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AssigneesTatabanvai Szenbanyak, Mecseki Ercbanyaszati Vallalat
InventorsBela Czegledi, Mihaly Csovari, Miklos Erdelyi, Jozsef Illi, Lajos Stocker, Attila Szoke, Katalin Szabo nee Mogyorosi, Szilard Riederauer, Miklos Ormossy, Gyula Terenyi, Istvan Csurgai
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The invention relates to an improved process for reducing the iron content of iron-, silicon- and aluminium-containing raw materials and for producing ferric oxide, optionally along with an alumina concentrate. According to the invention the iron content of mineral raw materials, e.g. bauxites, clay minerals, colliary rocks, red muds, etc. is eliminated by passing through one or more beds prepared from the unground but preferably prebroaken and sized raw material an aqueous hydrochloric acid solution, the concentration of which exceeds 100 g./lit., at a temperature below 90.degree. C., preferably at room temperature, optionally in the presence of a flocculating agent. By pyrolytic decomposition of the ferric chloride prepared ferric oxide can be produced. The bed residue of reduced iron content can be utilized in the Bayer process for producing alum earth, as a starting substance of ceramic industry or, after treating with sulfuric acid, dissolving in hydrochloric acid or water, elimination of silica, pyrolytic decomposition of the aluminium sulfate obtained, as an alumina concentrate.
In a process for reducing the iron content of iron- silicon- and aluminum-containing raw materials and for producing ferric oxide, along with an alumina concentrate, by treating the starting materials with hydrochloric acid or with hydrochloric acid and chlorine gas, deironizing the ferric chloride containing solution with an ion exchange resin, eluting ferric chloride from the ion exchange resin, subjecting the ferric chloride to pyrrolytic decomposition, treating the residue of reduced iron content with sulfuric acid, heating to produce aluminum sulfate, and subsequently treating with water to eliminate silica, subjecting aluminum sulfate to pyrrolytic decomposition and recycling hydrochloric acid and sulfuric acid in the system, wherein the improvement comprises passing in an upward direction at a rate of 0.2-10 cm./hour in a semi-continuous counter-current flow through one or more beds prepared from the unground raw material an aqueous hydrochloric acid solution of a concentration exceeding 100 g./lit. at room temperature, maintaining the solid to liquid ratio between 1:0.3 and 1:1, and maintaining the required hydrochloric acid concentration of at least about 100 g./lit. by absorbing at least a part of the hydrochloric acid gas formed during the decomposition of the chlorides formed in the ferric oxide containing solution.
Dependencies are inferred from the claim text.