• 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 recovering non-volatile metals from materials in dust form containing metal oxides, comprising the steps of blowing the material into the lower portion of a reactor, said reactor containing a solid reducing agent, passing said starting material into a reduction zone within said lower portion, said reduction zone being maintained by the use of a plasma generator adjacent thereto, substantially instantaneously reducing and melting said starting material in sad reduction zone, and removing the melted and reduced metal product from the bottom of the reactor.
    公开号:SU980629A3
    申请号:SU803220199
    申请日:1980-12-12
    公开日:1982-12-07
    发明作者:Сантен Свен
    申请人:Скф Стил Инджиниринг Актиеболаг (Фирма)；
    IPC主号:
    专利说明:

    (5) METHOD FOR RESTORING DUSTIC OXIDES IN A MINE REACTOR
    This invention relates to methods for melting fine-grained metal ore in a heated reactor filled with solid reducing agent.
    A known method, designed to remelt metal ore, in particular iron ore. This ore must be crushed to a pulverized state, and the pre-reduced ore is injected into the shaft furnace Q through nozzles, to which oxygen and gaseous hydrocarbons are simultaneously supplied.
    However, the reduction of nonvolatile metals from dust particles, which are determined, for example, when cleaning electrostatic precipitators, is not possible with the help of known means.
    In addition, such fine particles of metal oxides are released on refining of metal melts, and their amount is 50,000-60000 tonnes. per year only in the northern countries of Europe. These particles are a source of environmental pollution and
    form poisonous heavy metal compounds. .
    The closest to the proposed technical essence and the achieved result is a method of reducing pulverized oxides in a shaft reactor filled with solid carbon, including injecting the source material into the reduction zone formed by plasma torches in the lower part of the reactor using a carrier gas, restoring, melting and tapping the liquid metal one ..
    However, this method does not fully utilize the energy of the exhaust gases and does not allow recovery of the hardly reduced oxides.
    The purpose of the invention is the effective reduction of metals in the form of powdered oxides.
    The goal is achieved by the method of reducing non-volatile metals in the form of pulverized oxides in a shaft reactor filled with a solid reducing agent, which involves injecting a source material into the reduction zone formed by plasma torches in the lower part of the reactor, reducing, melting and removing liquid metal, pulverized oxides are blown into the reduction zone by means of gas, which is removed from the reactor throat, while carbon and / or slag forming gases are added to the oxides. additives, and flue gas is used to operate plasma torches.
    The drawing shows a diagram explaining the invention.
    In the diagram, there is a shaft furnace or reactor 1 loaded with a solid reducer, for example, coke through a gas-tight top furnace 2. The temperature in the reactor is controlled by one or several plasma torches.
    The pulverized starting material is introduced by means of a carrier gas through conduit 3 directly into the lower part of the reactor. A plasma torch or several torches are connected to the supply pipeline k for the transport medium (plasma gas).
    The portion of the reducing gas produced in the reactor is captured and used as a carrier gas or plasma gas. This gas leaves the reactor through the outlet nozzle 5 and is then sent in an expedient way to control its temperature through the heat exchanger 6.
    In the presented scheme, about 20% of the reaction gas flowing through the heat exchanger, as carrier gas or plasma gas, is returned to the circulating system through the gas-cleaning device 7, the connected blower and, possibly, through the compressor.
    The remaining 80 of the reaction gas exiting the heat exchanger containing carbon monoxide and hydrogen can be used for other purposes, for example for generating electricity.
    The carrier gas line is arranged in such a way that it interacts with a loading device 8, for example, a pneumatic loading device connected to the loading auger 9 connected to bunkers 10-12 containing pulverized raw material, as well as
    coal powder and slag-forming additives.
    When blown into the reactor, dust is instantaneously recovered, and melting occurs at the bottom of the reactor. The melt flows to the bottom of the reactor and is discharged from there through the outlet channel 13, while the slag is continuously or discretely discharged through the outlet channel 1.
    The required temperature in the recovery zone of the reactor, lying in the range of 1500-1 ° C, is easily controlled. using a plasma torch. In this case, the reactor and the coke bed can be adjusted in such a way that the pulverized starting material containing metal oxides is retained in the lower part of the coke bed 15, and the gas leaving the reactor consists of carbon monoxide and hydrogen.
    Example. A ton of filter dust containing metal oxides, in particular chromium oxide, is scraped from the filter walls for the exhaust gases during the production of stainless steel and collected. The initial size of the dust particles is 2-6 microns, and the dust has the following composition
    13 38
    Ni 6
    MoOj1,2
    The residue is slags, such as CaO, 02, and the like. This dust is mixed with 320 kg of coal powder and 12 kg of Og, a slag-forming additive. Thereafter, the mixture is continuously blown into the reduction zone of the reactor. The energy consumption for maintaining a temperature in the reduction zone of about 1550 ° C is about 2 kW of kWh, and the temperature is created by the plasma torch.
    Get 475 kg of iron, with the content,%. chromium 21, nickel 11, molybdenum 2.3.
    Further: 620 m of reaction gas consisting of,%: CO 70, N2 20, a mixture of nitrogen, carbon monoxide and water 10.
    The heat of combustion of the reducing gas is about 2,700 kcal /
    权利要求:
    Claims (2)
    [1]
    Invention Formula
    The method of reducing powdered oxides in a shaft reactor is filled with a 59806 solid reducing agent, which involves injecting, using a carrier gas, the starting material into the reduction zone formed by plasma torches in the lower part of the reactor, reducing, melting and releasing a liquid metal that, in order to increase the reduction efficiency of nonvolatile metals, pulverized oxides are blown into the reduction zone by means of gas emitted from the top of the reactor, while adding oxides to the oxides od and / or slag-forming additives, and the top gas is used for operation of plasma burners, sources of information, the received note in the examination 1. Patent of Germany N 2 03708, cl. C 07 D 39/30, 1975.
    [2]
    2. Patent of Sweden. W 388210, cl. From 21 to 11/02, 1971.
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    同族专利:
    公开号 | 公开日
    FI69115C|1985-12-10|
    AU532706B2|1983-10-13|
    US4310350A|1982-01-12|
    BR8100086A|1982-01-12|
    MX155702A|1988-04-15|
    DE3042276A1|1981-12-17|
    DE3042276C2|1985-07-04|
    AT373628B|1984-02-10|
    CA1150518A|1983-07-26|
    AR223256A1|1981-07-31|
    JPS5713130A|1982-01-23|
    CH647552A5|1985-01-31|
    FR2483955B1|1986-01-17|
    CS212727B2|1982-03-26|
    FR2483955A1|1981-12-11|
    PL135368B1|1985-10-31|
    KR830004441A|1983-07-13|
    FI803612L|1981-12-11|
    DD155330A5|1982-06-02|
    IT1141144B|1986-10-01|
    KR850001212B1|1985-08-20|
    OA06825A|1982-12-31|
    AU6456480A|1981-12-17|
    BE886233A|1981-03-16|
    JPS6055574B2|1985-12-05|
    IT8026770D0|1980-12-18|
    FI69115B|1985-08-30|
    ZA807151B|1981-10-28|
    ES496766A0|1981-10-16|
    PH16514A|1983-11-08|
    ES8107322A1|1981-10-16|
    PL229282A1|1982-06-07|
    SE8004313L|1981-12-11|
    ZW10481A1|1981-11-18|
    ATA561580A|1983-06-15|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    WO2005061739A1|2003-12-22|2005-07-07|Anatoly Timofeevich Neklesa|Device for producing iron from iron-containing raw material|
    WO2005080609A1|2004-02-23|2005-09-01|Anatoly Timofeevich Neklesa|Method for producing iron by direct reduction and device for carrying out said method|
    WO2006075977A1|2005-01-17|2006-07-20|Anatoly Timofeevich Neklesa|Plant for directly reducing iron oxides and for producing an iron melt|US2781255A|1955-11-16|1957-02-12|Union Carbide & Carbon Corp|Treatment of fumes containing suspended solids|
    FR1452850A|1965-08-04|1966-04-15|Siderurgie Fse Inst Rech|Electric furnace ore reduction process|
    US3429691A|1966-08-19|1969-02-25|Aerojet General Co|Plasma reduction of titanium dioxide|
    US3862834A|1971-04-03|1975-01-28|Krupp Gmbh|Method for producing steel|
    US4072504A|1973-01-26|1978-02-07|Aktiebolaget Svenska Kullagerfabriken|Method of producing metal from metal oxides|
    US3834895A|1973-04-11|1974-09-10|Park Ohio Industries Inc|Method of reclaiming iron from ferrous dust|
    SE395714B|1974-02-20|1977-08-22|Skf Ind Trading & Dev|METHODS AND DEVICES FOR MANUFACTURE OF METALS FROM OXIDIC MATERIAL|SE446014B|1981-03-10|1986-08-04|Skf Steel Eng Ab|SELECTIVE REDUCTION OF HEAVY-CORNED METALS, MAINLY OXIDICAL, MATERIALS|
    SE457265B|1981-06-10|1988-12-12|Sumitomo Metal Ind|PROCEDURE AND ESTABLISHMENT FOR PREPARATION OF THANKS|
    SE436124B|1982-09-08|1984-11-12|Skf Steel Eng Ab|SET TO MAKE PROCESS|
    US4530101A|1983-04-15|1985-07-16|Westinghouse Electric Corp.|Electric arc fired cupola for remelting of metal chips|
    US4606760A|1985-05-03|1986-08-19|Huron Valley Steel Corp.|Method and apparatus for simultaneously separating volatile and non-volatile metals|
    DE3535572C2|1985-10-03|1987-10-15|Korf Engineering Gmbh, 4000 Duesseldorf, De|
    JPS6286269U|1985-11-20|1987-06-02|
    US4765828A|1987-06-19|1988-08-23|Minnesota Power & Light Company|Method and apparatus for reduction of metal oxides|
    JPH0726160B2|1988-03-18|1995-03-22|日新製鋼株式会社|Method for recovering valuable metals from by-products during stainless steel production|
    JPH07103428B2|1992-01-17|1995-11-08|兼子操|Method of recovering valuable metals from iron-making dust using a vertical reduction melting furnace|
    DE4236202C2|1992-10-27|1994-07-21|Bayer Ag|Process for the low-residue and high-consumption production of sodium dichromate|
    US5399833A|1993-07-02|1995-03-21|Camacho; Salvador L.|Method for vitrification of fine particulate matter and products produced thereby|
    US5728193A|1995-05-03|1998-03-17|Philip Services Corp.|Process for recovering metals from iron oxide bearing masses|
    DE19539634C2|1995-10-25|1999-06-10|Hans Ulrich Feustel|Device for blowing in dusty and / or granular reactive substances and substance mixtures|
    US7169206B2|2004-04-19|2007-01-30|Umicore|Battery recycling|
    DE102006029725B4|2006-06-28|2008-08-28|Siemens Ag|Method and device for introducing dusts into a molten metal of a pyrometallurgical plant|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    SE8004313A|SE8004313L|1980-06-10|1980-06-10|SET OF MATERIAL METAL OXIDE-CONTAINING MATERIALS RECOVERED SOLAR METALS|
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