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乙烯氢甲酰化动力学研究

Studies on kinetics of ethylene hydroformylation

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【作者】 杨普王玲刁琰琰李春山王蕾

【Author】 Yang Pu;Wang Ling;Diao Yanyan;Li Chunshan;Wang Lei;Beijing Key Laboratory of Ionic Liquids Clean Process, Institute of Process Engineering, Chinese Academy of Sciences;

【机构】 中国科学院过程工程研究所离子液体清洁过程北京市重点实验室多相复杂系统国家重点实验室

【摘要】 固定甲苯、催化剂及配体用量,对乙烯在甲苯溶剂中的氢甲酰化反应动力学进行了研究。以反应计量比为1:1:1的乙烯、一氧化碳和氢气为反应混合气,测定了100℃、93℃和81℃下反应压力随时间的变化曲线,通过动力学方程求解获得了3种气体总的反应级数、反应速率常数和活化能,得到反应的活化能为55.0 k J/mol。进一步通过一氧化碳和氢气过量,得到了乙烯的反应级数。然后通过氢气过量,得到了乙烯和一氧化碳的总反应级数,随后即计算得到了一氧化碳和氢气各自的反应级数,表明一氧化碳分压高会抑制反应速率,而增加乙烯和氢气分压对反应速率有促进作用。

【Abstract】 Kinetics of ethylene hydroformylation using toluene as solvent was investigated by changing the temperature and molar ratio of C2H4, CO and H2 with fixed amounts of toluene, catalyst, and ligand. The reaction pressure changing with time with the reactant gas of C2H4:CO:H2 = 1:1:1 was determined at 100°C, 93°C, and 81°C. The sum reaction order of three gases, constant rate constant and activation energy were calculated. The activation energy of the reaction was 55.0 k J/mol. By overdosing CO and H2, the reaction order of C2H4 was gotten. And by overdosing H2, the sum reaction order of C2H4 and CO was obtained, then the respective reaction order of C2H4 and CO was calculated. The results showed that high partial pressure of CO was not good for the reaction rate, and the reaction rate increased with the partial pressure increasing of C2H4 or H2.

【关键词】 乙烯氢甲酰化动力学
【Key words】 ethylenehydroformylationkinetics
【基金】 国家自然科学基金资助项目(21476239);中国科学院战略性先导科技专项(XDA07070600)
  • 【文献出处】 计算机与应用化学 ,Computers and Applied Chemistry , 编辑部邮箱 ,2016年04期
  • 【分类号】O621.25
  • 【被引频次】2
  • 【下载频次】290
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