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
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
Journal title :
International Journal of Hydrogen Energy