期刊文献+

Effect of precipitants on Ni-CeO_2 catalysts prepared by a co-precipitation method for the reverse water-gas shift reaction 被引量:11

Effect of precipitants on Ni-CeO_2 catalysts prepared by a co-precipitation method for the reverse water-gas shift reaction
原文传递
导出
摘要 A series of Ni-CeO2 catalysts were prepared by co-precipitation method with Na2CO3, NaOH, and mixed precipitant (Na2CO3:NaOH; 1:1 ratio) as precipitant, respectively. The effect of the precipitants on the catalytic performance, physical and chemical properties of Ni-CeO2 catalysts was investigated with the aid of X-ray diffraction (XRD), Bmmaner-Emmett-Teller method (BET), Fou- rier-transform infrared spectroscopy (FT-IR), thermogravimetry (TG), and H2-TPR characterizations. The Ni-CeO2 catalysts were exam- ined with respect to their catalytic performance for the reverse water-gas shift reaction, and their catalytic activities were ranked as: Ni-CeO2-CP (Na2CO3:NaOH=I:I)〉Ni-CeO2-CP(Na2CO3)〉Ni-CeO2-CP(NaOH)- Correlating to the characteristic results, it was found that the catalyst prepared by co-precipitation with mixed precipitant (Na2CO3:NaOH; 1:1 ratio) as precipitant hadthe most amount of oxygen vacancies accompanied with highly dispersed Ni particles, which made the corresponding Ni-CeO2-CP(Na2CO3:NaOH=I: 1) catalyst exhibit the highest catalytic activity. While the precipitant of Na2CO3 or NaOH resulted in less or no oxygen vacancies in Ni-CeO2 catalysts. As a result, Ni-CeO2-CP(Na2CO3) and Ni-CeO2-CP(NaOH) catalysts presented poor catalytic performance. A series of Ni-CeO2 catalysts were prepared by co-precipitation method with Na2CO3, NaOH, and mixed precipitant (Na2CO3:NaOH; 1:1 ratio) as precipitant, respectively. The effect of the precipitants on the catalytic performance, physical and chemical properties of Ni-CeO2 catalysts was investigated with the aid of X-ray diffraction (XRD), Bmmaner-Emmett-Teller method (BET), Fou- rier-transform infrared spectroscopy (FT-IR), thermogravimetry (TG), and H2-TPR characterizations. The Ni-CeO2 catalysts were exam- ined with respect to their catalytic performance for the reverse water-gas shift reaction, and their catalytic activities were ranked as: Ni-CeO2-CP (Na2CO3:NaOH=I:I)〉Ni-CeO2-CP(Na2CO3)〉Ni-CeO2-CP(NaOH)- Correlating to the characteristic results, it was found that the catalyst prepared by co-precipitation with mixed precipitant (Na2CO3:NaOH; 1:1 ratio) as precipitant hadthe most amount of oxygen vacancies accompanied with highly dispersed Ni particles, which made the corresponding Ni-CeO2-CP(Na2CO3:NaOH=I: 1) catalyst exhibit the highest catalytic activity. While the precipitant of Na2CO3 or NaOH resulted in less or no oxygen vacancies in Ni-CeO2 catalysts. As a result, Ni-CeO2-CP(Na2CO3) and Ni-CeO2-CP(NaOH) catalysts presented poor catalytic performance.
出处 《Journal of Rare Earths》 SCIE EI CAS CSCD 2013年第10期969-974,共6页 稀土学报(英文版)
基金 Project supported by Natural Science Foundation of Zhejiang Province(Y4110220) Foundation of the Zhejiang Provincial Department of Education(Y200908245) Foundation of the Dinghai Academy of Science and Technology(201006)
关键词 reverse water-gas shift reaction Ni-CeO2 catalyst CO-PRECIPITATION oxygen vacancy PRECIPITANT rare earths reverse water-gas shift reaction Ni-CeO2 catalyst co-precipitation oxygen vacancy precipitant rare earths
  • 相关文献

参考文献3

二级参考文献43

  • 1吴晓东,梁清,翁端.Effect of Manganese Doping on Oxygen Storage Capacity of Ceria-Zirconia Mixed Oxides[J].Journal of Rare Earths,2006,24(5):549-553. 被引量:7
  • 2Xu X D, Moulijn J A. Mitigation of C02 by chemical conversion: Plausible chemical reactions and promising products. Energy Fuels, 1996,10(2): 305.
  • 3Chen C S, Cheng W H, Lin S S. Enhanced activity and sta bility of a Cu/Si02 catalyst for the reverse water gas shift reaction by an iron promoter. Chem. Commun., 2001, (18): 1770.
  • 4Chen C S, Cheng W H. Study on the mechanism of CO formation in reverse water gas shift reaction over Cu/Si02 catalyst by pulse reaction, TPD and TPR. Catal. Lett., 2002,83(3-4): 121.
  • 5Chen C S, Cheng W H, Lin S S. Study of iron-promoted Cu/Si02 catalyst on high temperature reverse water gas shift reaction. Appl. Catal., A, 2004, 257(1): 97.
  • 6Chen C S, Cheng W H, Lin S S. Study of reverse water gas shift reaction by TPD, TPR and C02 hydrogenation over potassium-promoted Cu/Si02 catalyst. Appl. Catal., A,2003, 238(1): 55.
  • 7Stone F, Waller D. Cu-ZnO and Cu-Zn0/Al203 catalysts for the reverse water-gas shift reaction. The effect of the Cu/Zn ratio on precursor characteristics and on the activity of the derived catalysts. Top. Catal., 2003, 22(3-4): 305.
  • 8Wang G C, Nakamura J. Structure sensitivity for forward and reverse water-gas shift reactions on copper surfaces: A DFT study. J. Phys. Chem. Lett., 2010,1(20): 3053.
  • 9Liu C, Cundari T R, Wilson A K. C02 reduction on transition metal (Fe, Co, Ni, and Cu) surfaces: In comparison with homogeneous catalysis. J. Phys. Chem. C, 2012, 116(9): 5681.
  • 10Kim S S, Lee H H, Hong S C. A study on the effect of support's reducibility on the reverse water-gas shift reaction over Pt catalysts. Appl. Catal., A, 2012,423: 100.

共引文献24

同被引文献69

引证文献11

二级引证文献32

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