Three-dimensional transient modelling of coal and coke co-combustion in the dynamic raceway of ironmaking blast furnaces

被引:84
作者
Zhuo, Yuting [1 ]
Shen, Yansong [1 ]
机构
[1] Univ New South Wales, Sch Chem Engn, Sydney, NSW 2052, Australia
基金
澳大利亚研究理事会;
关键词
Transient model; Blast furnace; Raceway; Coal; Coke; Combustion; NUMERICAL-SIMULATION; CHINA IRON; GAS; COMBUSTION; FLOW; TUYERE; GASIFICATION; INJECTION; HEIGHT; SIZE;
D O I
10.1016/j.apenergy.2019.114456
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The blast furnace is a highly efficient but energy-intensive chemical reactor for iron production. Two types of solid fuels, viz. coarse coke particles and fine pulverized coal powders, are combusted simultaneously, forming the dynamic cavities (termed raceway) at the lower part of the blast furnace, and their behaviour affects each other considerably, although this has not been clearly established in the past. In this study, a three-dimensional transient model is developed for describing the complex co-combustion of pulverized coal and coke coupled with the dynamic raceway evolution under industrial-scale blast furnace conditions. The model couples a gas-coke combustion model with a gas-coal combustion model in a transient state by means of two-way coupling scheme. The model is then validated against experimental measurements. The typical transient in-furnace phenomena are illustrated in terms of raceway shape and size, gas-solid-powder flow, temperature fields, gas composition and coal and coke combustion. As time progresses from 0 s to 7.0 s, the raceway size increases in depth, width and height; and the coal burnout slightly increases. At around 7.0 s, the raceway profile and coal and coke combustion approach a relatively stable state. Additionally, the effects of blast rate on the in-furnace phenomena are studied. Under the simulated conditions, when the blast rate is increased from 140 m/s to 180 m/s, a larger raceway is formed and the depth is increased by 22.2%. Subsequently, the average burnout of pulverized coal is improved by 3.6% and the reducing gas, i.e., CO, is increased by 1%. This model offers a cost-effective tool to optimize coke/coal co-combustion in blast furnaces for energy saving and operation stability.
引用
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页数:14
相关论文
共 51 条
[1]   Potential of energy savings and CO2 emission reduction in China's iron and steel industry [J].
An, Runying ;
Yu, Biying ;
Li, Ru ;
Wei, Yi-Ming .
APPLIED ENERGY, 2018, 226 :862-880
[2]  
[Anonymous], 1977, S INT COMBUST
[3]  
[Anonymous], 2018, BAOST INT TECHN REP
[4]   REACTIONS BETWEEN CARBON AND OXYGEN [J].
ARTHUR, JR .
TRANSACTIONS OF THE FARADAY SOCIETY, 1951, 47 (02) :164-178
[5]   Hydrodynamic analysis of gas-liquid-liquid-solid reactors using the XDEM numerical approach [J].
Baniasadi, Maryam ;
Peters, Bernhard ;
Baniasadi, Mehdi ;
Besseron, Xavier .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2018, 96 (12) :2673-2683
[6]   2-DIMENSIONAL RADIATING GAS FLOW BY A MOMENT METHOD [J].
CHENG, P .
AIAA JOURNAL, 1964, 2 (09) :1662-1664
[7]  
Chung JK, 1996, Met Mater, V2, P1, DOI 10.1007/
[8]  
De Bertodano, 1991, TURBULENT BUBBLY FLO
[9]   Performances of pulverized coal injection in blowpipe and tuyere at various operational conditions [J].
Du, Shan-Wen ;
Chen, Wei-Hsin ;
Lucas, John .
ENERGY CONVERSION AND MANAGEMENT, 2007, 48 (07) :2069-2076
[10]  
ERGUN S, 1952, CHEM ENG PROG, V48, P89