Ying-de  YIN Guo-qiang
Affiliation:LIAO Lie-wen~1,CUI Ying-de~2,YIN Guo-qiang~2
Abstract:The kinetics about hydroesterification of ethylene with methyl formate in RuCl_3 catalyst system was studied. The effect of mass transfer on the reaction was eliminated through using suction turbine impeller. The reaction mechanism was discussed and the kinetic equation was deduced as r_p=k_1C_(M_0)C_A/(1-1/β)]1-(C_A/C_(A_0))~((β-1))]. Rate constant (k_1) and active energy(E) obtained from the experiments are 0.0668mol/(s·L) and 81.363 kJ/mol, respectively.
Keywords:RuCl_3  methyl formate  methyl propionate  hydroesterification  kinetics  impeller  
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