Ceria as a catalyst for hydrogen iodide decomposition in sulfur-iodine cycle for hydrogen production

被引:31
作者
Zhang, Yanwei [1 ]
Wang, Zhihua [1 ]
Zhou, Junhu [1 ]
Cen, Kefa [1 ]
机构
[1] Zhejiang Univ, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Zhejiang, Peoples R China
基金
国家高技术研究发展计划(863计划); 美国国家科学基金会;
关键词
SI thermochemical cycle; Hydrogen production; Hydrogen iodide; Ceria; THERMOCHEMICAL CYCLE; PARTIAL OXIDATION; MEMBRANE REACTOR; SILICA MEMBRANE; SURFACE-AREA; EFFICIENCY; KINETICS; METHANE; MODEL; GAS;
D O I
10.1016/j.ijhydene.2008.11.089
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
In this work, ceria (CeO2) prepared with different methods and at various calcination temperatures have been tested to evaluate their effect on hydrogen iodide (HI) decomposition in sulfur-iodine (SI) cycle at various temperatures. The CeO2 catalysts' strongly enhance the HI decomposition by comparison with blank test, especially gel CeO2 300. TG-FTIR, BET, XRD, TEM and TPR were performed for catalysts' characterization. The results show that the CeO2 catalyst synthesized by citric-aided sol-gel method and calcined at low temperature (<500 degrees C) shows more lattice defects, smaller crystallites, larger surface area and better reducibility. oxygen can promote the significantly rapid surface reaction, but simultaneously consume hydrogen species (H) contained in HI. Lattice defects, especially the reduced surface sites, i.e., Ce3+ and oxygen vacancy, play the dominant role in surface reactions of HI decomposition. A new reaction mechanism for HI catalytic decomposition over CeO2 catalyst is proposed. (C) 2008 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:1688 / 1695
页数:8
相关论文
共 32 条
[1]   Evaluation of sol-gel methods for the synthesis of doped-ceria environmental catalysis systems - Part II. Catalytic activity and resistance to thermal aging [J].
Agrafiotis, C ;
Tsetsekou, A ;
Stournaras, CJ ;
Julbe, A ;
Dalmazio, L ;
Guizard, C ;
Boretto, G ;
Debenedetti, M ;
Parussa, F .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2001, 34 (02) :149-159
[2]   Gold-vanadia catalysts supported on ceria-alumina for complete benzene oxidation [J].
Andreeva, D ;
Nedyalkova, R ;
Ilieva, L ;
Abrashev, MV .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2004, 52 (03) :157-165
[3]   Effect of SO2 on CO and C3H6 oxidation over CeO2 and Ce0.75Zr0.25O2 [J].
Deshmukh, SS ;
Zhang, MH ;
Kovalchuk, VI ;
d'Itri, JL .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2003, 45 (02) :135-145
[4]   Influence of the oxidative/reductive treatments on the activity of Pt/Ce0.67Zr0.33O2 catalyst [J].
Fan, J ;
Wu, XD ;
Ran, R ;
Weng, DA .
APPLIED SURFACE SCIENCE, 2005, 245 (1-4) :162-171
[5]   Decomposition of hydrogen iodide in the S-I thermochemical cycle over Ni catalyst systems [J].
Favuzza, P. ;
Felici, C. ;
Lanchi, M. ;
Liberatore, R. ;
Mazzocchia, C. V. ;
Spadoni, A. ;
Tarquini, P. ;
Tito, A. C. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2009, 34 (09) :4049-4056
[6]  
Funk JE, 2001, INT J HYDROGEN ENERG, V26, P185, DOI 10.1016/S0360-3199(00)00062-8
[7]   Upper bound and best estimate of the efficiency of the iodine sulphur cycle [J].
Goldstein, S ;
Borgard, JM ;
Vitart, X .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2005, 30 (06) :619-626
[8]   Simulation study on the catalytic decomposition of hydrogen iodide in a membrane reactor with a silica membrane for the thermochemical water-splitting IS process [J].
Hwang, GJ ;
Onuki, K .
JOURNAL OF MEMBRANE SCIENCE, 2001, 194 (02) :207-215
[9]   Decomposition of hydrogen iodide on Pt/C-based catalysts for hydrogen production [J].
Kim, Jung-Min ;
Park, Jung-Eun ;
Kim, Young-Ho ;
Kang, Kyoung-Soo ;
Kim, Chang-Hee ;
Park, Chu-Sik ;
Bae, Ki-Kwang .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (19) :4974-4980
[10]   A demonstration study on a closed-cycle hydrogen production by the thermochemical water-splitting iodine-sulfur process [J].
Kubo, S ;
Nakajima, H ;
Kasahara, S ;
Higashi, S ;
Masaki, T ;
Abe, H ;
Onuki, K .
NUCLEAR ENGINEERING AND DESIGN, 2004, 233 (1-3) :347-354