• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A method of producing an aluminum metal from alumina, silica and iron oxide bearing materials by mixing the coal and bringing the mixtures to the temperature in the range of 600 DEG to 900 DEG C. in order to make the alumina bearing coked briquettes. Then, the coked briquettes are brought to the temperature in the range of 2,000 DEG to 2,100 DEG C. to produce aluminum, silicon and iron containing alloys. The alloys are scrubbed by molten lead spray directly after the alloys formation, and are converted to lead-aluminum alloy. An aluminum is separated from lead by liquation and purified by fractional distillation.
    公开号:SU1309915A3
    申请号:SU813263846
    申请日:1981-03-30
    公开日:1987-05-07
    发明作者:Кувахара Кенси
    申请人:Мицуи Алюминиум Ко Лтд (Фирма)；
    IPC主号:
    专利说明:

    113
    The invention relates to the production of aluminum and: 3 poor ores by the carbon-thermal method in a shaft furnace. The purpose of the invention is to increase the yield of aluminum and ensure the continuity of the process.
    The method involves the preparation of a mixture of ores with the addition of a carbon-containing component, which is then briquetted and subjected to heat treatment in a coking oven at a temperature of 600-900- for 20--50 minutes in a stream of non-oxygenating gases from the combustion products of the fuel in a shaft furnace. Hot briquettes serve "a shaft furnace where they progress
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    thirty
    and are heated down to temperatures of 000-2100 ° C, at which the carbothermal reduction of oxides proceeds with the formation of an alloy of etals: aluminum, silicon and iron. Molded lead is sprayed onto the droplets of metal in the area of the tuyeres, which adsorbs the reduced metals, in particular aluminum.
    Molten lead containing aluminum is transferred from the bottom of the shaft furnace to a segregation furnace, from where the upper layer is sent to fractional distillation, and the lower layer is recycled to the tuyere part.
    shaft furnace. I
    Example. To establish the charge, the mass molecular ratio of SiOj: AljOj is 1.5: 1, clay, May. %: 34.14; SiOj - 46.68 4.74, mixed with other components of the mixture in the following ratio, wt.%: Clay 43.5; alumina 8.7; sinter coal 47.8; A recycle load is added in an amount of 8.7% of the amount of previously mixed components.
    The material is crushed, passed through a No. 10 mesh sieve and mixed in a mill with the addition of a small amount of calcium aluminate as a binder. The mixture is briquetted with jfl lumps 110 75 65 65 and weighing about 0.5 kg and carbonized at a temperature of combustion products of 800 ° C. As a result of 30 minutes of processing, briquettes with a strength of 137 kg / cm and a bulk weight of ff45 kg / m were obtained.
    Filling the volume of the shaft furnace with 65% of the briquettes is heated in it to 2000-2100 ° C and is subjected to carbothermic
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    32
    recovery. The resulting aluminum alloy with silicon and iron flows down to the bottom. Under the level of tuyeres of the shaft furnace, molten lead is sprayed on the nago. Lead-aluminum alloy is removed from the bottom of the shaft furnace to a segregation crucible where it is exfoliated. The top layer containing aluminum is fed to the removal of lead residues by fractional distillation, and the bottom layer and lead residues are returned to the process.
    Example 2. When using clay containing, wt.%: AljUj 27,96; SiOj 54.82; 1.76, it is mixed with other components of the mixture, in the following ratio, wt.%: Clay 37.0; aluminum 14.8; coking coal 48.2; recycle 9.3.
    The material is crushed, passed through a No. 10 sieve, mixed in a mill with the addition of calcium aluminate, after which the mixture is briquetted. The tio processed in the coking oven briquettes are fed to the shaft furnace, where as they move downward they heat up to 2000-2100 s. The alloy of aluminum with silicon and iron formed during the carbothermic reduction, after the molten lead is sprayed onto it, forms a lead-aluminum alloy, which is first subjected to segregation and then the upper layer of fractional distillation.
    The table provides comparative research results.
    fl
    0
    five
    five
    权利要求:
    Claims (3)
    [1]
    Claim 1. Investigation of aluminum by cartothermic reduction in a shaft furnace of a briquetted mixture of materials containing oxides of aluminum, silicon, iron and carbon, to produce an aluminum alloy with silicon and iron and then extracting aluminum from it, characterized in that , in order to increase the yield of aluminum and ensure the continuity of the process, a briquetted mixture containing 35 to 50 wt.% of carbon is subjected to reduction, and the mixture is preoxidated e 20- 50 minutes in a medium non-oxidizing gas comprising less than 1% oxygen schihty reconstitution was carried out at 2000 - 2100 C to obtain an aluminum-silicon
    313
    iron alloy, molten lead is sprayed onto the alloy to extract aluminum from it to produce a lead-aluminum alloy, then lead-aluminum alloy is segregated to separate aluminum and lead, followed by distillation of aluminized aluminum to remove lead residues from it.
    [2]
    2. The method according to claim 1, about tl and h and u and with the fact that as the material of the mixture containing oxides of aluminum, silicon and iron, use clay, kaolinite, agalmatorite, aluminum slate and bauxite
    A1 Si W P
    Editor A. Kozoriz
    Compiled by A.Kalnitsky Tehred M. Khodanych
    Order 1808/58 Circulation 605 Subscription
    VNIZhM USSR State Committee
    for inventions and discoveries 113035, Moscow, Zh-35, Raushsk nab., 4/5
    Production and printing company, Uzhgorod, Projecto st., 4
    154
    the molecular ratio of silica to alumina in the mixture is in the range of (1-2): 1,
    [3]
    3. Method POP.1, characterized in that the sprinkling of molten lead onto an aluminum-silicon-iron alloy is carried out below the tuyere level of the shaft furnace, the lead-aluminum alloy formed on the bottom of the furnace is fed into the segregation crucible with the release of the main part of aluminum and the remaining lead in it is removed in the next; It is a fractional distillation.
    99.0 0.04 0.16 0.00
    Proofreader M. Demchik
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    同族专利:
    公开号 | 公开日
    DE3109318A1|1982-03-04|
    US4394167A|1983-07-19|
    CA1162055A|1984-02-14|
    FR2480790B1|1987-11-27|
    GB2076022B|1983-06-02|
    IT1154036B|1987-01-21|
    GB2076022A|1981-11-25|
    AU521285B2|1982-03-25|
    JPS591777B2|1984-01-13|
    BR8101507A|1982-01-12|
    AU6802481A|1981-10-29|
    IT8167353D0|1981-03-13|
    FR2480790A1|1981-10-23|
    JPS56150143A|1981-11-20|
    DE3109318C2|1985-03-21|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US1379523A|1919-08-15|1921-05-24|Standard Oil Co|Process of reducing aluminum oxid|
    CH133189A|1927-08-04|1929-05-31|Lonza Ag|Process for the production of alumina by electrothermal means.|
    FR1064876A|1951-10-19|1954-05-18|Kloeckner Humboldt Deutz Ag|Process for obtaining an aluminum alloy|
    US3234008A|1962-05-04|1966-02-08|Arthur F Johnson|Aluminum production|
    US3661561A|1970-08-03|1972-05-09|Ethyl Corp|Method of making aluminum-silicon alloys|
    US3661562A|1970-12-07|1972-05-09|Ethyl Corp|Reactor and method of making aluminum-silicon alloys|
    SU454839A1|1971-09-17|1977-11-25|Днепровский Ордена Ленина Алюминиевый Завод|Briquette for obtaining aluminium-silicon|
    GB1366808A|1972-02-08|1974-09-11|Alcan Res & Dev|Direct reduction process for production of aluminium|
    US3860415A|1972-08-02|1975-01-14|Ethyl Corp|Process for preparing aluminum|
    DE2335669A1|1973-07-13|1975-02-06|Metallgesellschaft Ag|PROCESS FOR THE MANUFACTURING OF ORECAKE HOT BRIQUETTES FOR SELF-DIVIDING|
    HU167973B|1973-09-28|1976-01-28|Veszpremi Vegyipari Egyetem|Process for producing anhydrous aluminium trichloride from aluminium containing raw materials|
    DE2420595A1|1974-04-27|1976-02-05|Wimmer Geb Haugg Erna|Recovery of metallic aluminium and silicon - by fusion melting using low grade carbon contg material as reductant|
    GB1472683A|1975-02-05|1977-05-04|Willhoft E|Recovering aluminium values from aluminium-containing minerals|
    ZA774928B|1976-08-23|1978-06-28|Tetronics Res & Dev Co Ltd|Preparation of feed materials for carbothermal processes|
    US4046558A|1976-11-22|1977-09-06|Aluminum Company Of America|Method for the production of aluminum-silicon alloys|
    US4053303A|1976-12-06|1977-10-11|Aluminum Company Of America|Method of carbothermically producing aluminum-silicon alloys|
    DE2801274B1|1978-01-13|1978-08-31|Vaw Ver Aluminium Werke Ag|Process for the production of stable pellets for the acid digestion of ores containing aluminum silicate|US4486229A|1983-03-07|1984-12-04|Aluminum Company Of America|Carbothermic reduction with parallel heat sources|
    US4491472A|1983-03-07|1985-01-01|Aluminum Company Of America|Carbothermic reduction and prereduced charge for producing aluminum-silicon alloys|
    US4734130A|1984-08-10|1988-03-29|Allied Corporation|Method of producing rapidly solidified aluminum-transition metal-silicon alloys|
    US4659374A|1985-06-14|1987-04-21|Dow Corning Corporation|Mixed binder systems for agglomerates|
    WO2010033108A1|2008-09-16|2010-03-25|Alcoa Inc.|Sidewall and bottom electrode arrangement for electrical smelting reactors and method for feeding such electrodes|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    JP55053374A|JPS591777B2|1980-04-22|1980-04-22|
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