Thermochemical conversion of coal and water to CO and H-2 by a two-step redox cycle of ferrite

被引:18
作者
Kodama, T
Miura, S
Shimizu, T
Kitayama, Y
机构
[1] Dept. of Chem. and Chem. Engineering, Faculty of Engineering, Niigata University, Niigata 950-21
关键词
D O I
10.1016/S0360-5442(97)00041-8
中图分类号
O414.1 [热力学];
学科分类号
摘要
Redox systems of iron-based oxides (ferrites) mixed with coal powder have been studied to determine the most reactive and selective working materials for thermochemical conversion of coal and water to CO and H-2. Reactions were performed in a two-step redox cycle in which the ferrites were reacted with coal powder at 900 degrees C to produce CO, H-2, and reduced ferrites (coal-gasification step); these were then reoxidized with water vapor to generate H-2 at 700 degrees C in a separate step (water-decomposition step). Magnetite and Mg(II)-, Mn(II)-, Ni(II)-, Zn(II)-, and In(III)-ferrites have been screened for reactivity and selectivity in the coal-gasification step. The In(III)-ferrite showed the greatest reactivity and selectivity for CO formation from coal at 900 degrees C. The CO-production rate in the coal-In(III)-ferrite reaction was 3.5 times as fast as that in the single-step direct coal-H2O reaction. The metallic phase of alpha-Fe and In, produced by the coal-In(III)-ferrite reaction, was reoxidized to the ferrite phase to generate I-I, in the water-decomposition step at 700 degrees C. The amount of H-2 evolved using In(III)-ferrite was 5 times larger than that using magnetite. The processes were repeated in the temperature range 700-900 degrees C, with the highly efficient net reaction CHtau(coal) + H2O --> CO + (tau/2 + 1)H-2. (C) 1997 Elsevier Science Ltd.
引用
收藏
页码:1019 / 1027
页数:9
相关论文
共 19 条
[1]   ECONOMICAL AND TECHNICAL EVALUATION OF UT-3 THERMOCHEMICAL HYDROGEN-PRODUCTION PROCESS FOR AN INDUSTRIAL-SCALE PLANT [J].
AOCHI, A ;
TADOKORO, T ;
YOSHIDA, K ;
KAMEYAMA, H ;
NOBUE, M ;
YAMAGUCHI, T .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1989, 14 (07) :421-429
[2]   AN ASSESSMENT OF SOLAR HYDROGEN-PRODUCTION USING THE MARK-13 HYBRID PROCESS [J].
BILGEN, E ;
JOELS, RK .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1985, 10 (03) :143-155
[3]  
DEBENI, 1980, INT J HYDROGEN ENERG, V5, P141
[4]  
FLETCHER EA, 1983, ENERGY, V8, P247, DOI [10.1016/0360-5442(83)90100-7, 10.1016/0360-5442(85)90136-7]
[5]  
FLETCHER EA, 1983, J MINNESOTA ACAD SCI, V49, P30
[6]  
HARIG HD, 1992, VDI BER, V984, P169
[7]   DIVERSIFICATION OF FEEDSTOCKS AND PRODUCTS - RECENT TRENDS IN THE DEVELOPMENT OF SOLID FUEL GASIFICATION USING THE TEXACO AND THE HTW PROCESS [J].
KELLER, J .
FUEL PROCESSING TECHNOLOGY, 1990, 24 (1-3) :247-268
[8]   Reactive and selective redox system of Ni(II)-ferrite for a two-step CO and H-2 production cycle from carbon and water [J].
Kodama, T ;
Watanabe, Y ;
Miura, S ;
Sato, M ;
Kitayama, Y .
ENERGY, 1996, 21 (12) :1147-1156
[9]   SYNTHESIS AND CHARACTERIZATION OF ULTRAFINE NICKEL(II)-BEARING FERRITES (NIXFE3-XO4,X=0.14-1.0) [J].
KODAMA, T ;
WADA, Y ;
YAMAMOTO, T ;
TSUJI, M ;
TAMAURA, Y .
JOURNAL OF MATERIALS CHEMISTRY, 1995, 5 (09) :1413-1418
[10]   MODEL-CALCULATIONS ON SOME FEASIBLE 2-STEP WATER SPLITTING PROCESSES [J].
LUNDBERG, M .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1993, 18 (05) :369-376