• Title of article

    Tar and CO2 removal from simulated producer gas with activated carbon and charcoal

  • Author/Authors

    Acharya، نويسنده , , Chethan K. and Jiang، نويسنده , , Fengchun and Liao، نويسنده , , Chang-hsien and Fitzgerald، نويسنده , , Patrick and Vecchio، نويسنده , , Kenneth S. and Cattolica، نويسنده , , Robert J.، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2013
  • Pages
    8
  • From page
    201
  • To page
    208
  • Abstract
    Steam gasification of biomass produces gases such as CO, CO2, H2, CH4, H2O, C2–C5 hydrocarbons, tars (aromatic hydrocarbons), NH3, HCN, and H2S, which are commonly known as producer gas. To produce liquid fuel, CO2 and tars have to be removed from the producer gas. The CO2 can be converted into a useful product such as CO using the reverse Boudouard reaction (CO2 + C ↔ 2CO). Tars can be removed in the presence of carbon by adsorption. Using simulated producer gas flow, reactor studies (200 °C–950 °C) of the reverse Boudouard reaction and the adsorption of toluene and ethylene, tar surrogates, were conducted with different commercially activated carbon and mesquite charcoal. The study showed that the reverse Boudouard reaction is limited by kinetics. The concentration of CO from the reverse Boudouard reaction approaches equilibrium with increase in temperature and residence time. The adsorption of the tar surrogate toluene in the presence of carbon at lower temperature of 200 °C–300 °C is a useful removal mechanism.
  • Keywords
    Reverse Boudouard reaction , carbon , Producer gas , Tars , Reforming , Empirical Models
  • Journal title
    Fuel Processing Technology
  • Serial Year
    2013
  • Journal title
    Fuel Processing Technology
  • Record number

    1509433