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Experimental research on the novel process of iron ore direct reduction by coal gas

机译:煤气直接减少铁矿石新工艺的实验研究

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In this paper, the direct reduction of iron ore pellets was carried out by simulating the typical gas composition in coal gasification process, Midrex and Hyl III process, the influence of gas composition and temperature on reduction was studied. Results show that the proportion of H_2 increasing is helpful to improve the reduction rate, while when H_2/CO>1.6, changes of H_2 content will have very little influence on it. Appropriate reduction temperature is about 950°C, higher temperature(1000°C) may unfavorably slowed the reduction rate. From the kinetics analysis at 950°C and 1000°C, when H_2/CO=0.4 the prophase of reduction course (~90%) is likely controlled by interfacial chemical reaction mechanism and in the later controlled by gaseous diffusion mechanisms. However, when H_2/CO>0.4 the whole reduction course is likely controlled by interfacial chemical reaction mechanism. The reaction rate constant (k) and effective diffusion coefficient (De) at 950°C are both better than those at 1000°C. Research also shows that the coal-water slurry gasification based on Texaco furnace is more suitable for iron ore direct reduction than other coal gasification processes.
机译:本文通过模拟煤气化过程中的典型气体组合物,中鼻肌III工艺,研究了铁矿石颗粒的直接减少,研究了气体组成和温度对还原的影响。结果表明,H_2增加的比例有助于提高减少率,而当H_2 / CO> 1.6时,H_2内容的变化对其影响很小。适当的还原温度约为950℃,较高温度(1000℃)可能不利地减缓减少率。从950℃和1000℃的动力学分析,当H_2 / CO = 0.4时,还原过程(〜90%)的预先通过界面化学反应机理控制,并在通过气态扩散机构控制的后来控制。但是,当H_2 / CO> 0.4时,整个还原过程可能由界面化学反应机制控制。在950℃下,反应速率常数(k)和有效扩散系数(DE)比1000℃的那些更好。研究还表明,基于德克萨克炉的煤水泥气化更适合于铁矿石直接减少而不是其他煤气化过程。

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