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全氧高炉炼铁工艺模拟分析
引用本文:王成善,时艳文,李丹丹,杨亚洲,穆小静. 全氧高炉炼铁工艺模拟分析[J]. 重庆大学学报(自然科学版), 2014, 37(9): 47-58
作者姓名:王成善  时艳文  李丹丹  杨亚洲  穆小静
作者单位:1. 重庆大学 材料科学与工程学院; 重庆大学 重庆市冶金工程重点实验室
2. 重庆大学 材料科学与工程学院
3. 重庆大学 化学化工学院,重庆,400044
基金项目:国家自然科学基金资助项目(50704040);重庆市自然科学基金资助项目(CSTC 2009BB4197)
摘    要:建立了全氧高炉工艺的系统模拟模型。该模型能够计算不同原燃料、不同操作参数下的原料消耗、熔剂消耗、渣量及其成分、各种煤气量及其成分等。模型计算结果表明:在炉身矿石金属化率为90%时,若在炉身底部吹入较多的循环煤气,热量的需求决定了完成炉身内矿石还原所需的煤气量;若在炉缸吹入较多的循环煤气,还原性气体的需求决定了完成炉身内还原所需的煤气量。在焦比固定和正常操作条件下,煤耗的计算值基本随系统输出煤气量的增加而线性增加。在焦比取为200 kg时,经计算获得的系统最低煤比为200 kg左右。

关 键 词:全氧高炉  数学模型  循环煤气  焦比  煤比  氧耗
收稿时间:2014-08-20

Simulation research on oxygen blast furnace ironmaking process
WANG Chengshan,SHI Yanwen,LI Dandan,YANG Yazhou and MU Xiaojing. Simulation research on oxygen blast furnace ironmaking process[J]. Journal of Chongqing University(Natural Science Edition), 2014, 37(9): 47-58
Authors:WANG Chengshan  SHI Yanwen  LI Dandan  YANG Yazhou  MU Xiaojing
Affiliation:School of Materials Science and Engineering; Chongqing Provincial Key Laboratory of Metallurgical Engineering,Chongqing University, Chongqing 400044, China,School of Materials Science and Engineering,Chongqing University, Chongqing 400044, China,School of Materials Science and Engineering,Chongqing University, Chongqing 400045, China,School of Materials Science and Engineering,Chongqing University, Chongqing 400046, China and School of Chemistry and Chemical Engineering, Chongqing University, Chongqing 400044, China
Abstract:A system simulation mathematical model on oxygen blast furnace ironmaking process is established. Provided that the material composition and the values of necessary process parameters are given, the model can predict the consumptions of raw material, fuel and flux, the quantity and composition of slag, the quantities and components of all kinds of gases, etc. At the condition of 90% stack ore metallization, the calculated results of the model show that when more circulating gas are introduced into the stack, the heat controls the total gas for the stack ore reduction, while when more circulating gas are introduced into the hearth, the reductive components control the total gas for the stack ore reduction. At normal operations with coke rate fixed, the coal consumption linearly increases with the output top gas. When the coke rate is fixed at 200 kg, the minimum value of calculated coal rate is 200 kg or so.
Keywords:oxygen blast furnace   mathematical model   circulating gas   coke rate   coal rate   oxygen consumption
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