欢迎登录材料期刊网

材料期刊网

高级检索

采用浸渍法制备了不同La掺杂量的Ni-SiO2催化剂,研究了La掺杂量对Ni-SiO2催化剂的Ni活性金属粒径、还原性能、甲烷催化裂解寿命以及反应后生成碳纤维的影响.结果表明:La、Ni物质的量比由0增长至0.3时,Ni-SiO2催化剂的寿命显著提高,而当La、Ni物质的量比由0.3增长至0.6时,催化剂寿命在一定程度上略有降低;La、Ni物质的量比由0增长至0.6时,还原后催化剂Ni金属的平均粒径从26.43nm不断降低至10.57nm.不同La掺杂量Ni-SiO2催化剂甲烷催化裂解过程中Ni金属平均粒径变化趋势明显不同,n(La)∶n(Ni) =0的Ni-SiO2催化剂随反应进行Ni金属平均粒径不断降低,而n(La)∶n(Ni)=0.3的Ni-SiO2催化剂随反应进行Ni金属平均粒径则不断升高.碳纤维形态受掺La掺杂量影响较大,随La、Ni物质的量比由0增长至0.3,反应过程中生成的碳纤维管径变粗,而随La、Ni物质的量比由0.3增长至0.6,碳纤维变短.

参考文献

[1] 王文华,王和义,蒋树斌,杨勇.甲烷催化裂解技术研究进展[J].材料导报,2011(11):116-120.
[2] Takenaka S;Ogihara H;Otsuka K .Structural change of Ni species in Ni/SiO2 catalyst during decomposition of methane[J].Journal of Catalysis,2003,208(01):54.
[3] Sakae Takenaka;Toru Shimizu;Kiyoshi Otsuka .Complete removal of carbon monoxide in hydrogen-rich gas stream through methanation over supported metal catalysts[J].International journal of hydrogen energy,2004(10):1065-1073.
[4] Sakae Takenaka;Emi Kato;Yo Tomikubo;Kiyoshi Otsuka .Structural change of Ni species during the methane decomposition and the subsequent gasification of deposited carbon with CO_2 over supported Ni catalysts[J].Journal of Catalysis,2003(1):176-185.
[5] Reshetenko T V;Avdeeva L B;Ushakov V A et al.Coprecipitated iron-containing catalysts (Fe-Al2O3,Fe-CoAl2O3,Fe-Ni-Al2O3) for methane decomposition at moderate temperatures.Ⅰ.Genesis of calcined and reduced catalysts[J].Applied Catalysis A:General,2004,268(1-2):127.
[6] Otsuka K;Takenaka S;Ohtsuki H .Production of pure hydrogen by cyclic decomposition of methane and oxidative elimination of carbon nanofibers on supported-Ni-based catalysts[J].Applied Catalysis A:General,2004,273(1-2):113.
[7] Sakae Takenaka;Yo Tomikubo;Emi Kato;Kiyoshi Otsuka .Sequential production of H_2 and CO over supported Ni catalysts[J].Fuel,2004(1):47-57.
[8] De Chen;Kjersti o.Christensen;Ester Ochoa-Fernandez;Zhixin Yu;Bard Totdal;Nieves latorre;Antonio Monzon;Anders Holmen .Synthesis of carbon nanofibers:effects of Ni crystal size during methane decomposition[J].Journal of Catalysis,2005(1):82-96.
[9] Takenaka S.;Kobayashi S.;Ogihara H.;Otsuka K. .Ni/SiO2 catalyst effective for methane decomposition into hydrogen and carbon nanofiber[J].Journal of Catalysis,2003(1):79-87.
[10] Avdeeva L B;Goncharova O V;Kochubey D I et al.Coprecipitated Ni-alumina and Ni-Cu-alumina catalysts of methane decomposition and carbon deposition.Ⅱ.Evolution of the catalysts in reaction[J].Applied Catalysis A:General,1996,117(1-2):117.
[11] Beatriz Zapata;Miguel A. Valenzuela;Jorge Palados;Enelio Torres-Garcia .Effect of Ca, Ce or K oxide addition on the activity of Ni/SiO_2 catalysts for the methane decomposition reaction[J].International journal of hydrogen energy,2010(21):12091-12097.
[12] Ni/Ce-MCM-41 mesostructured catalysts for simultaneous production of hydrogen and nanocarbon via methane decomposition[J].International journal of hydrogen energy,2010(8):3509.
[13] Li X C;Wu M;Lai Z H .Studies on nickel based catalysts for carbon dioxide reforming of methane[J].Applied Catalysis A:General,2005,290(1-2):81.
[14] Kiyoshi Otsuka;Hitoshi Ogihara;Sakae Takenaka .Decomposition of methane over Ni catalysts supported on carbon fibers formed from different hydrocarbons[J].Carbon: An International Journal Sponsored by the American Carbon Society,2003(2):223-233.
[15] Zongqing Bai;Haokan Chen;Baoqing Li;Wen Li .Methane decomposition over Ni loaded activated carbon for hydrogen production and the formation of filamentous carbon[J].International journal of hydrogen energy,2007(1):32-37.
[16] Yang R T;Chen J P .Mechanism of carbon filament growth on metal catalysts[J].Journal of Catalysis,1989,115(01):52.
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%