Comparative studies on isothermal and non-isothermal reduction of haematite in carbon monoxide atmosphere

被引:12
作者
El-Geassy, A. A. [1 ]
Nasr, M., I [1 ]
El-Raghy, S. M. [2 ]
Hammam, A. A. [1 ]
机构
[1] CMRDI, Helwan, Egypt
[2] Cairo Univ, Fac Engn, Giza, Egypt
关键词
Iron oxide; carbon monoxide; reduction; isothermal; non-isothermal; kinetics and mechanism; IRON-OXIDE REDUCTION; CAO AND/OR MGO; GASEOUS REDUCTION; GAS; MECHANISM; COMPACTS; KINETICS; FE2O3; MODEL;
D O I
10.1080/03019233.2019.1646564
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
Iron ore fines was isothermally and non-isothermally reduced with CO and the total mass loss was continuously recorded. The different phases developed during the reduction process were identified by X-ray diffraction analysis. The structural changes accompanying the reduction reactions were microscopically examined. During the isothermal reduction tests, temperature has a significant effect on the reduction reaction. At a given temperature, the highest rate was obtained at initial stages whereas the minimum rate was observed at the later stages due to the formation of dense iron layer. The activation energy values (Ea) at the early stages was 39.23kJ mol(-1) revealed that the reduction is most likely controlled by a combined effect of gaseous diffusion and interfacial chemical reaction mechanism. At later stages, the Ea values were 54.19 kJ mol-1 indicated that the interfacial chemical reaction is the rate controlling mechanism. Testing of the mathematical formulations derived from the gas-solid reaction model confirmed these controlling mechanisms. The non-isothermal reduction experiments were carried out using different heating rates which showed a considerable effect on the degree of reduction. The reduction conversion continuously increased with rise in temperature. The reduction mechanism was predicted from model free and model fitting. The activation energy values were ranging from 135-40 kJ.mol-1 indicating that gas diffusion is the rate controlling step.
引用
收藏
页码:948 / 957
页数:10
相关论文
共 21 条
[1]  
Bogdandy LV, 2013, The reduction of iron ores: scientific basis and technology
[2]   Kinetic analysis of the iron oxide reduction using hydrogen-carbon monoxide mixtures as reducing agent [J].
Bonalde, A ;
Henriquez, A ;
Manrique, M .
ISIJ INTERNATIONAL, 2005, 45 (09) :1255-1260
[3]   KINETIC PARAMETERS FROM THERMOGRAVIMETRIC DATA [J].
COATS, AW ;
REDFERN, JP .
NATURE, 1964, 201 (491) :68-&
[4]   Influence of doping with CaO and/or MgO on stepwise reduction of pure hematite compacts [J].
El-Geassy, AA .
IRONMAKING & STEELMAKING, 1999, 26 (01) :41-52
[5]  
ELGEASSY AA, 1985, T IRON STEEL I JPN, V25, P1202
[6]   GASEOUS REDUCTION OF FE2O3 COMPACTS AT 600-DEGREES-C TO 1050-DEGREES-C [J].
ELGEASSY, AA .
JOURNAL OF MATERIALS SCIENCE, 1986, 21 (11) :3889-3900
[7]  
ELGEASSY AA, 1977, T IRON STEEL I JPN, V17, P629
[8]   Effect of reducing gas on the volume change during reduction of iron oxide compacts [J].
ElGeassy, AA ;
Nasr, MI ;
Hessien, MM .
ISIJ INTERNATIONAL, 1996, 36 (06) :640-649
[9]   Reduction of CaO and/or MgO-doped Fe2O3, compacts with carbonmonoxide 1173-1473 K [J].
ElGeassy, AA .
ISIJ INTERNATIONAL, 1996, 36 (11) :1344-1353
[10]   SOME REMARKABLE FEATURES IN THE REDUCTION OF IRON-OXIDES [J].
GLEITZER, C .
SOLID STATE IONICS, 1990, 38 (1-2) :133-141