TY - JOUR
T1 - Water gas shift membrane reactor for CO2 control in IGCC systems
T2 - Techno-economic feasibility study
AU - Bracht, M.
AU - Alderliesten, P. T.
AU - Kloster, R.
AU - Pruschek, R.
AU - Haupt, G.
AU - Xue, E.
AU - Ross, J. R.H.
AU - Koukou, M. K.
AU - Papayannakos, N.
PY - 1997
Y1 - 1997
N2 - A novel reactor concept, the water gas shift membrane reactor (WGS-MR) for CO2 removal in IGCC systems has been investigated. In order to establish full insight in the possibilities of the application of such a reactor, a multidisciplinary feasibility study has been carried out comprising system integration studies, catalyst research, membrane research, membrane reactor modelling and bench scale membrane reactor experiments. The application of the WGS-MR concept in IGCC systems is an attractive future option for CO2 removal as compared to conventional options. The net efficiency of the IGCC process with integrated WGS-MR is 42.8 % (LHV) with CO2 recovery (80 % based on coal input). This figure has to be compared with 46.7 % (LHV) of an IGCC without CO2 recovery and based on the same components, and with 40.5 % (LHV) of an IGCC with conventional CO2 removal. Moreover, an economic analysis indicates favourable investment and operational costs. The development of the process is considered to be technically feasible. However, it became clear that the technology of inorganic high selective gas separation membrane manufacturing and high temperature ceramic materials engineering is not yet mature and that further development in this area remains necessary.
AB - A novel reactor concept, the water gas shift membrane reactor (WGS-MR) for CO2 removal in IGCC systems has been investigated. In order to establish full insight in the possibilities of the application of such a reactor, a multidisciplinary feasibility study has been carried out comprising system integration studies, catalyst research, membrane research, membrane reactor modelling and bench scale membrane reactor experiments. The application of the WGS-MR concept in IGCC systems is an attractive future option for CO2 removal as compared to conventional options. The net efficiency of the IGCC process with integrated WGS-MR is 42.8 % (LHV) with CO2 recovery (80 % based on coal input). This figure has to be compared with 46.7 % (LHV) of an IGCC without CO2 recovery and based on the same components, and with 40.5 % (LHV) of an IGCC with conventional CO2 removal. Moreover, an economic analysis indicates favourable investment and operational costs. The development of the process is considered to be technically feasible. However, it became clear that the technology of inorganic high selective gas separation membrane manufacturing and high temperature ceramic materials engineering is not yet mature and that further development in this area remains necessary.
KW - Ceramic membranes
KW - CO-removal
KW - Computational fluid dynamics
KW - Cycle calculations
KW - IGCC
KW - Membrane reactor
KW - Membrane reactor model
KW - Power generation
KW - Water gas shift
KW - Water gas shift catalysts
UR - http://www.scopus.com/inward/record.url?scp=0000176718&partnerID=8YFLogxK
U2 - 10.1016/s0196-8904(96)00263-4
DO - 10.1016/s0196-8904(96)00263-4
M3 - Article
AN - SCOPUS:0000176718
SN - 0196-8904
VL - 38
SP - S159-S164
JO - Energy Conversion and Management
JF - Energy Conversion and Management
IS - SUPPL. 1
ER -