Economic evaluation of pre-combustion CO2-capture in IGCC power plants by porous ceramic membranes

Pre-combustion-carbon-capture is one of the three main routes for the mitigation of CO2-emissions by fossil fueled power plants. Based on the data of a detailed technical evaluation of CO2-capture by porous ceramic membranes (CM) and ceramic membrane reactors (WGSMR) in an Integrated-Gasification-Combined-Cycle (IGCC) power plant this paper focuses on the economic effects of CO2-abatement. First the results of the process simulations are presented briefly. The analysis is based on a comparison with a reference IGCC without CO2-capture (dry syngas cooling, bituminous coal, efficiency of 47.4%). In addition, as a second reference, an IGCC process with CO2 removal based on standard Selexol-scrubbing is taken into account. The most promising technology for CO2-capture by membranes in IGCC applications is the combination of a water gas shift reactor and a H2-selective membrane into one water gas shift membrane reactor. For the WGSRM-case efficiency losses can be limited to about 6%-points (including losses for CO2 compression) for a CO2 separation degree of 90%. This is a severe reduction of the efficiency loss compared to Selexol (10.3% points) or IGCC–CM (8.6% points). The economic evaluation is based on a detailed analysis of investment and operational costs. Parameters like membrane costs and lifetime, costs of CO2-certificates and annual operating hours are taken into account. The purpose of these evaluations is to identify the minimum cost of electricity for the different capture cases for the variation of the boundary conditions. Fixing 90% CO2 separation the analysis identifies clearly that the economic minimum for cost of electricity and maximum thermodynamic efficiencies do not coincide. The cost of electricity for the reference case was 67€/MWh and for the WGSMR integration with 90% CO2 separation 57€/MWh, if certificate costs of 30€/tCO2, membrane costs of 300€/m2 and 8000 operating hours/year are considered. Further studies on the sensitivity of cost of electricity on the technical and commercial boundary conditions will be presented.

[1]  Bernd Meyer,et al.  Constructability study on a German reference IGCC power plant with and without CO2-capture for hard coal and lignite , 2010 .

[2]  Stefano Consonni,et al.  Shift reactors and physical absorption for Low-CO2 emission IGCCs , 1999 .

[3]  Giovanni Lozza,et al.  Thermodynamic analysis of air-blown gasification for IGCC applications , 2011 .

[4]  T. Merkel,et al.  Carbon dioxide capture with membranes at an IGCC power plant , 2012 .

[5]  G. Manzolini,et al.  CO2 capture in Integrated Gasification Combined Cycle with SEWGS – Part B: Economic assessment , 2013 .

[6]  John J. Marano,et al.  Integration of Gas Separation Membranes with IGCC Identifying the right membrane for the right job , 2009 .

[7]  Kevin Charles O'Brien,et al.  Simulation of a Process to Capture CO2 From IGCC Syngas Using a High Temperature PBI Membrane , 2009 .

[8]  Giovanni Lozza,et al.  CO2 Sequestration From IGCC Power Plants by Means of Metallic Membranes , 2005 .

[9]  Wim G. Haije,et al.  Advanced Membrane Reactors for Fuel Decarbonisation in IGCC: H 2 or CO 2 separation? , 2006 .

[10]  Edward S. Rubin,et al.  CO2 control technology effects on IGCC plant performance and cost , 2009 .

[11]  C. Cormos Integrated assessment of IGCC power generation technology with carbon capture and storage (CCS) , 2012 .

[12]  Vladimiros Nikolakis,et al.  A simulation study of the effect of operating and design parameters on the performance of a water gas shift membrane reactor , 2010 .

[13]  Yuichi Fujioka,et al.  Techno-economic evaluation of the coal-based integrated gasification combined cycle with CO2 capture and storage technology , 2009 .

[14]  Mario Amelio,et al.  Integrated gasification gas combined cycle plant with membrane reactors: Technological and economical analysis , 2007 .

[15]  V. Scherer,et al.  Impact of ceramic membranes for CO2 separation on IGCC power plant performance , 2011 .

[16]  Manfred Fischedick,et al.  RECCS : strukturell-ökomisch-ökologischer Vergleich regenerativer Energietechnologien (RE) mit Carbon Capture and Storage (CCS) , 2006 .

[17]  Hartmut Spliethoff,et al.  Modelling of an IGCC plant with carbon capture for 2020 , 2010 .

[18]  C. Bouallou,et al.  Efficiency of an Integrated Gasification Combined Cycle (IGCC) power plant including CO2 removal , 2008 .

[19]  F. Heredia,et al.  Optimal electricity market bidding strategies considering emission allowances , 2012, 2012 9th International Conference on the European Energy Market.

[20]  N. Hewitt,et al.  Techno-economic study of CO2 capture and storage in coal fired oxygen fed entrained flow IGCC power plants , 2008 .

[21]  M. Lieberman The Learning Curve and Pricing in the Chemical Processing Industries , 1984 .

[22]  Will Johnson,et al.  Towards a pilot-scale membrane system for pre-combustion CO2 separation , 2009 .

[23]  J. Franz,et al.  An evaluation of CO2 and H2 selective polymeric membranes for CO2 separation in IGCC processes , 2010 .

[24]  George Skodras,et al.  Energy and capital cost analysis of CO2 capture in coal IGCC processes via gas separation membranes , 2004 .

[25]  May-Britt Hägg,et al.  Techno-economic evaluation of a PVAm CO2-selective membrane in an IGCC power plant with CO2 capture , 2008 .

[26]  Matthias Finkenrath,et al.  Cost and Performance of Carbon Dioxide Capture from Power Generation , 2011 .