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添加剂对α-氧化铝载体性能的影响 被引量:5

Effect of Additive on Properties of α-Alumina Support
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摘要 以三水氧化铝为前体,在前体混合物中加入一定量的黏结剂和不同含量的添加剂,通过挤压成型的方法制备α-氧化铝载体,利用添加剂受热分解释放气体的特点改善α-氧化铝载体的性能,并以α-氧化铝为载体制备了负载型银催化剂。采用XRD、颗粒强度测定仪、压汞仪、TG-DTA等手段研究了添加剂及其加入量对α-氧化铝载体晶型、抗压强度、孔结构、晶相转变温度的影响,利用乙烯环氧化反应评价了银催化剂的性能。实验结果表明,添加剂能抑制焙烧过程中氧化铝颗粒间的烧结团聚、改善α-氧化铝载体的抗压强度及其孔直径尺寸、改变氧化铝α相变温度、提高银催化剂的活性和选择性,通过改变添加剂的含量可进一步优化α-氧化铝载体和银催化剂的性能。 α-Alumina was synthesized from gibbsite precursor with binder and additive through extrusion process, and was used in preparing supported silver catalysts for the epoxidation of ethylene to ethylene oxide. The a-alumina was modified with gases released from the additive by its decomposition. The modified supports were characterized by means of XRD, strength analyzer, mercury penetration method and TG-DTA to investigate the effect of the additive dosage on their performance. The catalytic performances of silver catalysts supported on the supports were evaluated in a micro-reactor. The results show that the addition of the additive can effectively inhibit the aggregation of a-alumina particles, improve the strength of the supports, enlarge their pore diameter and change their phase transition temperature. So the catalytic performances of the silver catalysts were improved. The performances of both a-alumina and silver catalyst can further be optimized by adjusting the additive dosage.
出处 《石油化工》 CAS CSCD 北大核心 2013年第8期849-853,共5页 Petrochemical Technology
关键词 α-氧化铝载体 添加剂 银催化剂 乙烯 环氧化 环氧乙烷 α-alumina support additive silver catalyst ethylene epoxidation ethylene oxide
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  • 1李燕.介孔氧化铝材料的合成和应用研究进展[J].高校理科研究,2011 (14) : 524-526.
  • 2Wang Jiabang, Huang Yameng, Lu Jingjuan, et al. Effectof Binder on the Structure and Mechanical Properties of LightWeight Bubble Alumina Ceramic [j]. Ceram Int, 2012, 38(1): 657 -662.
  • 3Sun Jing, Gao Lian, Li Wei. Colloidal Processing of CarbonNanotube/Alumina Composites [J]. Chem Mater, 2002, 14(12): 5169 - 5172.
  • 4Swarupa T S,Bersillon J L, Gopal K. Removal of Fluoridefrom Drinking Water by Adsorption onto Alum-ImpregnatedActivated Alumina [j]. Sep Purif Technol,2006, 50 (3 ):310-317.
  • 5Buchbinder A M, Ray N A, Lu Junling, et al. Displacementof Hexanol by the Hexanoic Acid Overoxidation Product inAlcohol Oxidation on a Model Supported Palladium Nano-particle Catalyst [J]. J Am Chem Soc,2011, 133(44):17816 - 17823.
  • 6Kalantar N A, Maki-Arvela P, Backman H, et al. Gas-PhaseHydrogenation of Oxylene over Pt/Alumina Catalyst, Acti-vity, and Stereoselectivity [J]. J Catal, 2003 , 218(2):267-279.
  • 7Zhu Z H,Zhu H Y,Wang SB, et al. Preparation and Charac-terization of Copper Catalysts Supported on Mesoporous A1203Nanofibers for N20 Reduction to N2 [J]. Catal Lett, 2003, 91(1/2) : 73-81.
  • 8Mao C F,Albert V M. High Surface Area a-Aluminas. H :Oxidation of Ethylene, Ethylene Oxide, and Acetaldehydeover Silver Dispersed on High Surface Area a-Alumina [J].Appl Catal, A, 1995, 122: 61 -76.
  • 9Onaka M, Oikawa T. Olefin Metathesis over MesoporousAlumina-Supported Rhenium Oxide Catalyst [ J]. Catal Lett,2002,31(8) : 850 - 851.
  • 10Shell Oil Company. Ethylene Oxide Catalyst and Process:US, 5380697 [P]. 1993-01-10.

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