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DIRECT REDUCTION OF FERROUS OXIDES TO FORM AN IRON ...

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422<br />

Ünal, H. İ., Turgut, E., Atapek, Ş. H.and Alkan, A.<br />

magnetite (Fe3O4). The iron content is normally around 70 %, with traces of non-ferrous metals and alkaline<br />

compounds. Mill scale is formed by flaky particles of a size of generally less than 5.0 mm. The size distribution<br />

depends on the stage in the process where the mill scale is generated [9]. In this study, the particle size of the mill<br />

scale is between 400-500 μm. Table 1 shows the contents of raw materials for 1 ton. The slag formers having a<br />

particle size of ~ 200 μm include bentonite, dolomite, limestone and are added to charge as 20 kg. Table 2 shows<br />

the contents (%) of slag formers used in the study. The content of coal used in mill scale processing is 67.25 %<br />

and its particle size is ~ 150 μm.<br />

Table 1. The contents of raw materials (%).<br />

Raw materials %<br />

Mill scale 76.39<br />

Coal 22.06<br />

Slag formers 1.550<br />

Table 2. The contents of slag formers used in the study (%).<br />

Slag formers %<br />

Bentonite 10<br />

Dolomite 40<br />

Limestone 50<br />

Hematite ores in pellet form was supplied from ERDEMİR A.Ş. and its reduction by solid carbon having a purity of<br />

99 % was investigated as a function of of reduction time and the ratio of Cfix / Fetotal. Cfix / Fetotal ratio can be<br />

described as the amount of carbon necessary to reduce completely the iron oxide that exists in the system [10].<br />

Table 3 shows x-ray fluorescence (XRF) analysis of both mill scale and ore materials.<br />

Table 3. XRF anaylsis of mill scale and ore material used in the experimental study.<br />

Materials Fe Mn Si Al Ca Cr K O<br />

Mill scale 69.10 0.66 0.11 - 0.21 0.10 - 29.82<br />

Hematite<br />

ore<br />

62.40 - 1.20 0.30 0.50 - 0.10 35.50<br />

2.2. Reduction procedure<br />

Industrially iron is produced from iron ores, principally hematite (Fe2O3), magnetite (Fe3O4) by a carbothermic<br />

reaction that is reduction with carbon, in a blast furnace at temperatures about 800-1600 °C. In the blast furnace,<br />

iron ore, carbon in the form of coke, and a flux such as limestone are fed into the top of the furnace, while blast of<br />

heated air is forced into the furnace at the bottom. Reduction of iron oxides occurs either by carbon or by carbon<br />

monoxide, formed by the gasification of carbon. The reduction process carried out by the carbon is called as<br />

direct reduction and the reaction can be defined in equation 1.<br />

FexOy + yC = xFe + yCO (equation 1)<br />

On the other hand, the reduction process conducted with CO is called as indirect reduction and its reaction is<br />

given in equation 2 and 3. The reduction of ferrous materials can be indirectly achieved by hydrogen and<br />

equations 4-6 indicate the stages of reactions. The reduction of iron ores by hydrogen is a gas-solid reaction<br />

which occurs in two or three stages. For temperatures higher than 570°C, hematite (Fe2O3) is first transformed<br />

into magnetite (Fe3O4), then into wustite (Fe1-yO), and finally into metallic iron whereas at temperatures below<br />

570°C, magnetite is directly transformed into iron since wustite is not thermodynamically stable.<br />

FexOy + yCO = xFe + yCO2 (equation 2)<br />

yCO2 + yC = 2yCO (Boudouard Reaction) (equation 3)<br />

3Fe2O3 + H2 → 2Fe3O4 + H2O (equation 4)<br />

Fe3O4 + H2 → 3FeO + H2O (equation 5)<br />

FeO + H2 → Fe + H2O (equation 6)

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