Oxygen transport capacity and kinetic study of ilmenite ores for methane chemical-looping combustion

被引:32
作者
Khakpoor, Nima [1 ]
Mostafavi, Ehsan [1 ]
Mahinpey, Nader [1 ]
Siegler, Hector De la Hoz [1 ]
机构
[1] Univ Calgary, Dept Chem & Petr Engn, 2500 Univ Dr NW, Calgary, AB T2N 1N4, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Chemical-looping combustion; CO2; capture; Grain model; Cyclic redox operation; Ilmenite; CO2; CAPTURE; REDOX CYCLES; CARRIERS; PERFORMANCE; TECHNOLOGY;
D O I
10.1016/j.energy.2018.12.056
中图分类号
O414.1 [热力学];
学科分类号
摘要
Reactivity and oxygen-transport capacity of Canadian and commercial ilmenite ores in the chemical looping combustion of methane were investigated in a thermogravimetric analyzer (TGA). Oxygen carrier performance was evaluated over multiple cycles during which Canadian ilmenite oxygen transport capacity increased from 2.7% to 14.2% and the commercial sample maintained an approximately constant oxygen transport capacity at 4.5%. XRD and SEM results indicate that new phases were formed, and surface morphology was transformed significantly during cyclic operations. Studies on carbon deposition on the ilmenite surface indicate that lower methane partial pressure and reduction temperatures are favorable to effectively prevent this phenomenon. The kinetic grain model (GM) was found satisfactorily to fit reduction rate data obtained at atmospheric pressure. Intrinsic reaction rates and kinetic parameters were assessed, accordingly. Activation energy were estimated 106.7 +/- 10.6 kJ/mol and 95.0 8.5 kJ/ mol for the Canadian and commercial samples, respectively. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:329 / 337
页数:9
相关论文
共 26 条
[1]   Kinetics of redox reactions of ilmenite for chemical-looping combustion [J].
Abad, Alberto ;
Adanez, Juan ;
Cuadrat, Ana ;
Garcia-Labiano, Francisco ;
Gayan, Pilar ;
de Diego, Luis F. .
CHEMICAL ENGINEERING SCIENCE, 2011, 66 (04) :689-702
[2]   Ilmenite Activation during Consecutive Redox Cycles in Chemical-Looping Combustion [J].
Adanez, Juan ;
Cuadrat, Ana ;
Abad, Alberto ;
Gayan, Pilar ;
de Diego, Luis F. ;
Garcia-Labiano, Francisco .
ENERGY & FUELS, 2010, 24 (02) :1402-1413
[3]   Exergy analysis of chemical-looping combustion systems [J].
Anheden, M ;
Svedberg, G .
ENERGY CONVERSION AND MANAGEMENT, 1998, 39 (16-18) :1967-1980
[4]   Sulfation phenomena in fluidized bed combustion systems [J].
Anthony, EJ ;
Granatstein, DL .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2001, 27 (02) :215-236
[5]   Carbon capture by physical adsorption: Materials, experimental investigations and numerical modeling and simulations - A review [J].
Ben-Mansour, R. ;
Habib, M. A. ;
Bamidele, O. E. ;
Basha, M. ;
Qasem, N. A. A. ;
Peedikakkal, A. ;
Laoui, T. ;
Ali, M. .
APPLIED ENERGY, 2016, 161 :225-255
[6]   Oxy-fuel combustion technology for coal-fired power generation [J].
Buhre, BJP ;
Elliott, LK ;
Sheng, CD ;
Gupta, RP ;
Wall, TF .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2005, 31 (04) :283-307
[7]   A commentary on "The greenhouse-gas footprint of natural gas in shale formations" by RW Howarth, R. Santoro, and Anthony Ingraffea [J].
Cathles, Lawrence M., III ;
Brown, Larry ;
Taam, Milton ;
Hunter, Andrew .
CLIMATIC CHANGE, 2012, 113 (02) :525-535
[8]   Chemically and physically robust, commercially-viable iron-based composite oxygen carriers sustainable over 3000 redox cycles at high temperatures for chemical looping applications [J].
Chung, Cheng ;
Qin, Lang ;
Shah, Vedant ;
Fan, Liang-Shih .
ENERGY & ENVIRONMENTAL SCIENCE, 2017, 10 (11) :2318-2323
[9]   Chemical looping combustion process in fixed-bed reactors using ilmenite as oxygen carrier: Conceptual design and operation strategy [J].
Fernandez, J. R. ;
Alarcon, J. M. .
CHEMICAL ENGINEERING JOURNAL, 2015, 264 :797-806
[10]   Amine degradation in CO2 capture. I. A review [J].
Gouedard, C. ;
Picq, D. ;
Launay, F. ;
Carrette, P. -L. .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2012, 10 :244-270