The redox reaction kinetics of Sinai ore for chemical looping combustion applications

被引:25
作者
Ksepko, Ewelina [1 ]
Babinski, Piotr [1 ]
Nalbandian, Lori [2 ]
机构
[1] Inst Chem Proc Coal, 1 Zamkowa, PL-41803 Zabrze, Poland
[2] Chem Proc & Energy Resources Inst, Ctr Res & Technol Hellas, 6th km Harilaou Thermi Rd,POB 60361, Thermi 57001, Thessaloniki, Greece
关键词
Chemical looping combustion; Kinetics; Sinai ore; Fe-Mn-based ore; Natural OCs; Ilmenite; OXYGEN UNCOUPLING CLOU; FLUIDIZED-BED REACTOR; SYNTHESIS GAS; IRON-ORE; CARRIERS; COAL; OXIDES; OXIDATION; ILMENITE; METHANE;
D O I
10.1016/j.apenergy.2017.01.026
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 objective of this work was to study the use of Sinai ore, a Fe-Mn-based ore from Egypt, as a low-cost oxygen carrier (OC) in Chemical Looping Combustion (CLC). The Sinai ore was selected because it possesses relatively high amounts of iron and manganese oxides. Furthermore, those oxides have low cost, very favorable environmental and thermodynamic properties for the CLC process. The performance of the Sinai ore as an OC in CLC was compared to that of ilmenite (Norway Tellnes mine), the most extensively studied naturally occurring Fe-based mineral. The kinetics of the reduction and oxidation reactions with the two minerals were studied using a thermogravimetric analyzer (TGA). Experiments were conducted under isothermal conditions, with multiple redox cycles, at temperatures between 750 and 950 degrees C. For the reduction and oxidation reactions, different concentrations of CH4 (10-25 vol.%) and O-2 (5-20 vol.%) were applied, respectively. The kinetic parameters, such as the activation energy (E-a), pre-exponential factor (A(0)), and reaction order (n), were determined for the redox reactions. Furthermore, models of the redox reactions were selected by means of a model-fitting method. For the Sinai ore, the D3 model (3-dimensional diffusion) was suitable for modeling reduction reaction kinetics. The calculated E-a was 35.3 kJ/mole, and the reaction order was determined to be approximately 0.76. The best fit for the oxidation reaction was obtained for the R3 model (shrinking core). The oxidation (regeneration) reaction E-a was equal to 16.7 kJ/mole, and the determined reaction order was approximately 0.72. The crystalline phases present, as well as the morphology and inhomogeneities in elemental composition were studied for both materials, fresh as well as after multiple redox cycles, by X-ray Diffraction (XRD) and Scanning Electron Microscopy (SEM) combined with X-ray Microanalysis - Energy Dispersive Spectroscopy (EDS). Structural and morphological changes were detected and correlated to the reaction temperature as well as the reactant compositions and thus the stability of the ores in repetitive CLC cycles was determined. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1258 / 1274
页数:17
相关论文
共 36 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]   Progress in Chemical-Looping Combustion and Reforming technologies [J].
Adanez, Juan ;
Abad, Alberto ;
Garcia-Labiano, Francisco ;
Gayan, Pilar ;
de Diego, Luis F. .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2012, 38 (02) :215-282
[3]   Thermodynamically consistent modeling of redox-stable perovskite oxides for thermochemical energy conversion and storage [J].
Albrecht, Kevin J. ;
Jackson, Gregory S. ;
Braun, Robert J. .
APPLIED ENERGY, 2016, 165 :285-296
[4]   On the evaluation of synthetic and natural ilmenite using syngas as fuel in chemical-looping combustion (CLC) [J].
Azis, Muhammad Mufti ;
Jerndal, Erik ;
Leion, Henrik ;
Mattisson, Tobias ;
Lyngfelt, Anders .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2010, 88 (11A) :1505-1514
[5]   Development of a Co-Ni bimetallic aerogel catalyst for hydrogen production via methane oxidative CO2 reforming in a magnetic assisted fluidized bed [J].
Chen, Lin ;
Zhu, Qingshan ;
Hao, Zhigang ;
Zhang, Tao ;
Xie, Zhaohui .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2010, 35 (16) :8494-8502
[6]   Impregnated CuO/Al2O3 oxygen carriers for chemical-looping combustion:: Avoiding fluidized bed agglomeration [J].
de Diego, LF ;
Gayán, P ;
García-Labiano, F ;
Celaya, J ;
Abad, M ;
Adánez, J .
ENERGY & FUELS, 2005, 19 (05) :1850-1856
[7]  
FAHIM M., 2013, Journal of Minerals and Materials Charaterization and Engineering, V1, P68, DOI [10.4236/jmmce.2013.12013, DOI 10.4236/jmmce.2013.12013]
[8]   Study of inexpensive oxygen carriers for chemical looping combustion [J].
Fossdal, A. ;
Bakken, E. ;
Oye, B. A. ;
Schoning, C. ;
Kaus, I. ;
Mokkelbost, T. ;
Larring, Y. .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2011, 5 (03) :483-488
[9]  
Gaggioli RA, 1983, EFFICIENCY COSTING 2, P71
[10]   Bulk monolithic Ce-Zr-Fe-O/Al2O3 oxygen carriers for a fixed bed scheme of the chemical looping combustion: Reactivity of oxygen carrier [J].
Gu, Zhenhua ;
Li, Kongzhai ;
Wang, Hua ;
Qing, Shan ;
Zhu, Xing ;
Wei, Yonggang ;
Cheng, Xianming ;
Yu, He ;
Cao, Yan .
APPLIED ENERGY, 2016, 163 :19-31