• Title of article

    Bench-scale WGS membrane reactor for CO2 capture with co-production of H2

  • Author/Authors

    Li، نويسنده , , H. and Pieterse، نويسنده , , J.A.Z. and Dijkstra، نويسنده , , J.W. and Boon، نويسنده , , J. and van den Brink، نويسنده , , R.W. and Jansen، نويسنده , , D.، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2012
  • Pages
    5
  • From page
    4139
  • To page
    4143
  • Abstract
    This study investigated the water-gas shift reaction in a bench-scale membrane reactor (M-WGS), where three supported Pd membranes of 44 cm in length and ca. 6 μm in thickness were used, reaching a total membrane surface area of 580.6 cm2. The WGS reaction was studied with the syngas mixture: 4.0% CO, 19.2% CO2, 15.4% H2O, 1.2% CH4 and 60.1% H2, under high temperature/pressure conditions: T = 673 K, pfeed = 20–35 bar(a), pperm = 15 bar(a), mimicking CO2 capture with co-production of H2 in a natural gas fired power plant. High reaction pressure and high permeation of Pd membranes allowed for near complete CO conversion and H2 recovery. Both the membranes and the membrane reactor demonstrated a long-term stability under the investigated conditions, indicating the potential of M-WGS to substitute conventional systems.
  • Keywords
    M-WGS , H2 recovery factor , NGCC , Long–term stability , Bench–scale , WGS membrane reactor
  • Journal title
    International Journal of Hydrogen Energy
  • Serial Year
    2012
  • Journal title
    International Journal of Hydrogen Energy
  • Record number

    1670130