• DocumentCode
    3249134
  • Title

    Catalytic cracking of tar model compound from over different catalysts

  • Author

    Zhang, Kang ; Wu, Zhengshun ; Tang, Ninglu ; Chen, Yifeng

  • Author_Institution
    Chem. Coll., Huazhong Normal Univ., Wuhan, China
  • fYear
    2011
  • fDate
    22-24 April 2011
  • Firstpage
    6493
  • Lastpage
    6497
  • Abstract
    For the purpose of developing a series of novel supported NiO and AgO catalysts for toluene as a model compound of tar from a biomass gasification process, the supported MO/Al2O3 and AgO/Al2O3 catalysts were prepared and characterized. Considerless of the porous structure with some loading of AgO and NiO in catalysts , results showed that the Ni-based catalysts not only had a smaller pore size, but also had a larger specific area. After using a bench-scale catalyst evaluated device to investigate the activity of the catalysts,we got that the toluene removal efficiency reached to 97% for catalytic pyrolysis with 15wt%NiO/Al2O3 catalyst at 800°C. But the activity of AgO/Al2O3 catalyst was poor.
  • Keywords
    catalysis; catalysts; chemical engineering; fuel gasification; organic compounds; pyrolysis; bench-scale catalyst; biomass gasification process; catalytic cracking; catalytic pyrolysis; porous structure; tar model compound; toluene removal efficiency; Aluminum oxide; Biomass; Carbon; Chemistry; Gases; Nickel; X-ray scattering; catalysts; catalytic cracking; toluene;
  • fLanguage
    English
  • Publisher
    ieee
  • Conference_Titel
    Electric Technology and Civil Engineering (ICETCE), 2011 International Conference on
  • Conference_Location
    Lushan
  • Print_ISBN
    978-1-4577-0289-1
  • Type

    conf

  • DOI
    10.1109/ICETCE.2011.5775849
  • Filename
    5775849