期刊文献+

锆铪催化添加剂对PX液相氧化过程的影响 被引量:3

Effect of Zr and Hf Additives on p-Xylene Liquid Phase Oxidation
原文传递
导出
摘要 向对二甲苯(PX)催化氧化体系加入锆铪离子可有效地加速该反应过程.对锆铪离子与Co-Mn-Br催化剂体系的协同催化机理作了简要阐述,并对添加不同浓度下锆铪离子的催化作用进行了动力学实验,考察了添加锆和铪离子对主反应和燃烧副反应的影响,获得了锆铪离子添加剂对PX氧化过程的影响规律.研究发现,在实验所考察的温度与催化剂组成条件下,添加锆铪离子对反应过程中不同阶段的加速效果各不相同,且两种离子对燃烧副反应过程也有不同程度的加速作用. p-Xylene liquid phase oxidation would be accelerated by the addition of zirconium or hafnium ions to the Co/Mn/Br catalyst system. In this paper, the activating catalysis mechanisms of Zr and Hf promoters were presented concisely, and a series of PX oxidation experiments at different Zr and Hf concentrations were carried out. A well-known kinetic model was employed to fit the data and the rate constant for each oxidation step was obtained. The rate constant data show that the effect of Zr and Hf additives on the reaction rate of different stages of PX oxidation is various, and hafnium is more active than zirconium. In the other hand, CO_X productions data illustrate that the burning rate increase with adding Zr and Hf in a different extent.
出处 《分子催化》 EI CAS CSCD 北大核心 2004年第6期436-442,共7页 Journal of Molecular Catalysis(China)
基金 国家自然科学基金项目(20076039).
关键词 锆铪离子 对二甲苯 催化氧化 Co-Mn-Br催化剂 Zr and Hf ions p-Xylene Catalytic oxidation Co-Mn-Br Catalyst
  • 相关文献

参考文献7

  • 1Partenheimer W. Catal. Today[J], 1995, 23:69-158
  • 2Partenheimer W. J. Mol. Catal. A: Chem. [J],2003, 206: 105-119
  • 3Partenheimer W. J. Mol. Catal. A: Chem. [J],2003, 206:131-144
  • 4Belmonte F G, Fjare K A. Partenheimer W. [P].USA Patent 5112992
  • 5Chavan S A, Halligudi S B. J. Mol. Catal. A:Chem. [J], 2000, 161:49-64
  • 6Partenheimer W. r. Mol. Catal. A: Chem. [J],2001, 174: 29-33
  • 7Ariko N G.Kinetics Catal.[J],1992,32:757-761

同被引文献81

  • 1成有为,李希.液相催化氧化降解聚苯乙烯[J].中国环境科学,2004,24(5):542-546. 被引量:2
  • 2唐盛伟,刘长军,吴潘,张全忠,梁斌.工艺操作条件对甲苯液相氧化反应的影响[J].石油化工,2005,34(2):116-121. 被引量:11
  • 3唐盛伟,梁斌,吴潘,张全忠,刘长军.甲苯液相空气氧化过程中苯甲醛生成的影响因素分析[J].四川大学学报(工程科学版),2005,37(5):76-81. 被引量:4
  • 4李希 谢刚.一种生产对苯二甲酸用的鼓泡塔氧化反应装置[P].发明专利,申请号:200310107889 5.2003-10-12.
  • 5Suresh A K, Sharma M, Sridhar T. [J]. lnd, Eng. Chem.Res. , 2000, 39:3958-3997.
  • 6Raghavendrachar P, Ramachandran S.[J]. Ind. Eng. Chem.Res., 1992, 31:453-462.
  • 7Partenheimer W. [J]. Catal. Today, 1995, 23:69-158.
  • 8成有为.[D].杭州:浙江大学,2004.
  • 9Partenheimer W. Production of Polycarboxylic Acids with a Molybdenum Activated Cobalt Catalyst [P]. US4992580, 1991.
  • 10Partenheimer W, Graziano D J. Process for Making Aromatic Polycarboxylic Acids and Oxidation Catalyst System [P].US 5081290, 1992.

引证文献3

二级引证文献16

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