辽宁石油化工大学学报

辽宁石油化工大学学报 ›› 2008, Vol. 28 ›› Issue (2): 11-14.

• 石油化工 • 上一篇    下一篇

CuSO4/SiO2固体酸催化合成环己酮乙二醇缩酮

高文艺张晓丽任立国*   

  1. 辽宁石油化工大学化学与材料科学学院, 辽宁抚顺 113001
  • 收稿日期:2007-10-24 出版日期:2008-06-20 发布日期:2017-07-23

Catalytic Synthesis of Cyclohexanon Ethylene Ketal  With CuSO4/SiO2 Solid Acid

GAO Wen-yiZHANG Xiao-li, REN Li-guo*   

  1. School of Chemistry and Materials Science, Liaoning University of Petroleum & Chemical Technology, Fushun Liaoning 113001,P.R.China
  • Received:2007-10-24 Published:2008-06-20 Online:2017-07-23

摘要: 通过溶胶-胶凝法和浸渍法制备了CuSO4/SiO2固体酸催化剂,用XRD、N2-吸附和NH3-TPD进行了表征,研究了CuSO4/SiO2固体酸催化合成环己酮乙二醇缩酮的催化性能,考察了催化剂的焙烧温度、CuSO4负载量、催化剂用量、酮醇摩尔比等因素的影响。结果表明,CuSO4/SiO2固体酸催化剂在环己酮和乙二醇的缩合反应中具有良好的催化活性和稳定性。催化剂制备和缩合反应的最佳条件为:焙烧温度为500 ℃、CuSO4的负载量为20%、酮醇摩尔比为1∶1.2、催化剂的用量1.1 g,在此条件下,环己酮乙二醇缩酮的收率可达99.1%。

关键词: 溶胶-胶凝, 浸渍, 固体酸, 缩酮化反应, 环己酮乙二醇缩酮

Abstract: The CuSO4/SiO2 solid acid catalyst was prepared by sol-gel and impregnation methods. The CuSO4/SiO2 solid acid catalyst were characterized by XRD、N2-adsorption and NH3-TPD. Cyclohexanone ethylene ketal was synthesized from cyclohexanone and ethylene glycol through condensation, CuSO4/SiO2 as catalyst. The effects of calcination temperature of catalyst, CuSO4 loading, catalyst dosage, molar ratio of reactants, reaction time,types and volume of entrainer on the synthesis were investigated. The results show that the CuSO4 solid acid catalyst has high catalytic activities and good stability. The optimum conditions are as follows: the calcination temperature of catalyst is 500 ℃, the CuSO4 loading is 20%(w), molar ratio of cyclohexanone to ethylene glycol is 1∶1.2. Under these conditions, the yield of cyclohexanone ethylene ketal  would  be 99.1%.

Key words: Sol-gel, Impregnation, Solid acid, Ketalization reaction, Cyclohexanone ethylene ketal

引用本文

高文艺, 张晓丽, 任立国. CuSO4/SiO2固体酸催化合成环己酮乙二醇缩酮[J]. 辽宁石油化工大学学报, 2008, 28(2): 11-14.

GAO Wen-yi, ZHANG Xiao-li, REN Li-guo. Catalytic Synthesis of Cyclohexanon Ethylene Ketal  With CuSO4/SiO2 Solid Acid[J]. Journal of Liaoning Petrochemical University, 2008, 28(2): 11-14.

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