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Gasification kinetics of bulk coke in the CO2/CO/H2/H2O/N2 system simulating the atmosphere in the industrial blast furnace

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【作者】 Min-min SunJian-liang ZhangKe-jiang LiKe GuoZi-ming WangChun-he Jiang

【Author】 Min-min Sun;Jian-liang Zhang;Ke-jiang Li;Ke Guo;Zi-ming Wang;Chun-he Jiang;School of Metallurgical and Ecological Engineering, University of Science and Technology Beijing;School of Chemical Engineering, The University of Queensland;Sinosplendor Engineering & Technology Co., Ltd.;

【通讯作者】 Ke-jiang Li;

【机构】 School of Metallurgical and Ecological Engineering, University of Science and Technology BeijingSchool of Chemical Engineering, The University of QueenslandSinosplendor Engineering & Technology Co., Ltd.

【摘要】 The gasification characteristics and gasification kinetics of coke in complex CO2/CO/H2/H2O/N2 systems similar to the gas system of industrial blast furnace(BF) were studied by the method of isothermal thermogravimetric analysis. The experimental gas compositions and the corresponding temperature were chosen according to data reported for industrial BFs. The gasification behavior of coke was described by the Random Pore Model(RPM), Volumetric Model(VM), and Grain Model(GM). Results showed that the gas composition of the coke gasification zone in BF changes slightly and that the temperature is the most important factor affecting coke gasification. The lower activation energy of coke samples(Coke Reaction Index(CRI)>50) is due to the high Fe2O3 in the ash, lower degree of graphitization, and larger pore structure. In addition, the choice of kinetic model does not differ substantially in describing the gasification mechanism of coke in a BF.

【Abstract】 The gasification characteristics and gasification kinetics of coke in complex CO2/CO/H2/H2O/N2 systems similar to the gas system of industrial blast furnace(BF) were studied by the method of isothermal thermogravimetric analysis. The experimental gas compositions and the corresponding temperature were chosen according to data reported for industrial BFs. The gasification behavior of coke was described by the Random Pore Model(RPM), Volumetric Model(VM), and Grain Model(GM). Results showed that the gas composition of the coke gasification zone in BF changes slightly and that the temperature is the most important factor affecting coke gasification. The lower activation energy of coke samples(Coke Reaction Index(CRI)>50) is due to the high Fe2O3 in the ash, lower degree of graphitization, and larger pore structure. In addition, the choice of kinetic model does not differ substantially in describing the gasification mechanism of coke in a BF.

【关键词】 blast furnacecokegasification kineticsgas system
【Key words】 blast furnacecokegasification kineticsgas system
【基金】 financially supported by the National Key Research and Development Program of China (Nos. 2017YFB0304300 and 2017YFB0304303);the National Science Foundation of China (No. 51774032);the Chinese Fundamental Research Funds for the Central Universities (No. FRF-TP-17-086A1)
  • 【文献出处】 International Journal of Minerals Metallurgy and Materials ,矿物冶金与材料学报(英文版) , 编辑部邮箱 ,2019年10期
  • 【分类号】O643.12
  • 【被引频次】4
  • 【下载频次】20
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