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Development of Reduction model of Ore Powder in a Fluidized Bed (Fundamental Research on lronmaking by Smelting Reduction)

Development of Reduction model of Ore Powder in a Fluidized Bed (Fundamental Research on lronmaking by Smelting Reduction)
流化床矿粉还原模型的研制(熔融还原炼铁基础研究)
批准号:
05555200
负责人:
ONO Yoichi
金额:
$4.48万
依托单位:
依托单位国家:
日本
项目类别:
Grant-in-Aid for Developmental Scientific Research (B)
财政年份:
1993
资助国家:
日本
项目状态:
已结题
起止时间:
1993 至 1995

项目摘要

项目成果

ONO Yoichi的其他基金

相关文献

中文摘要
翻译
本研究的主要结果如下:1.提出了用热天平测定单个赤铁矿颗粒还原速率的方法,以确定用于流化床还原速率分析的速率参数。实验证明,所获得的速率参数可用于流化床还原速率分析.在还原孔隙率为10-20%的工业矿石的情况下,即使在直径为0.15mm的小颗粒中,颗粒中的扩散阻力也不能忽略。另一方面,对于孔隙率为30%的试剂级赤铁矿粉,还原速率受化学反应控制.测量了不同形状(球形、圆柱形和平板形)的大尺寸试样的压下速率,并从数据中获得了速率参数。速率参数随形状因子的变化而变化.建立了一个考虑流化床内颗粒粒度分布的还原模型。实验表明,该模型在床层中颗粒偏析严重的情况下是有效的.建立了一个考虑流化床还原过程中颗粒降解和带出导致颗粒直径减小的数学模型。发现由于颗粒的降解,还原速率明显加快.颗粒的降解是由还原和流化引起的。在700 ℃的流化床还原中,降解最为显著。
英文摘要
The main results of this research are as follows.1. The measurement method of reduction rate of single hematite particle by using thermo-balance was developed for the determination of rate parameters which can be used for the reduction rate analysis in a fluidized bed. It was confirmed in experiment that the obtained rate parameters can be used for the reduction rate analysis in a fluidized bed.2. The diffusion resistance in a particle was not able to be ignored in the case of reduction of commercial ores having the porosity of 10-20% even in the small particle of 0.15mm in diameter. On the other hand, in the case of reagent grade hematite powder having the porosity of 30%, reduction rate was controlled by chemical reaction.3. Reduction rate of the large size samples having various shape (sphere, cylinder, and plate) was measured and rate parameters were obtained from the data. The rate parameters varied with the value of shape factor.4. A reduction model considering the particle size distribution in a fluidized bed was developed. It was clarified in experiment that this model was effective in the case that particle segregation was significant in the bed.5. A mathematical model considering a decrease of particle diameter by degradation and carry-out of particles from the bed during the fluidized bed reduction was developed. It was found that the reduction rate became faster apparently because of the degradation of particles.6. Degradation of particles resulted from the reduction and the fluidization. Degradation was most significant in the fluidized bed reduction at 700゚C.
期刊论文(18)
专著(0)
科研奖励(0)
会议论文
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通讯作者:
荒木一朗: "Effect of Fluidization on Reduction of Hematite Powder by Fluidized Bed" The First International Congress on Science and Technology of Ironmaking. 134-139 (1994)
荒木一郎:“流化对流化床还原赤铁矿粉的影响”第一届国际炼铁科学技术大会134-139(1994)。
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I.ARAKI: ""Measurement of Reduction Rate of Hematite Powder with CO-CO_2 Gas Mixture by using Thermo-balance"" CAMP-ISIJ. 8-4. 1079-1079 (1995)
I.ARAKI:“使用热天平测量 CO-CO_2 气体混合物中赤铁矿粉末的还原率”CAMP-ISIJ。
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荒木一朗: "粉鉄鉱石の流動層還元に及ぼす流動化状態の影響" 材料とプロセス. 6. 878-878 (1993)
Ichiro Araki:“流化状态对细铁矿流化床还原的影响”材料和工艺。6. 878-878 (1993)。
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17
    Thermodynamic study of Multi-Component Calcium Ferrite
    • 批准号:
      63470050
    • 项目类别:
      Grant-in-Aid for General Scientific Research (B)
    • 资助金额:
      $3.58万
    • 财政年份:
      1988
    • 负责人:
      ONO Yoichi
    • 依托单位: