• DocumentCode
    2826140
  • Title

    Nickel-based monolithic catalyst for tar cracking of biomass pyrolysis

  • Author

    Lu Peng Mei ; Lu Min ; Yuan Zhen Hong ; Li Hui Wen ; Xu Jing Liang

  • Author_Institution
    Key Lab. of Renewable Energy & Gas Hydrate, Chinese Acad. of Sci., Guangzhou, China
  • fYear
    2011
  • fDate
    15-17 July 2011
  • Firstpage
    7472
  • Lastpage
    7475
  • Abstract
    To eliminate the tar coming from biomass pyrolysis, a kind of nickel-based monolithic catalyst is prepared in this study. The specific surface area, pore volume is characterized. The effect of different acid treatment time, different nickel loading quantity on its catalytic activity is investigated. The results show that the specific surface area is 156m2/g after acid treatment of 5h. The loading quantity of active component is linear with coating times. The influence of coating times on the gas composition is quite small, and the sum of the content of H2 and CO keeps as high as 90 vol %. After 6h catalytic reaction, the phase structure of catalyst hasn´t any change, and the tar conversion decreased from 87.4 wt % to 81.3wt %. The quantity of the coking is tested to be about 1wt %.
  • Keywords
    catalysts; chemical engineering; coatings; fuel gasification; nickel; pyrolysis; renewable materials; acid treatment; biomass pyrolysis; catalytic activity; coating times; coking; gas composition; nickel based monolithic catalyst; nickel loading quantity; tar conversion; tar cracking; time 5 h; Biological system modeling; Biomass; Carbon; Coatings; Inductors; Loading; Surface treatment; biomass pyrolysis; monolithic; nickel-based; tar;
  • fLanguage
    English
  • Publisher
    ieee
  • Conference_Titel
    Mechanic Automation and Control Engineering (MACE), 2011 Second International Conference on
  • Conference_Location
    Hohhot
  • Print_ISBN
    978-1-4244-9436-1
  • Type

    conf

  • DOI
    10.1109/MACE.2011.5988778
  • Filename
    5988778