Method of processing reduced ferric oxides
专利摘要:
1522248 Silicate coated sponge iron MIDREX CORP 26 Aug 1976 [19 Sept 1975] 35591/76 Heading B2E Oxidation of sponge iron is inhibited by treatment with an alkali metal silicate, preferably as an aqueous solution, e.g. by immersion or spraying. The alkali metal is preferably Na but may be K or Li. The treated sponge iron may be dried under oxidising conditions, e.g. at 250 to 400‹F. 公开号:SU712033A3 申请号:SU762399512 申请日:1976-09-15 公开日:1980-01-25 发明作者:Артур Эхрендт Уильям;Чарльз Мейсснер Дэвид 申请人:Мидрекс Корпорейшн (Фирма); IPC主号:
专利说明:
I The invention relates to the treatment of reducing iron oxides, in particular, to the technology of preventing the oxidation of reducing iron, and the slowing down of rusting of sponge iron. A known method for producing sponge iron, metallized granules, briquettes or materials from a reducing metal, in which iron ore is reduced to metallic iron by direct contact with a reducing gas, such as a mixture of hydrogen and carbon monoxide. Reduced iron oxides with a degree of metallization of at least 80 / o are treated with an alkali metal silicate solution to obtain a protective sheath preventing oxidation of the reducing iron f I. However, with this method, the reducing metal is oxidized by water or air, and an insufficiently thick protective coating of alkali metal leads to the fact that iron is oxidized in air to form a magnetic iron by the reaction: 3Fe- | -20ft- Fe, 0. (I) This oxidation reaction is highly exothermic, which can lead to harmful losses in metallic iron content or metallization, as well as excessive overheating of the volume of sponge iron and its combustion. When water is in contact with iron in the presence of atmospheric oxygen, the occurrence of rust occurs in two stages. In the first stage of rusting, iron hydroxide is formed by the reaction: (2) Fe + HtO + l / 2O Fe (OH) x The second and final stage of rusting - the formation of hydrated iron oxide occurs in accordance with the reaction: (.one) 2F (OH) a + Hj, 0 + 1/2 O There is also a third reaction in which hydrogen is released. Part of the first stage of rusting is converted to form iron oxide, known as magnetic iron, water and hydrogen by the reaction: (four) 3Fe (OH) i FejO + + H Reactions (2) and (3) are exothermic. The amount of heat released by the reaction only at 15% of the source water is capable of providing latent heat for the vapors of the remaining 85% of the source water. Although reaction (4) is somewhat endothermic, the cooling effect is small. The impact of atmospheric air and moisture on the mass of active working sponge iron causes rusting with significant losses of metallization. The purpose of the invention is to achieve the effectiveness of the process of preventing oxidation and hydrogen generation by creating a method for slowing down the rusting of metallic materials that are chemically active because of their high porosity and the associated high specific surface area. This is achieved in that the reduced iron is immersed in an aqueous solution of liquid alkali metal silicate, followed by drying at a temperature below the spontaneous iron sponge ignition temperature. Iron reacts with water from an aqueous solution to form a solid corrosive product, which is a positively charged iron hydroxide, which immediately removes the negatively charged silica particles from the solution, to form a protective film of an amorphous, silica gel on the surface of iron. With the formation of a film of corrosion, the metal surface ceases. Since the formation of the film depends on the presence of the corrosive product and no further formation of the corrosive product occurs after the formation of the film, its buildup is prevented. Thus, in this way, the protective film is self-thicknessing, in addition, it self-shrinks when damaged. When part of the film is removed from the surface, corrosion of the exposed surface begins and a film formation reaction occurs immediately. The electric potential between the negatively charged silica and the positively charged iron hydroxide causes the silica to be attracted to a solid surface that forms a film in the corners and sharp areas of the surfaces, since the capillary action of the porous body leads to a rapid absorption of the sodium silicate solution into spongy iron. Treatment solutions according to the invention are single soluble alkali metal silicates. The preferred alkali metal silicate is aqueous sodium silicate with a concentration of from 2 to 50 wt.%, But lithic or potassium silicates should be used. Sodium silicate is a generic definition for the family of chemical elements containing sodium oxide (NatO), silica (SiOj) and usually water (). The ratio of NajO to SiOj in sodium silicate is expressed as the weight ratio at which the alkaline component is taken as unit. It was established experimentally that a drying temperature of up to 175 ° C is effective when the coolant is heated air. When drying at a temperature of 205 ° C, the treatment is not as effective for passivating the granules in a wet or dry state. The drying temperature must be significantly lower than the spontaneous combustion temperature of the sponge iron, which is in the 230 ° C range. S and 260 ° C. Thus, the drying temperature should not exceed 205 ° C and preferably does not exceed 175 ° C. The best results are achieved when drying is carried out in an oxidizing atmosphere.
权利要求:
Claims (1) [1] Invention Formula The method of processing reduced iron oxides with a degree of metallization up to 80% by creating a protective shell of alkali metal silicate on the surface of the pellets, characterized in that, in order to effectively prevent oxidation and hydrogen generation, the reduced iron is immersed in an aqueous solution of liquid alkali metal silicate, followed by drying at sponge iron spontaneous combustion temperature . Sources of information taken into account in the examination 1. Troms Iron and Steel Inst lap 1975, 5, No. 8, -429-435.
类似技术:
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同族专利:
公开号 | 公开日 BE890184Q|1982-01-04| DE2640419B2|1977-09-15| DE2640419C3|1978-04-20| AR209826A1|1977-05-31| AU1774476A|1978-03-23| FR2324756B1|1982-11-12| EG12062A|1978-06-30| CA1068560A|1979-12-25| NO142482C|1980-08-27| NO142482B|1980-05-19| GB1522248A|1978-08-23| BR7606114A|1977-05-24| KE3140A|1981-07-24| ZA764991B|1977-07-27| JPS5917164B2|1984-04-19| NO763174L|1977-03-22| MY8200069A|1982-12-31| US4069015A|1978-01-17| FR2324756A1|1977-04-15| DE2640419A1|1977-03-24| AU500617B2|1979-05-24| JPS5239541A|1977-03-26| MX144268A|1981-09-22|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题 US2462900A|1946-09-30|1949-03-01|John P Riott|Reduction accelerator for the sponge iron rotary kiln process| US3597260A|1966-11-01|1971-08-03|Exxon Research Engineering Co|Passivation of metals| US3632390A|1969-07-16|1972-01-04|Claremont Polychemical Corp|Process of coating metal flakes with calcium silicate| US3690930A|1970-07-13|1972-09-12|Exxon Research Engineering Co|Method of protecting reduced iron ore by coating| JPS5222620B2|1972-10-07|1977-06-18|US4388116A|1981-08-04|1983-06-14|Hylsa, S.A.|Passivation of sponge iron| DE4441591C2|1994-11-11|2001-05-03|Peter Goerzen|Process for corrosion protection of exhaust pipes and silencers for exhaust gases from motor vehicles with internal combustion engines| DE19518514A1|1995-05-19|1996-11-21|Setral Chemie Technology Gmbh|Corrosion inhibitor for use in aq. media| US6599643B2|1997-01-31|2003-07-29|Elisha Holding Llc|Energy enhanced process for treating a conductive surface and products formed thereby| US6592738B2|1997-01-31|2003-07-15|Elisha Holding Llc|Electrolytic process for treating a conductive surface and products formed thereby| US6322687B1|1997-01-31|2001-11-27|Elisha Technologies Co Llc|Electrolytic process for forming a mineral| US6743275B1|2000-05-22|2004-06-01|Alternative Casting Technologies, Llc|Method of making and using ferrous metal particle briquettes| JP2002363625A|2001-06-05|2002-12-18|Kobe Steel Ltd|Surface coated reduced iron, production method therefor and dissolution method therefor| BRPI0603592A|2006-08-22|2008-04-08|Vale Do Rio Doce Co|liquid or pulp aerator device| AU2011299042A1|2010-09-10|2013-03-21|Nu-Iron Technology, Llc|Processed DRI material| US9045809B2|2012-05-05|2015-06-02|Nu-Iron Technology, Llc|Reclaiming and inhibiting activation of DRI fines| US9464338B2|2012-05-05|2016-10-11|Nu-Iron Technology, Llc|Reclaiming and inhibiting activation of DRI dust and fines|
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申请号 | 申请日 | 专利标题 US05/614,830|US4069015A|1975-09-19|1975-09-19|Method of inhibiting rusting of sponge iron| 相关专利
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