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助剂对Ni/Co双金属催化剂上沼气重整制氢的影响 被引量:4

Effects of additives on biogas reforming to hydrogen over NiCo bimetallic catalyst
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摘要 用传统的等体积浸渍法制备了不同助剂掺杂的NiCo/γ-Al2O3双金属催化剂,用V(CH4)/V(CO2)=1的混合气体模拟沼气,考察了助剂对沼气重整制氢催化剂NiCo/γ-Al2O3的催化性能与结构的影响。运用X射线衍射(XRD)、H2程序升温还原(H2-TPR)、BET比表面积与孔结构分析(BET)、热重-差示扫描量热(TG-DSC)、程序升温加氢(TPH)等手段对催化剂进行了表征。结果表明,NiCo/γ-Al2O3催化剂掺杂La2O3、CeO2或CaO后活性较好。CeO2在反应前后发生了晶型转变,ZrO2反应后仍以晶体形式存在,其它助剂以无定形均匀地分散在载体中。除ZrO2外的助剂增强了载体与金属之间的相互作用,使催化剂难以被还原。助剂的添加使催化剂的比表面积、孔容都有所减少,却明显改善了催化剂的抗积炭性能,其中La2O3与CeO2是较好的助剂。 NiCo/γ-Al2O3 bimetallic catalysts doped with different additives were prepared by conventional incipient wetness impregnation.The experimental biogas was simulated with a gas composed of equal volumes of CH4 and CO2.Effects of additives on the performance and physicochemical properties of NiCo/γ-Al2O3 catalyst were investigated.The catalysts were characterized by XRD,H2-TPR,BET,TG-DSC and TPH.Results showed that doped La2O3,CeO2 or CaO improved the activity of NiCo/γ-Al2O3 catalyst.Crystal CeO2 was changed into amorphous after reaction,but crystal ZrO2 did not change.Other additives dispersed evenly in support by the amorphous form.All additives but ZrO2 enhanced the interaction between metal and support,which made the catalysts more difficult to be reduced.The addition of additives decreased the BET specific surface area and pore volume of the catalysts,but improved obviously anti-coking performance.La2O3 and CeO2 were better additives.
作者 徐军科
出处 《天然气化工—C1化学与化工》 CAS CSCD 北大核心 2010年第6期38-44,共7页 Natural Gas Chemical Industry
基金 科技部国际合作重点项目(2007DFC61690) 同济大学汉高基金教席(081591)
关键词 双金属催化剂 沼气重整 制氢 助剂 nickel cobalt bimetallic catalyst biogas reforming hydrogen production additive
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参考文献26

  • 1Harasimowicz M,Orhk P,Zakrzewska-Trznadel G,et al.Application of polyimide membranes for biogas purification and enrichment[J].J Hazard Mater,2007,144(3):698-702.
  • 2Yanherle J,Membrez Y.Biogas as a fuel source for SOFC co-generators[J].J Power Sources,2004,127(1-2):300-312.
  • 3Themelis N J,Ulloa P A.Methane generation in landfills[J].Renewable Energy,2007,32(7):1243-1257.
  • 4Turner J,Sverdrupy G,Mann M K,et al.Renewable hydrogen production[J].Int J Energy Res,2008,32(5):379-407.
  • 5Pinilla J L,Moliner R,Suelves I,et al.Production of hydrogen and carbon nanofibers by thermal decomposition of methane using metal catalysts in a fluidized bed reactar[J].Int J Hydrogen Energy,2007,32(18):4821-4829.
  • 6Lombardi L,Camevale E,Corti A.Greenhouse effect reduction and energy recovery from waste landfill[J].Energy,2006,31(15):3208-3219.
  • 7Zhang Z G,Xu G W,Chen X,et al.Process development of hydrogenous gas production for PEFC from biogas[J].Fuel Process Technol.2004,85(8-10):1213-229.
  • 8Benito M,García S,Ferreira-Aparicio P,et al.Development of biogas reforming Ni-La-Al catalysts for fuel cells[J].J Power Sources,2007,169(1):177-183.
  • 9Kolbitsch P,Pfeifer C,Hofbaner H.Catalytic steam reforming of model biogas[J].Fuel,2008,87(6):701-706.
  • 10Duerr M,Galr S,Cmden A,et al.Hydrogen and electrical energy from organic waste treatment[J].Int J Hydrogen Energy,2007,32(6):705-709.

二级参考文献125

  • 1余长春,丁雪加,沈师孔.CO_2与CH_4催化反应合成气研究[J].分子催化,1993,7(2):151-155. 被引量:21
  • 2崔月华,徐恒泳,葛庆杰,毕亚东,王玉忠,侯守福,李文钊.Ni/La_2O_3/α-Al_2O_3中的高温脱附氢促进CH_4/CO_2重整反应的初活性[J].催化学报,2006,27(8):659-663. 被引量:7
  • 3阎子峰,薛锦珍,沈师孔,王弘立.担载型铂催化剂上甲烷活化的TPSR研究[J].催化学报,1997,18(1):9-12. 被引量:5
  • 4Gonzalez, O.; Lujano, J.; Pietri, E.; Goldwasser, M. R. Catal. Today, 2005, 107-108:436
  • 5Jing, Q. S.; Lou, H.; Mo, L. Y.; Fei, J. H.; Zhertg, X. M. J. Mol, Catal. A-Chem., 2004, 212(1-2): 211
  • 6Xu, Z.; Li, Y. M.; Zhang, J.Y.; Chang, L.; Zhou, R. Q.; Duan, Z. T. Appl. Catal. A, 2001, 213(1): 65
  • 7Goldwasser, M. R.; Rivas, M. E.; Pietri, E.; Perez-Zurita, M. J.; Cubeiro, M. L.; Gingembre, L.; Leclercq, L.; Leclercq, G. Appl. Catal. A, 2003, 255(1-2): 45
  • 8Hou, Z. Y.; Yokota, O.; Tanaka, T.; Yashima, T. Appl. Catal. A, 2003, 253(2): 381
  • 9Souza, M. M. V. M.; Claye, L.; Dubois, V.; Perez, C. A. C.; Schmal, M. Appl. Catal. A, 2004, 272(1-2): 133
  • 10Aparicio, L. M. J. Catal., 1997, 165(2): 262

共引文献86

同被引文献52

  • 1徐恒泳,王玉忠,刘淑红,张建,陈亚中,袁立祥,江魁,侯守福,葛庆杰,李文钊,金香兰,李建中,王刚.天然气或液体燃料现场制氢新工艺[J].石油与天然气化工,2004,33(z1):23-28. 被引量:9
  • 2周志军,田晓飞,王萍,李成岳,孙桂大.镍-钨氮化物催化剂的实验研究[J].石油学报(石油加工),2004,20(3):30-36. 被引量:7
  • 3项益智,李小年.Supported Cobalt Molybdenum Bimetallic Nitrides for Ammonia Decomposition[J].Chinese Journal of Chemical Engineering,2005,13(5):696-700. 被引量:6
  • 4张晓阳.甲醇水蒸汽重整制氢催化剂的研究[J].天然气化工—C1化学与化工,2007,32(1):10-13. 被引量:6
  • 5Vasiliadou E S, Heracleous E, Vasalos IA, et all. Ru- based catalysts for glycerol hydrogenolysis[J]. Appl Catal B, 2009, 92(1): 90-99.
  • 6Sarkari R, Anjaneyulu C, Krishna V, et al. Vapor phase synthesis of methylpyrazine using aqueous glycerol and ethylenediamine over ZnCr204 catalyst: Elucidation of reaction mechanism[J].Catal Commun,2011,12:1067-1070.
  • 7Sun W, Liu D Y, Zhu H Y, et d. A new egicient approach to 3-methylindindole: vapor-phase synthesis from aniline and glycerol over Cu-based catalyst[J]. Catal Commun, 2010, 12: 147-150.
  • 8Byrd A J, Pant K K, Gupta R B. Hydrogen production from glycerol by reforming in supercfitical water over Ru/ A1203 catalyst[J]. Fuel, 2008, 87(13-14): 2956-2960.
  • 9Rennard D C, Kruger J S, Schmidt L D. Autothermal catalytic partial oxidation of glycerol to syngas and to non-equilibrium products[J]. ChemSusChem, 2009, 2(1): 89-98.
  • 10Valliyappan T, Ferdous D, Bakhshi N N, et al. Production of hydrogen and syngas via steam gasification of glycerol in a fixed-bed reactor[J].Top Catal, 2008, 49(1-2): 59-67.

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