Stepwise Solar Methane Reforming and Water-Splitting via Lattice Oxygen Transfer in Iron and Cerium Oxides

被引:26
作者
Chuayboon, Srirat [1 ,2 ]
Abanades, Stephane [1 ]
Rodat, Sylvain [3 ,4 ]
机构
[1] PROMES CNRS, Proc Mat & Solar Energy Lab, 7 Rue Four Solaire, F-66120 Font Romeu, France
[2] King Mongkuts Inst Technol Ladkrabang, Dept Mech Engn, Prince Chumphon Campus, Chumphon 86160, Thailand
[3] Univ Grenoble Alpes, INES, BP 332,50 Ave Lac Leman, F-73375 Le Bourget Du Lac, France
[4] CEA LITEN Lab Syst Solaires Haute Temp LSHT, F-38054 Grenoble, France
关键词
ceria; chemical-looping reforming; concentrated solar energy; iron oxide; syngas; SYNTHESIS GAS; SYNGAS PRODUCTION; HYDROGEN-PRODUCTION; DIRECT CONVERSION; CARBON-DIOXIDE; REDOX CYCLE; REDUCTION; CATALYST; CH4; C-2-HYDROCARBONS;
D O I
10.1002/ente.201900415
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
Chemical-looping reforming of methane (CLRM) involves lattice oxygen transfer in metal oxides. This study aims to compare iron (Fe2O3) and cerium (CeO2) oxides as oxygen carrier materials for isothermal solar-driven stepwise CH4 reforming and H2O splitting. Experiments are conducted in a directly irradiated lab-scale solar reactor heated by concentrated sunlight at 950-1150 degrees C. Using solar energy for process heat reduces the dependence on fossil energy resources and avoids CO2 emissions, while converting solar energy into chemical fuels. The performance of the oxygen carrier materials is compared and evaluated by determining the amount of oxygen transferred, methane conversion, syngas yield, and thermochemical cycling stability. As a result, iron oxide reduction with methane strongly depends on temperature and displays relatively lower reaction rate than CeO2. The reduced iron is not completely reoxidized to Fe3O4 after water-splitting because of low thermal stability resulting in strong sintering and agglomeration, thereby decreasing syngas yield and leading to material deactivation. In contrast, ceria exhibits faster reaction rate and stable syngas yield with H-2/CO molar ratios approaching two over repeated cycles. Stable patterns in the averaged oxygen nonstoichiometry (delta = 0.35-0.38) demonstrate excellent thermal cycling stability. Thus, using Fe2O3 oxygen carrier is not suitable for solar CLRM, but iron oxide reduction with methane can be promising for solar metallurgy aiming at producing both metallic iron and syngas.
引用
收藏
页数:12
相关论文
共 38 条
[1]   Thermochemical hydrogen production from a two-step solar-driven water-splitting cycle based on cerium oxides [J].
Abanades, Stephane ;
Flamant, Gilles .
SOLAR ENERGY, 2006, 80 (12) :1611-1623
[2]  
Abanades S, 2006, ENERGY, V31, P2805, DOI 10.1016/j.energy.2005.11.002
[3]   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
[4]   Syngas production via solar-driven chemical looping methane reforming from redox cycling of ceria porous foam in a volumetric solar reactor [J].
Chuayboon, Srirat ;
Abanades, Stephane ;
Rodat, Sylvain .
CHEMICAL ENGINEERING JOURNAL, 2019, 356 :756-770
[5]   High efficiency solar chemical-looping methane reforming with ceria in a fixed-bed reactor [J].
Fosheim, Jesse R. ;
Hathaway, Brandon J. ;
Davidson, Jane H. .
ENERGY, 2019, 169 :597-612
[6]   Thermochemical CO2 splitting via redox cycling of ceria reticulated foam structures with dual-scale porosities [J].
Furler, Philipp ;
Scheffe, Jonathan ;
Marxer, Daniel ;
Gorbar, Michal ;
Bonk, Alexander ;
Vogt, Ulrich ;
Steinfeld, Aldo .
PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 2014, 16 (22) :10503-10511
[7]   Solar hydrogen production via a two-step thermochemical process based on MgO/Mg redox reactions -: Thermodynamic and kinetic analyses [J].
Galvez, M. E. ;
Frei, A. ;
Albisetti, G. ;
Lunardi, G. ;
Steinfeld, A. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (12) :2880-2890
[8]   The morphological stability and fuel production of commercial fibrous ceria particles for solar thermochemical redox cycling [J].
Gladen, Adam C. ;
Davidson, Jane H. .
SOLAR ENERGY, 2016, 139 :524-532
[9]   Stepwise production of syngas and hydrogen through methane reforming and water splitting by using a cerium oxide redox system [J].
Jeong, Hye Heun ;
Kwak, Jung Hun ;
Han, Gui Young ;
Yoon, Ki June .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2011, 36 (23) :15221-15230
[10]   Oxygen-carrier selection and thermal analysis of the chemical-looping process for hydrogen production [J].
Kang, Kyoung-Soo ;
Kim, Chang-Hee ;
Bae, Ki-Kwang ;
Cho, Won-Chul ;
Kim, Sung-Hyun ;
Park, Chu-Sik .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2010, 35 (22) :12246-12254