Deactivation of modified iron oxide materials in the cyclic water gas shift process for CO-free hydrogen production

被引:67
作者
Galvita, Vladimir [1 ]
Hempel, Thomas [2 ]
Lorenz, Heike [3 ]
Rihko-Struckmann, Liisa K. [3 ]
Sundmacher, Kai [1 ,3 ]
机构
[1] Otto VonGuericke Univ Magdegurg, Chair Proc Syst Engn, D-39106 Magdeburg, Germany
[2] Otto VonGuericke Univ Magdegurg, Inst Expt Phys, D-39106 Magdeburg, Germany
[3] Max Planck Inst Dynam Comples Tech Syst, D-39106 Magdeburg, Germany
关键词
D O I
10.1021/ie0708879
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The iron oxide Fe2O3 is a potential oxygen storage material for the production of hydrogen in the cyclic water gas shift (CWGS) reaction. The deactivation of modified iron oxides during repeated reduction and reoxidation cycles was investigated. Sintering was found to be the main reason for deactivation during the CWGS cycles. The influence of CeO2, La2O3, and Ce0.5Zr0.5O2 as promoters in the system was investigated, as well. CeO2- or La2O3-promoted iron oxide deactivated significantly during the progression of the redox cycles due to the solid-solid transformation of oxide structures (CeFeO3 or LaFeO3) which had a lower oxygen capacity. Iron oxide promoted by Ce0.5Zr0.5O2 showed high stability and activity in the CWGS process. The influence of the Fe2O3-Ce0.5Zr0.5O2 oxide composition ratio and the effect of Mo, Cu, and Mg metal additives on the lifetime stability and activity have been declared. A sample containing 80 wt % Fe2O3 gave the highest activity during the reduction and reoxidation cycles compared to the other oxide composition ratios. The Mo species impregnated on Fe2O3-Ce0.5Zr0.5O2 inhibited the interaction between iron oxide particles during the redox cycles and resulted in mitigated sintering of the iron species. The Mo-impregnated sample was stable over 100 redox cycles.
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页码:303 / 310
页数:8
相关论文
共 22 条
[1]   Mechanisms of catalyst deactivation [J].
Bartholomew, CH .
APPLIED CATALYSIS A-GENERAL, 2001, 212 (1-2) :17-60
[2]   A geometrical sintering model (GSM) to predict surface area change [J].
Cho, Kuk ;
Biswas, Pratim .
JOURNAL OF AEROSOL SCIENCE, 2006, 37 (10) :1378-1387
[3]   RH-LOADED CEO2-ZRO2 SOLID-SOLUTIONS AS HIGHLY EFFICIENT OXYGEN EXCHANGERS - DEPENDENCE OF THE REDUCTION BEHAVIOR AND THE OXYGEN STORAGE CAPACITY ON THE STRUCTURAL-PROPERTIES [J].
FORNASIERO, P ;
DIMONTE, R ;
RAO, GR ;
KASPAR, J ;
MERIANI, S ;
TROVARELLI, A ;
GRAZIANI, M .
JOURNAL OF CATALYSIS, 1995, 151 (01) :168-177
[4]   Hydrogen production from methane by steam reforming in a periodically operated two-layer catalytic reactor [J].
Galvita, V ;
Sundmacher, K .
APPLIED CATALYSIS A-GENERAL, 2005, 289 (02) :121-127
[5]   Cyclic water gas shift reactor(CWGS) for carbon monoxide removal from hydrogen feed gas for PEM fuel cells [J].
Galvita, Vladimir ;
Sundmacher, Kai .
CHEMICAL ENGINEERING JOURNAL, 2007, 134 (1-3) :168-174
[6]   Thermal behavior and cation distribution in nanosized Mo-Co ferrite spinels Mo0.5CoyFe2.5-yO4 (0 ≤ y ≤ 1) studied by DTG, FT-IR and DC conductivity [J].
Gillot, B ;
Lorimier, J ;
Bernard, F ;
Nivoix, V ;
Douard, S ;
Tailhades, P .
MATERIALS CHEMISTRY AND PHYSICS, 1999, 61 (03) :199-206
[7]  
GILLOT B, 1993, SOLID STATE IONICS, V620, P63
[8]   Contribution of cerium/zirconium mixed oxides to the activity of a new generation of TWC [J].
González-Velasco, JR ;
Gutiérrez-Ortiz, MA ;
Marc, JL ;
Botas, JA ;
González-Marcos, MP ;
Blanchard, G .
APPLIED CATALYSIS B-ENVIRONMENTAL, 1999, 22 (03) :167-178
[9]   Thermal stability of oxygen storage properties in a mixed CeO2-ZrO2 system [J].
Hori, CE ;
Permana, H ;
Ng, KYS ;
Brenner, A ;
More, K ;
Rahmoeller, KM ;
Belton, D .
APPLIED CATALYSIS B-ENVIRONMENTAL, 1998, 16 (02) :105-117
[10]   Catalyst deactivation: is it predictable? What to do? [J].
Moulijn, JA ;
van Diepen, AE ;
Kapteijn, F .
APPLIED CATALYSIS A-GENERAL, 2001, 212 (1-2) :3-16