欢迎登录材料期刊网

材料期刊网

高级检索

采用等体积浸渍法制备了不同助剂(Fe,Mg,Mn和Ce)修饰的镍-凹凸棒石粘土基催化剂(Ni/PG),并用于催化裂解生物质气化焦油反应.采用X射线衍射和透射电子显微镜对Ni/PG催化剂进行了表征,并用总碳分析仪测定了催化剂上的积炭.结果表明,助剂的种类及其含量对催化剂性能的影响显著,在所选用的助剂中,Fe助剂入最有利于提高Ni/PG催化剂上焦油的去除率和H_2的收率,且随助剂Fe含量的增加,催化剂活性逐渐提高.

The palygorskite-supported nickel (Ni/PG) catalysts were modified by loading with several additives (Fe, Mg, Mn, and Ce) by incipient wetness impregnation. The effect of the additives and their content on the catalytic activity of Ni/PG and H_2 yield in tar cracking was investigated. The catalysts were characterized by X-ray diffraction and transmission electron microscopy. The content of the additives affected the catalyst activity and the selectivity in tar cracking. Fe was the best species for promoting the performance of Ni/PG both in tar conversion and H_2 yield. Increasing the Fe loading amount over the Ni/PG catalyst was favorable for tar removal.

参考文献

[1] Li C S;Suzuki K .[J].Renewable & Sustainable Energy Reviews,2009,13:594.
[2] Li C S;Hirabayashi D;Suzuki K .[J].BIORESOURCE TECHNOLOGY,2010,101:S97.
[3] Park H J;Park S H;Sohn J M;Park J Jeon J K Kim S S Park Y K .[J].BIORESOURCE TECHNOLOGY,2010,101:S101.
[4] Polychronopoulou K;Fierro JLG;Efstathiou AM .The phenol steam reforming reaction over MgO-based supported Rh catalysts[J].Journal of Catalysis,2004(2):417-432.
[5] Ishihara A;Qian E W;Finahari I N;Sutrisna I P Kabe T .[J].FUEL,2005,84:1462.
[6] Nakamura K;Miyazawa T;Sakurai T;Miyao T Naito S Begum N Kunimori K Tomishige K .[J].Applied Catalysis B:Environmental,2009,86:36.
[7] Uddin M A;Tsuda H;Wu S J;Sasaoka E .[J].FUEL,2008,87:451.
[8] Sato K;Fujimoto K .[J].Catalysis Communications,2007,8:1697.
[9] Furusawaa T;Tsutsumi A .[J].Applied Catalysis A:General,2005,278:207.
[10] Polychronopoulou K;Bakandfitsos A;Tzitzios V Fierro J L G;Efstathiou A M .[J].Journal of Catalysis,2006,241:132.
[11] Gluhoi A C;Bogdanchikova N;Nieuwenhuys B E .[J].Journal of Catalysis,2005,229:154.
[12] 余林,袁书华,田久英,王升,储伟.甲烷部分氧化制合成气 载体及助剂对Ni系催化剂活性的影响[J].催化学报,2001(04):383-386.
[13] 季亚英,李文钊,徐恒泳,陈燕馨.流化床甲烷部分氧化制合成气Ni催化剂及助剂La的作用[J].分子催化,2001(01):37-41.
[14] 王海涛,李振花,田树勋,何菲.助剂对甲烷部分氧化制合成气镍基催化剂性能的影响[J].燃料化学学报,2004(04):475-480.
[15] 杨咏来,徐恒泳,李文钊.CeO2和Pd在Ni/γ-Al2O3催化剂中的助剂作用[J].物理化学学报,2002(04):321-325.
[16] Wang S B;Lu G Q .[J].Applied Catalysis B:Environmental,1998,19:267.
[17] 于建华,袁红艳,徐绍平,杨小芹,刘淑琴.Ni-Fe/坡缕石催化水蒸气重整杏核热解焦油制氢[J].西安交通大学学报,2008(08):1049-1053.
[18] 石莹 .[D].合肥:合肥工业大学,2009.
[19] Simell P;Stahlberg P;Kurkela E;Albrecht J;Deutsch S;Sjostrom K;Beenackers AACM (ed.);Maniati .Provisional protocol for the sampling and analysis of tar and particulates in the gas from large-scale biomass gasifiers. Version 1998.[J].Biomass & Bioenergy,2000(1):19-38.
[20] 王卫平,席靖宇,王志飞,吕功煊,赵普.Ni-Fe催化剂乙醇部分氧化制氢的研究[J].物理化学学报,2002(05):426-431.
[21] 陈天虎,王健,庆承松,彭书传,宋垠先,郭燕.热处理对凹凸棒石结构、形貌和表面性质的影响[J].硅酸盐学报,2006(11):1406-1410.
[22] 张保才,李勇,蔡伟杰,唐晓兰,徐奕德,申文杰.Ni-Cu/CeO2催化剂上乙醇水蒸气重整反应[J].催化学报,2006(07):567-572.
[23] 甄开吉;王国甲;毕颖丽;李荣生,阚秋斌.催化作用基础[M].北京:科学出版社,2005:17.
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%