CO2 Mitigation in Coal Gasification Cogeneration Systems with Integration of the Shift Reaction, CO2 Absorption and Methanol Production

被引:1
作者
Duan, Yuanyuan [1 ]
Zhang, Jin [1 ]
机构
[1] Tsinghua Univ, Dept Thermal Engn, Key Lab Thermal Sci & Power Engn, Beijing 100084, Peoples R China
关键词
cogeneration system; methanol synthesis; CO2; mitigation; exergy analysis;
D O I
10.1007/s11630-004-0031-6
中图分类号
O414.1 [热力学];
学科分类号
摘要
Cogeneration of electricity and liquid fuel can achieve higher efficiencies than electricity generation alone in Integrated Gasification Combined Cycle (IGCC), and cogeneration systems are also expected to mitigate CO2 emissions. A proposed methanol-electricity cogeneration system was analyzed in this paper using exergy method to evaluate the specified system. A simple cogeneration scheme and a complicated scheme including the shift reaction and CO2 removal were compared. The results show that the complicated scheme consumes more energy, but has a higher methanol synthesis ratio with partial capture of CO2. In those methanol and electricity cogeneration systems, the CO2 mitigation is not merely an additional process that consumes energy and reduces the overall efficiency, but is integrated into the methanol production.
引用
收藏
页码:193 / 198
页数:6
相关论文
共 16 条
[1]   New technology trends for improved IGCC system performance [J].
Anand, AK ;
Cook, CS ;
Corman, JC ;
Smith, AR .
JOURNAL OF ENGINEERING FOR GAS TURBINES AND POWER-TRANSACTIONS OF THE ASME, 1996, 118 (04) :732-736
[2]  
[Anonymous], 1988, EXERGY ANAL ENERGY S
[3]   Thermodynamic and environmental assessment of integrated gasification and methanol synthesis (IGMS) energy systems with CO2 removal [J].
Cau, G ;
Carapellucci, R ;
Cocco, D .
ENERGY CONVERSION AND MANAGEMENT, 1997, 38 :S179-S186
[4]   Shift reactors and physical absorption for low-CO2 emission IGCCs [J].
Chiesa, P ;
Consonni, S .
JOURNAL OF ENGINEERING FOR GAS TURBINES AND POWER-TRANSACTIONS OF THE ASME, 1999, 121 (02) :295-305
[5]   Numerical study on the coal gasification characteristics in an entrained flow coal gasifier [J].
Choi, YC ;
Li, XY ;
Park, TJ ;
Kim, JH ;
Lee, JG .
FUEL, 2001, 80 (15) :2193-2201
[6]   LIQUID-PHASE METHANOL SYNTHESIS - CATALYSTS, MECHANISM, KINETICS, CHEMICAL-EQUILIBRIA, VAPOR - LIQUID EQUILIBRIA, AND MODELING - A REVIEW [J].
CYBULSKI, A .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1994, 36 (04) :557-615
[7]  
Diao J, 2001, CHEM REACT ENG TECH, V17, P10
[8]  
Duan Y, 2002, TSINGHUA SCI TECHNOL, V7, P190
[9]   Study on commercialization of high efficiency IGCC system [J].
Hashimoto, K ;
Abe, T ;
Utsunomiya, M .
JSME INTERNATIONAL JOURNAL SERIES B-FLUIDS AND THERMAL ENGINEERING, 1998, 41 (04) :1061-1066
[10]  
Haupt G, 2003, GREENHOUSE GAS CONTROL TECHNOLOGIES, VOLS I AND II, PROCEEDINGS, P1063