• Title of article

    An experimental study on hydrogen-rich gas production via steam gasification of biomass in a research-scale fluidized bed

  • Author/Authors

    Fremaux، نويسنده , , Sylvain and Beheshti، نويسنده , , Sayyed-Mohsen and Ghassemi، نويسنده , , Hojat and Shahsavan-Markadeh، نويسنده , , Rasoul، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2015
  • Pages
    6
  • From page
    427
  • To page
    432
  • Abstract
    A research scale fluidized-bed reactor has been built and used to study the effect of steam/biomass ratio, time duration of experiments, reactor temperature, and biomass particle size on hydrogen yield and tar content in produced syngas during steam gasification of biomass. Batch experiments were performed with wood residue crushed into three different sizes of 0.5–1 mm (small), 1–2.5 mm (medium), and 2.5–5 mm (large), at reactor temperatures of 700, 800, and 900 °C. As the steam/biomass ratio increases, a decrease in formation of CO, accompanied by an increase in the hydrogen concentration, is observed. As expected, an increase in reactor temperature leads to a significant increase of H2 output and tar reforming. The obtained results show that hydrogen yield increases as time duration of the experiment is increased. It is also found that a reduction in particle diameter leads to a significant improvement in hydrogen yield.
  • Keywords
    Biomass particle size , fluidized bed , Hydrogen production
  • Journal title
    Energy Conversion and Management
  • Serial Year
    2015
  • Journal title
    Energy Conversion and Management
  • Record number

    2339128