期刊文献+

助剂对低温水煤气变换反应Au/α-Fe_2O_3催化剂性能的影响 被引量:5

Effect of promoter on the performance of low-temperature water-gas shift reaction in H_2-rich steam over supported gold catalyst
下载PDF
导出
摘要 采用共沉淀法制备了系列Au/α-Fe2O3-MOx(M=Zr、A l、Mg、Ca、Ba)催化剂,通过N2物理吸附、XRD、H2-TPR和CO2-TPD-MS等手段对催化剂的物化性质进行表征,考察了富氢下低温水煤气变换(WGS)反应中助剂对Au/α-Fe2O3催化剂性能的影响。结果表明,助剂ZrO2能有效提高Au/α-Fe2O3催化剂在富氢气氛下低温WGS反应活性和稳定性,反应温度150℃时CO转化率可达88.45%,且催化剂具有较高的稳定性。研究发现,添加ZrO2助剂能抑制载体晶粒的生长,降低载体晶粒度,提高催化剂的比表面积,改善催化剂的还原性能和表面酸碱度,从而提高催化剂的催化活性和稳定性。 The Au/α-Fe2O3 -MOx catalysts ( M = Zr , Al, Mg, Ca, Ba) prepared by coprecipitation method were characterized by BET , XRD, H2-TPR and CO2-TPD-MS. The catalytic performance for low-temperature watergas shift reaction(WGSR) in H2-rich gas was investigated. It was found that the activity and stability of Au/α- Fe2O3-MOx was strongly dependent on the type of additive. Among the tested samples, the Au/α-Fe2O3 catalyst modified by ZrO2 or Al2O3 showed highest activity and stability. On the contrary, the modification by MgO ,CaO and BaO resulted in an activity decrease. The structure and surface analyses revealed that zirconia added to the the Au/α-Fe2O3 catalyst increased the surface area, decreased crystallite size of support, and limited the growth of the crystallite size of support during the catalytic reaction. The results indicated that addition of the promoter zirconia and alumina, changed the structure and performances of the support and resulted in higher activity and stability.
出处 《燃料化学学报》 EI CAS CSCD 北大核心 2006年第6期712-716,共5页 Journal of Fuel Chemistry and Technology
基金 国家自然科学基金(20271012) 福建省科技计划(2002H026)
关键词 助剂 低温水煤气变换 Au/α-Fe2O3 富氢气氛 additive low temperature water-gas shift reaction Au/α-Fe2O3 H2-rich
  • 相关文献

参考文献5

二级参考文献68

  • 1华金铭,郑起,林性贻,魏可镁.制备参数对Au/Fe_2O_3催化剂水煤气变换性能的影响[J].催化学报,2003,24(12):957-963. 被引量:8
  • 2郝郑平,安立敦,李胜利,王弘立.负载型金催化剂对CO氧化的催化性能(Ⅰ)[J].分子催化,1995,9(3):233-236. 被引量:7
  • 3Andreeva D, Idakiev V, Tabakova T, et al. Low-temperature water-gas shift reaction over Au/CeO2 catalysts [ J ]. Catal Today,2002,72: 51 - 57.
  • 4Qi Fu, Svetlana Kudriavtseva, Hovard Saltsburg, et al. Goldceria catalysts for low-temperature water-gas shift reaction[J]. Chem Eng J ,2003,93:41 - 53.
  • 5Neri G,Visco A M, Galvagno S, et al. Au/iron catalysts:temperature programmed reduction and X-ray diffraction characterization[ J]. Thermochimica Acta, 1999,329:39 - 46.
  • 6Donka Andreeva, Vasko Idakiev, Tatjana Tabakova, et al.Low-temperature water-gas shift reaction on Au/α-Fe2O3catalyst [ J ]. Appl Catal A, 1996,134: 275 - 283.
  • 7Donka Andreeva, Tatjana Tabakova, Vasko Idakiev, et al.Au/α-Fe2O3 catalyst for water-gas shift reaction prepared by deposition-precipitation [ J ]. Appl Catal A, 1998, 169:9- 14.
  • 8Costello C K,Kung M C,Oh H-S,et al. Nature of the active site for CO oxidation on highly active Au/γ-A12O3 [J ]. Appl Catal A:General,2002,232:159 - 168.
  • 9Tatyana Tabakova, Vosko Idakiev, Donka Andreeva, et al.Influence of the microscopic properties of the support on the catalytic activity of Au/ZnO, Au/ZrO2, Au/Fe2O3, Au/Fe2O3-ZnO, Au/Fe2O3-ZrO2 catalysts for WGS reaction[J]. Appl Catal A,2000,202:91 - 97.
  • 10Bond G C, Thompson D T. Catal Rev-Sci Eng, 1999, 41(3/4) : 319.

共引文献49

同被引文献96

引证文献5

二级引证文献11

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