Process for producing sponge iron particles and molten pig iron
AssigneeKorf Engineering GmbH
InventorBogdan Vuletic
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AssigneeKorf Engineering GmbH
InventorBogdan Vuletic
Estimating the term…
In this process for the direct production of sponge iron particles and molten pig iron from lump iron ore, which is reduced in a direct reduction unit (2) and supplied in the hot state to a melt-down gasifier (1), the sponge iron particles discharged from the direct reduction unit are separated into a fine particle fraction and a coarse particle fraction and only the former is supplied to the melt-down gasifier. Separation takes place in an air classifier (7) connected to the discharge means of the direct reduction unit and through said classifier flows cooling gas at a predetermined velocity in countercurrent to the sponge iron particles. This cooling gas is admixed with the reducing gas produced in the melt-down gasifier for the direct reduction unit and said gas mixture, as well as the fine particle fraction of the sponge iron entrained therewith are supplied to cyclones (5 and 6). The solid separated therein, e.i., the fine particle fraction and the coke particles, are introduced into the melt-down gasifier level with the coal fluidized bed. The gas mixture freed from the solids is used as a reducing gas in the direct reduction unit. Part is branched therefrom beforehand, washed and compressed and used as a cooling gas. The coarse particle fraction passes out of the air classifier into a cooling or buffer unit (4) and is then discharged therefrom.
A process for producing sponge iron particles and molten pig iron from lump iron ore comprising the steps of reducing the iron ore to sponge iron in a direct reduction unit by introducing the lump iron ore and a reducing gas into said direct reduction unit, discharging the sponge iron particles from said reduction unit and introducing same into an air separator, separating said sponge iron in said separator into a sponge iron fine particle fraction and a sponge iron coarse particle fraction, feeding the fine particle fraction to a melt-down gasifier, introducing coal and blown-in oxygen-containing gas into said melt-down gasifier to produce said reducing gas as well as the heat necessary for melting the fine particle fraction of the sponge iron, and introducing at least a part of said reducing gas into the direct reduction unit.
Dependencies are inferred from the claim text.