Techno-economic evaluation of advanced IGCC lignite coal fuelled power plants with CO2 capture

被引:44
作者
Mondol, Jayanta Deb [1 ]
McIlveen-Wright, David [1 ]
Rezvani, Sina [1 ]
Huang, Ye [1 ]
Hewitt, Neil [1 ]
机构
[1] Univ Ulster, Ctr Sustainable Technol, Sch Built Environm, Coleraine BT37 0QB, Antrim, North Ireland
关键词
Integrated gasification combined cycle (IGCC); CO2 capture and storage (CCS); Techno-economic; Emissions; Power plant; GASIFICATION COMBINED-CYCLE; CARBON-DIOXIDE; ELECTRIC-POWER; CAPITAL-COST; GENERATION; TECHNOLOGIES; PERFORMANCE; SEPARATION; EMISSIONS; HYDROGEN;
D O I
10.1016/j.fuel.2009.04.019
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The techno-economic evaluation of four novel integrated gasification combined cycle (IGCC) power plants fuelled with low rank lignite coal with CO2 capture facility has been investigated using ECLIPSE process simulator. The performance of the proposed plants was compared with two conventional IGCC plants with and without CO2 capture. The proposed plants include an advanced CO2 capturing process based on the Absorption Enhanced Reforming (AER) reaction and the regeneration of sorbent materials avoiding the need for sulphur removal component, shift reactor and/or a high temperature gas cleaning process. The results show that the proposed CO2 capture plants efficiencies were 18.5-21% higher than the conventional IGCC CO2 capture plant. For the proposed plants, the CO2 capture efficiencies were found to be within 95.8-97%. The CO2 capture efficiency for the conventional IGCC plant was 87.7%. The specific investment costs for the proposed plants were between 1207 and 1479 (sic)/kW(e) and 1620 (sic)/kW(e) and 1134 (sic)/kW(e) for the conventional plants with and without CO2 capture respectively. Overall the proposed IGCC plants are cleaner, more efficient and produce electricity at cheaper price than the conventional IGCC process. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2495 / 2506
页数:12
相关论文
共 37 条
[1]   Integrated gasification gas combined cycle plant with membrane reactors: Technological and economical analysis [J].
Amelio, Mario ;
Morrone, Pietropaolo ;
Galucci, Fausto ;
Basile, Angelo .
ENERGY CONVERSION AND MANAGEMENT, 2007, 48 (10) :2680-2693
[2]   Process evaluation of an 865 MWe lignite fired O2/CO2 power plant [J].
Andersson, Klas ;
Johnsson, Filip .
ENERGY CONVERSION AND MANAGEMENT, 2006, 47 (18-19) :3487-3498
[3]  
[Anonymous], 2005, Key World Energy Statistics
[4]   High efficiency electric power generation:: The environmental role [J].
Beer, Janos M. .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2007, 33 (02) :107-134
[5]   High-temperature membranes in power generation with CO2 capture [J].
Bredesen, R ;
Jordal, K ;
Bolland, O .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2004, 43 (09) :1129-1158
[6]   Concept for a competitive coal fired integrated gasification combined cycle power plant [J].
Campbell, PE ;
McMullan, JT ;
Williams, BC .
FUEL, 2000, 79 (09) :1031-1040
[7]   Co-production of hydrogen, electricity and CO2 from coal with commercially ready technology.: PartA:: Performance and emissions [J].
Chiesa, P ;
Consonni, S ;
Kreutz, T ;
Williams, R .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2005, 30 (07) :747-767
[8]  
Christou C, 2008, RENEW SUST ENERG REV, V12, P2459, DOI 10.1016/j.rser.2007.06.010
[9]   A comparison of electricity and hydrogen production systems with CO2 capture and storage.: Part A:: Review and selection of promising conversion and capture technologies [J].
Damen, K ;
van Troost, M ;
Faaij, A ;
Turkenburg, W .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2006, 32 (02) :215-246
[10]   Efficiency of an Integrated Gasification Combined Cycle (IGCC) power plant including CO2 removal [J].
Descamps, C. ;
Bouallou, C. ;
Kanniche, M. .
ENERGY, 2008, 33 (06) :874-881