• DocumentCode
    2106203
  • Title

    Research on the Reactivity of Oxygen Carrier Fe2O3 for Chemical Looping Combustion (CLC)

  • Author

    Dong, Changqing ; Jiang, Jingzhou ; Yang, Yongping ; Zhang, Junjiao ; Shan, Liang

  • Author_Institution
    Nat. Eng. Lab. for Biomass Power Generation Equip., North China Electr. Power Univ., Beijing, China
  • fYear
    2010
  • fDate
    28-31 March 2010
  • Firstpage
    1
  • Lastpage
    4
  • Abstract
    Chemical looping combustion (CLC) was a promising combustion technology with inherent separation of CO2. In this paper, thermodynamic equilibrium approach was used to investigate the reactions between CO or biomass gas and oxygen carrier Fe2O3, and experiments were carried out in a laboratory fluidized bed reactor. The results showed that when temperature was below 1000 K, the carbon deposition on oxygen carrier was serious. When CO was used as fuel, the highest gas yield of CO to carbon dioxide reached to 99.5% at 1153 K. And when biomass gas was used as fuel, the highest gas yield of biomass gas to carbon dioxide was almost 75% at 1113 K.
  • Keywords
    chemical reactors; combustion; fluidised beds; fuel gasification; iron compounds; thermodynamics; Fe2O3; biomass gas; carbon deposition; chemical looping combustion; laboratory fluidized bed reactor; oxygen carrier reactivity; thermodynamic equilibrium approach; Biomass; Carbon dioxide; Chemical technology; Combustion; Fluidization; Fuels; Iron; Laboratories; Oxygen; Thermodynamics;
  • fLanguage
    English
  • Publisher
    ieee
  • Conference_Titel
    Power and Energy Engineering Conference (APPEEC), 2010 Asia-Pacific
  • Conference_Location
    Chengdu
  • Print_ISBN
    978-1-4244-4812-8
  • Electronic_ISBN
    978-1-4244-4813-5
  • Type

    conf

  • DOI
    10.1109/APPEEC.2010.5448948
  • Filename
    5448948