期刊文献+

异丁烯两段催化氧化制甲基丙烯酸催化剂研究 Ⅰ.异丁烯气相氧化制甲基丙烯醛多元复合氧化物催化剂的研究 被引量:4

Catalyst for Isobutene Conversion to Methacrylic Acid by Two-stage Catalytic Oxidation Ⅰ. Study on the Multicomponent Metal Oxide Catalysts for Vapor Phase Oxidation of Isobutene to Methacrolein
在线阅读 下载PDF
导出
摘要 本文报导用于异丁烯(叔丁醇)选择氧化制MAL(甲基丙烯醛)的多元复合氧化物催化剂的研究结果。同共沉淀法制备的催化剂的活性主要决定于其化学组成,同时受到制备条件的影响。最佳催化剂的主要物相组成为PbO3,Bi2MoO3.3、NiMoO4、Sb2O3及a-Fe2O3小颗粒。在355℃,1000~2500h-1空速范围,叔丁醇:水:空气=1:3.3:7(摩尔比)的条件下可获得异丁烯转化率达96%,MAL选择性达89%的结果。 The effect of the chemical composition and preparation method of the multicomponent metal oboes and tile catalytic reaction condition on the catalytic oxidation of isobutene to methacrolein (MAL) were studied. X-ray diffraction (XRD), BET surface area measurement and Mossbauer spectroscopy were used for the catalyst characterization. It is shown that the catalytic activity and selectivity for the oxidation of isobutene to MAL are significantly improved by the addition of W and Cs element into the catalyst, and the ekistance of Bi is beneficial to MAL selectivity. The most active catalyst consists of NiMoO4, Bi2MoO3.3 , Sb2O3, PbO2 and superparamagnetic a-Fe2O3 crystalline phases. Compared to Bi2MoO6 phase Bi2MoO3.3 is more efficient for the reaction. Higher catalytic activity can be correlated to the higher surface area of the catalyst, although no direct proportional relationship is observed. At 355℃, with Me3 COH: H2O: air=1: 3. 3: 7 and space velocity= 1000 ̄2500h-1, 96% conversion and 89% selectivity for MAL is obtained over the catalyst mentioned above.
机构地区 南京大学化学系
出处 《工业催化》 CAS 1994年第1期25-31,共7页 Industrial Catalysis
关键词 异丁烯 甲基丙烯酸 催化剂 氧化 methacrolein multicomponent catalyst co-precipitation
  • 相关文献

共引文献3

同被引文献27

  • 1梁文学,邱学青,欧阳新平,杨东杰.麦草碱木质素磺甲基化反应及性能的研究(英文)[J].四川大学学报(自然科学版),2007,44(1):129-134. 被引量:2
  • 2Deshpand R M, Diwakar M M, Bipasic catalysis for a selective synthesis of methacrolein [J]. Mahajan A N, etal. oxo-mannich tandem Journal of Molecular Catalysis A: Chemical, 2004, 211: 49.
  • 3Legrini O, Oliveros E, Braun A M. Photochemical processes for water treatment [J]. Chem Rev, 1993, 93: 671.
  • 4Nogueira R F P, Trovo A G, Mode D F. Solar photo degradation of dichloroacetic acid and 2, 4-dichloro- phenol using an enhanced photo-fenton process [J]. Chemosphere, 2002, 48 (4):385.
  • 5Wu K Q, Xie Y D, Zhao J C, et al. Photo-fenton degradation of a dye under visible light irradiation [J]. Journal of Molecular Catalysis A: Chemical , 1999, 144(1): 77.
  • 6De Morais J L, Zamora P P. Use of advanced oxidation processes to improve the biodegradability of mature landfill leachates [J]. Journal of Hazaldous Materials B, 2005, 123: 181.
  • 7Carlos A, Teixeiraa S C, Guardani R. Degradation of an amino silicone polymer in a water emulsion by the fenton and the photo chemically enhanced fenton reactions [J]. Chemical Engineering and Processing, 2005, 44: 923.
  • 8Kurt U, Gonull U M T, Avsar Y, et al. Research on treat ability of young landfill leachates by fenton's reaction [M]. Istanbul:ISWA 2002 World Environmental Congress & Exhibition, 2002.
  • 9Hrvoje K, Natalija K, Ana L B, etal. Photo-assisted Fenton type processes for the degradation of phenol: a kinetic study [J]. Journal of Hazardous Materials, 2006, 138(12): 632.
  • 10DuY X, Zhou M H, Lei L C. Kinetic model of 4- CP degradation by fenton/O2 system [J]. Water Research, 2007 , 41(5) : 1121.

引证文献4

二级引证文献8

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