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载体对镍基催化剂催化2,4-二硝基甲苯加氢反应的影响 被引量:3

Effects of Support on the Nickel-Based Catalysts for Hydrogenation of 2,4-Dinitrotoluene
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摘要 采用浸渍沉淀法制备了Ni/MgO、Ni/HZSM-5、Ni/硅藻土、Ni/SiO2及Ni/HY催化剂,通过XRD、BET、TPR等分析手段对催化剂进行了表征,并将其应用于2,4-二硝基甲苯液相加氢制2,4-甲苯二胺反应。结果表明,在2.2MPa、90℃、反应原料5g、溶剂300mL、催化剂0.5g的条件下,这5种镍基催化剂催化2,4-二硝基甲苯液相加氢反应按2,4-甲苯二胺的选择性高低的排列顺序为Ni/HY、Ni/硅藻土、Ni/SiO2、Ni/HZSM-5、Ni/MgO,其中Ni/HY催化剂催化活性最高,2,4-二硝基甲苯转化率和2,4-甲苯二胺的选择性分别达到99.94%和99.40%,且在循环使用3次后仍能保持良好的催化活性。 A series Ni-based catalysts of Ni/MgO,Ni/HZSM-5,Ni/diatomite,Ni/SiO2 and Ni/HY were prepared by impregnation-precipitation method and characterized by X-ray diffraction(XRD),nitrogen adsorption-desorption(BET) and temperature-programmed reduction(TPR),and used to catalyze the process of liquid-phase hydrogenation of 2,4-dinitrotoluene to 2,4-tolylenediamine.Under the reaction conditions of 2.2 MPa,90℃,2,4-dinitrotoluene 5 g,solvent 300 mL,catalyst 0.5 g,the five Ni-based catalysts followed the order of Ni/HY,Ni/diatomite,Ni/SiO2,Ni/HZSM-5,Ni/MgO,according to the order from high to low of 2,4-tolylenediamine selectivity in 2,4-dinitrotoluene catalytic hydrogenation.The Ni/HY catalyst showed the highest catalytic activity with 2,4-dinitrotoluene conversion of 99.94% and 2,4-tolylenediamine selectivity of 99.40%.No obvious deactivation of the catalyst was observed after being reused for three times in the reaction.
出处 《石油学报(石油加工)》 EI CAS CSCD 北大核心 2012年第2期231-235,共5页 Acta Petrolei Sinica(Petroleum Processing Section)
基金 国家自然科学基金项目(20961004)资助
关键词 镍基催化剂 2 4-二硝基甲苯 2 4-甲苯二胺 加氢催化 Ni-based catalyst 2 4-dinitrotoluene 2 4-tolylenediamine hydrogenation catalytic
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  • 1房永彬.碳纳米管负载催化剂在对硝基甲苯液相催化加氢中的应用[J].天津化工,2004,18(6):24-26. 被引量:5
  • 2毛从文,蒋新.物质的相间分配对吸附相技术制备Ag/SiO_2反应过程的影响[J].高校化学工程学报,2007,21(2):328-333. 被引量:5
  • 3张晟卯,李健,张春丽,吴志申,张治军.羧基功能化离子液体修饰Pd纳米微粒的制备及结构表征[J].无机化学学报,2007,23(4):729-732. 被引量:6
  • 4KREUTZER M T, KAPTEIJN F, MOULIJN J A. Fast gasliquid-solid reactions in monoliths: A ease study of nitro-aromatic hydrogenation [J]. Catalysis Today, 2005,105 : 421-428.
  • 5MALYALA R V,JAGANATHAN R,CHAUDHARI R V. A trickle-bed reactor model for hydrogenation of 2,4- dinitrotoluene: experimental verification [J]. Chemieal Engineering Science, 1998,53 : 787-805.
  • 6KIRILLOV V A, KUZIN N A, MESCHERYAKOV V D, et al. Catalytic heat-exchanger reactor for strongly exotherrnic reactions [J]. Chemical Engineering Science, 2001, 56 : 381- 386.
  • 7AUERE, GROSS M, PANSTER P, et al. Supported iridium catalysts-a novel catalytic system for the synthesis of toluenediamlne [J]. Catalysis Today, 2001,65 : 31-37.
  • 8TAKASHIO,SHINJI I, MASASHI I. Synthesis and activity of the Pt catalyst supported on CNT [J]. Catalysis Communications, 2007,8:701-706.
  • 9MALYALA R V, CHAUDHARI R V. Hydrogenation of 2,4- dinitrotoluene using a supported Ni catalyst: reaction kinetics and semibateh slurry reactor modeling [J]. Ind Eng Chem Res,1999,38:906-915.
  • 10NERI G, MUSOLINO M G, MILONE C, et al. Mechanism of 2,4-dinitrotoluene hydrogenation over Pd/C [J]. Journal of Molecular Catalysis A: Chemical, 1995,95 : 235-241.

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