CO2 capture study in advanced integrated gasification combined cycle

This paper presents the results of technical and economic studies in order to evaluate, in the French context, the future production cost of electricity from IGCC coal power plants with CO2 capture and the resulting cost per tonne of CO2 avoided. The economic evaluation shows that the total cost of base load electricity produced in France by coal IGCC power plants with CO2 capture could be increased by 39% for ‘classical’ IGCC and 28% for ‘advanced’ IGCC. The cost per tonne of avoided CO2 is lower by 18% in ‘advanced’ IGCC relatively to ‘classical’ IGCC. The approach aimed to be as realistic as possible for the evaluation of the energy penalty due to the integration of CO2 capture in IGCC power plants. Concerning the CO2 capture, six physical and chemical absorption processes were modeled with the Aspen Plus™ software. After a selection based on energy performance three processes were selected and studied in detail: two physical processes based on methanol and Selexol™ solvents, and a chemical process using activated MDEA. For ‘advanced’ IGCC operating at high-pressure, only one physical process is assessed: methanol.

[1]  A. Trejo,et al.  Solubility of carbon dioxide in binary mixtures of N-methylpyrrolidone with alkanolamines , 1992 .

[2]  Chakib Bouallou,et al.  Technico-economic feasibility study of CO2 capture, transport and geo-sequestration: A case study for France , 2005 .

[3]  Henry D. Jacoby,et al.  Future carbon regulations and current investments in alternative coal-fired power plant technologies , 2007 .

[4]  Kunio Arai,et al.  Isothermal vapor-liquid equilibrium data for binary systems at high pressures: carbon dioxide-methanol, carbon dioxide-ethanol, carbon dioxide-1-propanol, methane-ethanol, methane-1-propanol, ethane-ethanol, and ethane-1-propanol systems , 1990 .

[5]  J. Gmehling,et al.  PSRK: A Group Contribution Equation of State Based on UNIFAC , 1991 .

[6]  Giovanni Lozza,et al.  CO2 Emission Abatement in IGCC Power Plants by Semiclosed Cycles: Part A — With Oxygen-Blown Combustion , 1998 .

[7]  M. Aineto,et al.  Thermal expansion of slag and fly ash from coal gasification in IGCC power plant , 2006 .

[8]  Cédric Philibert,et al.  Beyond Kyoto: Energy Dynamics and Climate Stabilisation , 2002 .

[9]  Pilar Coca,et al.  Condensing species from flue gas in Puertollano gasification power plant, Spain , 2006 .

[10]  Eric Croiset,et al.  Technoeconomic evaluation of IGCC power plants for CO2 avoidance , 2006 .

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

[12]  Igor Bulatov,et al.  Techno-economic modelling and cost functions of CO2 capture processes , 2007, Comput. Chem. Eng..

[13]  Amr Henni,et al.  Solubility of carbon dioxide in methyldiethanolamine + methanol + water , 1995 .

[14]  Giovanni Lozza,et al.  CO2 Emission Abatement in IGCC Power Plants by Semiclosed Cycles: Part A—With Oxygen-Blown Combustion , 1999 .

[15]  Giovanni Lozza,et al.  CO2 Emission Abatement in IGCC Power Plants by Semiclosed Cycles: Part B—With Air-Blown Combustion and CO2 Physical Absorption , 1999 .

[16]  R. Pruschek,et al.  Combined cycle power plant with integrated coal gasification, CO shift and CO2 washing , 1995 .

[17]  R. Kobayashi,et al.  Vapor—liquid equilibrium studies for the carbon dioxide—methanol system , 1988 .

[18]  Cathy Descamps Etude de la capture du CO2 [dioxyde de carbone] par absorption physique dans les systèmes de production d'électricité basés sur la gazéification du charbon intégrée à un cycle combiné , 2004 .