Advancements in Development of Chemical-Looping Combustion: A Review

被引:116
作者
He Fang [1 ]
Li Haibin [1 ]
Zhao Zengli [1 ]
机构
[1] Chinese Acad Sci, Guangzhou Inst Energy Convers, Renewable Energy & Gas Hydrate Key Lab, Guangzhou 510640, Peoples R China
基金
中国国家自然科学基金;
关键词
D O I
10.1155/2009/710515
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Chemical-looping combustion (CLC) is a novel combustion technology with inherent separation of greenhouse CO2. Extensive research has been performed on CLC in the last decade with respect to oxygen carrier development, reaction kinetics, reactor design, system efficiencies, and prototype testing. Transition metal oxides, such as Ni, Fe, Cu, and Mn oxides, were reported as reactive species in the oxygen carrier particles. Ni-based oxygen carriers exhibited the best reactivity and stability duringmultiredox cycles. The performance of the oxygen carriers can be improved by changing preparation method or by making mixedoxides. The CLC has been demonstrated successfully in continuously operated prototype reactors based on interconnected fluidizedbed system in the size range of 0.3-50 kW. High fuel conversion rates and almost 100% CO2 capture efficiencies were obtained. The CLC system with two interconnected fluidized-bed reactors was considered the most suitable reactor design. Development of oxygen carriers with excellent reactivity and stability is still one of the challenges for CLC in the near future. Experiences of building and operating the large-scale CLC systems are needed before this technology is used commercially. Chemical-looping reforming (CLR) and chemical-looping hydrogen (CLH) are novel chemical-looping techniques to produce synthesis gas and hydrogen deserving more attention and research. Copyright (C) 2009 He Fang et al.
引用
收藏
页数:16
相关论文
共 99 条
[1]   The use of iron oxide as oxygen carrier in a chemical-looping reactor [J].
Abad, A. ;
Mattisson, T. ;
Lyngfelt, A. ;
Johansson, M. .
FUEL, 2007, 86 (7-8) :1021-1035
[2]   Chemical-looping combustion in a 300 W continuously operating reactor system using a manganese-based oxygen carrier [J].
Abad, A ;
Mattisson, T ;
Lyngfelt, A ;
Rydén, M .
FUEL, 2006, 85 (09) :1174-1185
[3]   Mapping of the range of operational conditions for Cu-, Fe-, and Ni-based oxygen carriers in chemical-looping combustion [J].
Abad, Alberto ;
Adanez, Juan ;
Garcia-Labiano, Francisco ;
de Diego, Luis F. ;
Gayan, Pilar ;
Celaya, Javier .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (1-2) :533-549
[4]   Nickel-copper oxygen carriers to reach zero CO and H2 emissions in chemical-looping combustion [J].
Adánez, J ;
García-Labiano, F ;
de Diego, LF ;
Gayán, P ;
Celaya, J ;
Abad, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (08) :2617-2625
[5]   Selection of oxygen carriers for chemical-looping combustion [J].
Adánez, J ;
de Diego, LF ;
García-Labiano, F ;
Gayán, P ;
Abad, A ;
Palacios, JM .
ENERGY & FUELS, 2004, 18 (02) :371-377
[6]   Chemical looping combustion in a 10 kWth prototype using a CuO/Al2O3 oxygen carrier:: Effect of operating conditions on methane combustion [J].
Adanez, Juan ;
Gayan, Pilar ;
Celaya, Javier ;
de Diego, Luis F. ;
Garcia-Labiano, Francisco ;
Abad, Alberto .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (17) :6075-6080
[7]   Design and operation of a 10 kWth chemical-looping combustor for solid fuels -: Testing with South African coal [J].
Berguerand, Nicolas ;
Lyngfelt, Anders .
FUEL, 2008, 87 (12) :2713-2726
[8]   The use of petroleum coke as fuel in a 10 kWth chemical-looping combustor [J].
Berquerand, Nicolas ;
Lyngfelt, Anders .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2008, 2 (02) :169-179
[9]   Deactivation of iron oxide used in the steam-iron process to produce hydrogen [J].
Bleeker, M. F. ;
Veringa, H. J. ;
Kersten, S. R. A. .
APPLIED CATALYSIS A-GENERAL, 2009, 357 (01) :5-17
[10]   Performance of a NiO-based oxygen carrier for chemical looping combustion and reforming in a 120kW unit [J].
Bolhar-Nordenkampf, Johannes ;
Proell, Tobias ;
Kolbitsch, Philipp ;
Hofbauer, Hermann .
GREENHOUSE GAS CONTROL TECHNOLOGIES 9, 2009, 1 (01) :19-25