期刊文献+

锌修饰亚铬酸铜催化甘油制备羟基丙酮 被引量:2

Copper-chromite deposited with zinc catalysts for dehydration of glycerol to acetol
下载PDF
导出
摘要 以锌修饰的亚铬酸铜为催化剂,考察了锌含量、催化剂煅烧温度、催化剂用量、反应温度等条件对甘油脱水制备羟基丙酮的影响。结果表明:助剂锌修饰作用提高了亚铬酸铜的催化剂活性,延长了催化剂的使用次数,提高了羟基丙酮选择性和产率。适宜催化剂制备及反应条件为:硝酸锌浸渍液浓度为10%,焙烧温度为350℃,催化剂用量为4%,反应温度为220℃,羟基丙酮选择性达88.9%。 The zinc-modified copper-chromite catalyst prepared for preparation of acetol by reaction of dehydration of glycerol was investigated.The effect of zinc dosage,catalyst calcination temperature,catalyst dosage,reaction temperature on dehydration of glycerol to acetol were studied.The results showed that: the addition of zinc increased the activity of catalyst,significantly lowers the reaction temperature,increased the yield of acetol,and prolongs the life of the catalyst.The optimal conditions obtained for the reaction with the selectivity of acetol up to 88.9% were as follows:zinc dosage 10%,catalyst calcination temperature 350 ℃,catalyst dosage 4%,reaction temperature 220 ℃.
出处 《应用化工》 CAS CSCD 2011年第6期931-934,共4页 Applied Chemical Industry
基金 国家高技术研究发展(863)计划基金项目(2008AA05Z405) 长沙市科技计划重点基金项目(k1005012-11)
关键词 亚铬酸铜 甘油 脱水 羟基丙酮 copper-chromite zinc glycerol dehydration acetol
  • 相关文献

参考文献2

二级参考文献39

  • 1闵恩泽.利用可再生农林生物质资源的炼油厂——推动化学工业迈入“碳水化合物”新时代[J].化学进展,2006,18(2):131-141. 被引量:33
  • 2沈宜泓,王帅,罗琛,刘海超.生物质利用新途径:多元醇催化合成可再生燃料和化学品[J].化学进展,2007,19(2):431-436. 被引量:21
  • 3Hulaer G W,lbrra S,Corma A.Syntheis of transportation fuels from biomass:Chemistry,catalysts,and engineering[Jl.Chem Rev,2006,106(9):4044-4098.
  • 4Chiu C W,Dasari M A,Supprs G J,et al.Dehydration of glycerol to acetol via catalytic reactive distillation[J].AICHE J,2006,52(10):3.543-3548.
  • 5Tessie C.Production of propanediols[P].US Patent 4,642,394,1987.
  • 6Casale B,Gomez A M.Catalytic method of hydrogenating glycerol[P].US Patent 5,276,181,1994.
  • 7Schuster L,Eggersdorfer M.Preparation of 1,2-propanediol[P].US Patent 5,616,817,1997.
  • 8Miyazawa T,Kusunoki Y,Kunimori K,et al.Glycerol conversion in the aqueous solution under hydrogen over Ru/C+ an ion-exchange resin and its reaction mechanism[J].J Catal,2006,240:213-221.
  • 9Huber G W,Dumesic J A.Catal.Today,2006,111:119-132.
  • 10Chiu C W,Dasari M A,Suppes G J,et al.Ind.Eng.Chem.Res.,2006,45:791-795.

共引文献20

同被引文献23

  • 1潘振良,沈永雯,梁永民.有机合成中的高价碘应用[J].化学进展,2007,19(2):303-312. 被引量:2
  • 2冯建,袁茂林,陈华,李贤均.甘油催化氢解的研究与应用[J].化学进展,2007,19(5):651-658. 被引量:36
  • 3何延青,吴永强,闻建平.生物柴油生产及其副产物甘油的有效利用[J].中国油脂,2007,32(5):47-51. 被引量:27
  • 4潘振良,孙希孟,梁永民.PIDA/PIFA在有机合成中的应用[J].化学试剂,2007,29(2):85-87. 被引量:2
  • 5Kahrama Bozbas. Biodiesel as an alternative motor fuel: Production and policies in the European Union. Renewable and Sustainable Energy Re- views, 2008, (12) :542 -552.
  • 6Chiu, C. W. , Tekeei, A. , Ronco, J. M. , Banks, M. L. , Suppes, G.J. Reducing. Byproduct. Formation during Conversion of Glycerol to Propylene Glycol. Ind. Eng. Chem. Res., 2008,47 (18): 6878 - 6884.
  • 7Abdullah Alhanash, Elena F Kozhevnikova, Ivan V Kozhevnikov. Hy-drogenolysis of Glycerol to Propanediol Over Ru: Polyoxometalate Bi- functional Catalyst. Catalysis letters, 2008, 120:307 - 311.
  • 8Erin P Maris, Robert J Davis. Hydrogenolysis of glycerol over carbon - supported Ru and Pt catalysts. Journal of Catalysis, 2007, 249 : 328 - 337.
  • 9Mohanprasad A Dasari, Pim- Pahn Kiatsimkul, Willam R Sutterlin, et al. Low - pressure hydrogenolysis of glycerol to propylene glycol. Ap- plied Catalysis A : General, 2005,281:225 - 231.
  • 10Dasari MA, Kiatsimkul PP, Sutterlin WR, Suppes GJ. Low - pressure hydrogenolysis of glycerol to propylene glycol. Applied Catalysis A: General,2005,281 ( 1 -2) :225 -231.

引证文献2

二级引证文献1

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部