期刊文献+

CeO_2及其含量对Au-Pd/ZnO催化剂甲醇部分氧化制氢性能的影响 被引量:2

Effect of CeO_2 on the performances of CeO_2-ZnO supported Au-Pd catalysts for hydrogen production by methanol partial oxidation
下载PDF
导出
摘要 采用聚合物保护乙醇还原法制备了不同Zn/Ce摩尔比的Au-Pd/ZnO-CeO2催化剂,考察了CeO2掺入量对Au-Pd/ZnO-CeO2催化剂甲醇部分氧化制氢反应性能的影响,并运用XRD、TPR、CH3OH(CO2)-TPD、比表面积测定等技术对催化剂进行了表征。结果表明,CeO2的掺入提高了Au-Pd/ZnO催化剂的活性、氢选择性和稳定性,当n(Zn)/n(Ce)=7/3时催化剂活性最佳,598K甲醇的转化率和氢气选择性分别达到99%和64%,反应20h后催化剂的活性仍保持在95%以上。这归因于在该摩尔比时载体的比表面积最大、活性组分与载体的相互作用最强、催化剂的碱中心和对反应物甲醇的吸附量最大,这些均有利于甲醇部分氧化制氢反应性能的提高。 The Au-Pd/ZnO-CeO2 catalysts with different Zn/Ce ratios were prepared by poly (N-vinyl-2-pyrrolidone)(PVP)-stabilized ethanol reduction method, and the effects of ceria on the catalytic performances of Au-Pd/ZnO-CeO2 catalysts for partial oxidation of methanol were investigated. XRD, TPR, TPD and nitrogen adsorption-desorption were used to characterize the properties of the catalysts. The results showed that the addition of ceria could improve the activity, hydrogen selectivity and stability of the Au-Pd/ ZnO catalysts, and the best catalytic activity (99% methanol conversion) and hydrogen selectivity (64%) were obtained over the catalyst with the Zn/Ce molar ratio of 7:3 at 598 K, and the methanol conversion remained above 95% after 20 hours reaction over this catalyst. The support with the Zn/Ce molar ratio of 7:3 had the largest surface area, the strongest interaction between the active species and the support, and the most alkali sites and absorption of methanol in the catalyst, and all of these were advantageous to the catalytic performance enhancement.
出处 《天然气化工—C1化学与化工》 CAS CSCD 北大核心 2009年第1期30-34,45,共6页 Natural Gas Chemical Industry
基金 江西省教育厅科技项目(GJJ08021) 高等学校博士学科点专项研究基金(20040403001)
关键词 Au-Pd催化剂 CeO2改性 甲醇部分氧化 制氢 Au-Pd catalysts CeO2 promotion methanol partial oxidation hydrogen generation
  • 相关文献

参考文献23

  • 1汪丛伟 潘立卫 袁中山 等.ZnO/Cr2O3/CeO2/ZrO2整体催化剂上甲醇重整的工艺参数分析.中国稀土学报,2004,23(12):31-34.
  • 2Haruta M,Yamada N,Kobayashi T, et al. Gold catalysts prepared by coprecipitation for low-temperature oxidation of hydrogen and of carbon monoxide[J].J Catal,1989,115:301.
  • 3Chang F W,Yu H Y,Roselin L S,et al.Production of hydrogen via partial oxidation of methanol over Au/TiO2 catalysts[J].Appl Catal A,2005,290:138.
  • 4Chang F W,Yu H Y,Roselin L S,et al.Hydrogen production by partial oxidation of methanol oxer gold catalysts supported on TiO2-MO, (M=Fe,Co,Zn)composite [J].Appl Catal A,2006, 302: 157.
  • 5Venezia A M,Liotta L F,Pantaleo G,et al.Activity of SiO2 supported gold-palladium catalysts in CO oxidation [J]. Appl Catal A,2003,251:359.
  • 6Idem R O,Bakhshi N N.Production of hydrogen from methanol over promoted coprecipitated Cu-AI catalysts: the effects of various promoters and catalyst activation methods[J].Ind Eng Chem Res 1995,34:1548.
  • 7Wang G Y, Zhang W X,Lian H Let al.Effect of calcination temperatures and precipitant on the catalytic performance of Au/ZnO catalysts for CO oxidation at ambient temperature and in humid circumstances[J].Appl Catal A,2003,239:1.
  • 8Xiao L H,Sun K P,Xu X LI.Low-temperature catalytic combustion of methane overPd/CeO2 prepared by deposition-precipitation method[J].Catal Commun,2005, 6:796.
  • 9Sheng P Y,Bowmaker G A,Idriss H.The Reactions of Ethanol over Au/CeO2[J].Appl Catal A, 2004,261:171.
  • 10刘源,王哓燕,白雪.氧化铈气凝胶担载的铜催化剂对氢气中一氧化碳选择氧化的催化性能[J].中国稀土学报,2004,22(4):543-546. 被引量:6

二级参考文献17

  • 1陈燕馨 李灿 李文昭.物理化学学报(Wuli Huaxue Xuebao),1992,8:452-452.
  • 2田杨超 伏义路 林培琰.催化学报(Cuihua Xuebao),1994,3:189-189.
  • 3[1]Farrauto R J,Heck R M.Environmental catalysis into 21st century [J].Catal.Today,2000,55(1-2): 179.
  • 4[2]Hasegawa Y,Kusakabe K,Morooka.Selective oxidation of carbon monoxide in hydrogen-rich mixtures by permeation through a platinum-loaded Y-Type zeolite membrane [J].S.J.Membr.Sci.,2001,190(1): 1.
  • 5[3]Korotkikh O,Farrauto R.Selective catalytic oxidation of CO in H2: fuel cell applications [J].Catal.Taday,2000,62(2-3): 249.
  • 6[4]David L T,Onsan Z H.Onboard fuel conversion for hydrogen-fuel-cell-driven vehicles [J].Catal.Rev.Sci.Eng.,2001,43 (1 and 2): 31.
  • 7[5]Wronski Z S.Materials for rechargeable batteries and clean hydrogen energy sources [J].Inter.Mater.Rev.,2001,46(1): 1.
  • 8[6]Hohlein B,Biedermann P,Grube T,et al.Fuel cell power trains for road traffic [J].J.Power Sources,1999,84(2): 203.
  • 9[7]George Avgouuroulos,Theophilos Ioannides.CuO-CeO2 mixed oxide catalysts for the selective oxidation of carbon monoxide in excess hydrogen [J].Catal.Ltetter.2001,73(1): 33.
  • 10[8]In Hyuk Son,Alan M Lane.Promotion of Pt/γAl2O3 by Ce for preferential oxidation of CO in H2 [J].Catal.Lett.,2001,76(3-4): 151.

共引文献49

同被引文献43

  • 1吴平霄.蒙脱石酸活化与微结构变化关系研究[J].现代化工,2005,25(1):36-38. 被引量:8
  • 2邱业君,陈吉祥,张继炎.MgO助剂对甲烷部分氧化Ni/Al_2O_3催化剂结构和性能的影响[J].燃料化学学报,2006,34(4):450-455. 被引量:19
  • 3Agrell J, Hasselbo K, Jansson K, et al. Production of hydrogen by partial oxidation of methanol over Cu/ZnO catalysts prepared by microemulsion technique[J].Appl Catal A, 2001, 211(2): 239-250.
  • 4Alejo L, Lago R, Pena M A. Partial oxidation of methanol to produce hydrogen over Cu-Zn-based catalysts [J]. Appl Catal A, 1997, 162(1-2): 281-297.
  • 5Cubeiro M L, Fierro J L G. Partial oxidation of methanol over supported palladium catalysts[J].Appl Catal A, 1998, 168: 307-322.
  • 6Agrell J, Germani G, Jaras S G, et al. Production of hydrogen by partial oxidation of methanol over ZnO-supported palladium catalysts prepared by microemulsion technique[J]. Appl Catal A, 2003, 242(2): 233-245.
  • 7Chang F W, Lai S C, Roselin L S, et al. Hydrogen production by partial oxidation of methanol over ZnO-promoted Au/Al2O3 catalysts[J].J Mol Catal A, 2008, 282: 129-135.
  • 8Chang F W, Roselin L S, Ou T C, et al. Hydrogen production by partial oxidation of methanol over bimetallic Au-Ru/Fe2O3 catalysts [J]. Appl Catal A, 2008, 334: 147- 155.
  • 9Pawelec B, Venezia A M, Parola V L, et al. AuPd alloy formation in Au-Pd/Al2O3 catalysts and its role on aromatics hydrogenation[J].Appl Surf Sci, 2005, 242: 380-391.
  • 10Hurtado-Juan M A, Yeung C M Y, Tsang S C. A study of co-precipitated bimetallic gold catalysts for water-gas shift reaction[J]. Catal Commun, 2008, 9: 1551-1557.

引证文献2

二级引证文献12

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