• 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:
    1. UNIT FOR THE PRODUCTION OF STEEL from solid and / or liquid charge materials, in particular, cast iron, large and lightweight scrap, containing a melt refining tank lined with refractory material, in which a plasma torch and devices for insertion can be moved in the vertical direction powdered materials, characterized in that, in order to increase the scrap fraction in the charge, an oxygen supply channel enclosed in a cooled housing is complete around the plasma torch, that at the bottom of the refining vessel for the melt under the plasma torch electrode set. 2. Pop-1 unit, characterized in that the devices for introducing additional powder materials are made in the form of feed tubes surrounding the cooled casing of the plasma torch. 3. The unit according to claims 1 or 2, differing in the fact that the plasma (Q torch has a central CO rod-shaped electrode installed in the annular gap for the water of the plasma gas. 4. The unit according to claims 1-3, characterized in that the channel for oxygen supply is made in the form of a crown of slit-like or round nozzles.
    公开号:SU1142006A3
    申请号:SU823529503
    申请日:1982-12-23
    公开日:1985-02-23
    发明作者:Федерль Йожеф；Лугшайдер Вальтер
    申请人:Фоест-Альпине Аг (Инопредприятие)；
    IPC主号:
    专利说明:

    The invention relates to metallurgistsId more specifically to devices for the production of steel, mainly converters. It is known the use of fuel ™ for oxidation: tuyeres to increase the fraction of scrap processed in steelmaking aggregates, Cl3 This device allows for a slight increase in the fraction of scrap in the steelmaking mixture chargej, however, this increases the total melting time. The closest in technical essence and the achieved effect to The invention is a unit for the production of steel from solid and / or liquid materials, in particular iron, coarse and lightweight scrap; containing a melt refining tank lined with a refractory material in which the plasma torch and C 2 addition powder materials are capable of moving in a vertical direction. .,. However, the known device does not provide for the formation of a broad melting front, the reaction can proceed only at E-very limited volume. Therefore, the use of a known device cannot ensure an increase in the proportion of scrap processed. The aim of the invention is to create a device that allows an increase in the scrap fraction in the charge. The goal is achieved by the fact that in an aggregate for the production of steel from solid and / or liquid charge materials 5 in particular cast iron a large and lightweight scrapj containing a melt refining tank lined with refractory material in which the plasma plasma is placed with the possibility of moving in the vertical direction Reel and devices for introducing additional powdered materials-5 around the plasma torch, the oxygen supply channel enclosed in a cooled housing was removed, while an electrode was installed under the plasma torch in the bottom of the tank for refining the melt. Devices for introducing additional powdered materials are made in the form of feed tubes surrounding the 62 crown of the cooled plasma burner housing. The plasma torch has a central sterling electrode, mounted in an annular gap for supplying a plasma gas. The oxygen supply channel is provided in the form of a crown of slit-like or round nozzles. Fig. 1 shows a refining tank, a vertical section; FIG. 2 shows a plasma torch, a cut on the axis -, —a pa of FIG. The refining tank 1 is made in the form of a tiltable converter with a metal outer casing 2 and a refractory lining 3. In the vertical position of the converter in the center of the cavity 4 of the converter, a tube 5 containing a plasma torch 6 enters. This tube 5 has a centrally located rod-shaped electrode 7 which is surrounded limited by tube 8 and annular space 9.1. in which plasma gas is produced, formed by Ar or He, .N 5 He, Co, CO and -i with their mixtures g The burner is preferably operated with argon 5 of an argon mixture with medical nitrogen. The arresting length of the arc is determined by the electrical voltage feeding the plasma torch. Plasma burner 6 is surrounded by another shell 10, which forms another annular plasma burner b annular space 11 for addition of technical pure oxygen for refining. At the end of the plasma torch 6 there is an annular space 1.1 through which oxygen is supplied, which passes into viable, radially symmetrical radially symmetric 1 holes 12, preferably a Laval nozzle, made of copper head 13 of the feed pipe 5. Oxygen outlets 12 for oxygen are parallel the burner axis 14, or is inclined to the axis 14 at an acute angle, so that a stream of oxygen is obtained either cylindrical, lighter, conical, diverging outside when exiting; va -) -, with a plasma jet 15 at a possibly greater distance from 3 heads 13. This significantly increases the service life of the cathode 7, especially the point 16 consisting of metallic tungsten. The cathode retaining insulators 17 have through holes 18 for smooth passage of plasma gas. Outside, the supply pipe is surrounded by a double cooling jacket 19, in which the circulation of the cooler is maintained by a known method. In the bottom 20 of the converter, a bottom electrode 21 is inserted in the center, the wear part of which is 22 steel outlets and has a cooled copper current lead 23. To add additional materials, the central supply pipe 5 env: two or more parallel pipes 24, which are located radialio str. 1 relative to the pipe 5 Through the radial consumption of oil and gas pipe 24, dusty oxides of the same left 5 can be blown into fine ore, other powdered additional materials are known to i-shea. A plasma torch is made of a arc-arc direct current plasma torch. The burner is powered from a thyristor current converter 25. The electrical supply for the single-phase burner is schematically shown in FIG. At the bottom 20 of the converter, docking stations for oxygen supply (circumferentially) to coal dust (in the center), as well as porous blocks 27 for supplying argon, are provided for producing flexible process control. The device works next time. After loading into the converter 1 iron 28, coarse scrap metal 29 and fine scrap metal 30, the plasma torch 6 is ignited between the tip 16 of the central tungsten cathode 7 and the scrap metal 29 and 30, which is in a conductive connection, through the iron 28 with the bottom electrode 21. Plasma structure 15 melts a central cone in the scrap metal, thereby creating favorable conditions for igniting the oxygen flow leaving pipe 5. 6 When this is established, the profile of the melt 31 is established (dashed lines in FIG. 1) and immediately after ignition of the plasma torch is formed, a funnel-shaped cavity 32 in the scrap metal of the foamy or continuous lowering of the pipe 5 becomes deeper and in the radial direction wider. Heat transfer from the central plasma jet to the scrap metal takes place, without appreciable absorption through the surrounding jacket of oxygen. The temperature of the plasma string 15, depending on the plasma gas, is 5000–30000 K. Along with the ignition of the plasma torch 6, oxygen is supplied through the pipe. Due to the parallel or expanding supply of oxygen, a zone of maximum heat transfer from the plasma jet to the surrounding space is formed. Oxygen reacts where it is needed first: in the preheated plasma torch 6 scrap metal 30. After ignition of oxygen on the surface of a bath of molten iron, two melts for scrap metal occur, the distance between which decreases with melting time, i.e. The plasma arc melting center moves along the scrap metal in the direction towards the burning point 33 (reaction zone between 0 and liquid iron 28), to the area to which oxygen is supplied. The advantage of the proposed device is, first of all, that the transfer of electrically introduced energy due to the radiation of the plasma strut 15 and the generation of heat through the exothermic reaction of hot iron and / or scrap metal with pure oxygen is combined in an optimal way, which gives the application of the plasma torch 6 the shortest possible time melting Due to the injection of pulverized iron oxides through consumable pipes 24, this flow enters the plasma arc radiation region, namely, S in the region of greatest CO gas evolution. This gives the use of reducing components and reduces oxygen burning. Strong, mainly acting radially thermal radiation of plasma 1
    The variable jet 15 contributes to the very rapid heating of these additional materials. In this reduction process, metallic impurities of the pi-like iron oxides, especially zinc, are also evaporated, which can be precipitated above the bath in the area of the cooling device 34.
    The invention is not limited to the proposed embodiment, the unit may be modified. For example, additionally provide several torches, with the supply pipe 5 being surrounded radially symmetrically by several plasma torches. At the same time the melting of scrap metal
    420066
    B will be a little more, but, in principle, the same process as described.
    In addition, the supply pipe 5 may have a hinge suspension at the upper end in order to perform a circular (precessional) movement during operation. to increase the reaction zone 33, or to cause a movement of the metal bath.
    Instead of the shirt-forming openings 12, an annular gap can be provided as an outlet for oxygen.
    The technical and economic efficiency of the invention is determined by the increase in the scrap fraction in the charge.
    权利要求:
    Claims (4)
    [1]
    1. UNIT FOR PRODUCING STEEL from solid and / or liquid charge materials, in particular cast iron, coarse and lightweight scrap, containing a container for refining melt lined with refractory material, in which a plasma torch and devices for introducing additional powder materials, characterized in that, in order to increase the share of scrap in the charge, a channel for oxygen supply is made around the plasma torch, enclosed in a cooled casing, while The bottom of the vessel for refining the melt under the plasma torch has an electrode.
    [2]
    2. The unit according to claim 1, characterized in that the device for introducing additional powdery materials is made in the form of feed pipes surrounding the crown of the cooled plasma torch casing.
    [3]
    3. The unit according to claims 1 or 2, characterized in that the plasma · torch burner has a central rod-shaped electrode installed in the annular gap 'for supplying plasma gas.
    [4]
    4. The unit according to paragraphs. 1-3, characterized in that the channel for supplying oxygen is made in the form of a crown of slit-like or round nozzles.
    ί142006
    类似技术:
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    同族专利:
    公开号 | 公开日
    JPS6158524B2|1986-12-12|
    FR2518577A1|1983-06-24|
    ATA553381A|1983-01-15|
    SE8207257L|1983-06-24|
    DE3247572A1|1983-07-14|
    GB2112509B|1985-03-13|
    US4426709A|1984-01-17|
    AT372110B|1983-09-12|
    IT8224882D0|1982-12-21|
    LU84547A1|1983-06-13|
    BE895444A|1983-04-15|
    JPS58113309A|1983-07-06|
    DE3247572C2|1985-08-08|
    IT1155036B|1987-01-21|
    SE8207257D0|1982-12-20|
    FR2518577B1|1987-01-02|
    GB2112509A|1983-07-20|
    DD208826A5|1984-04-11|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    BE470715A|1960-08-01|1900-01-01|
    AT232531B|1961-10-27|1964-03-25|Voest Ag|Blowpipe for refining metals while heating the insert with adjustable heating power|
    US3316082A|1964-12-08|1967-04-25|Inland Steel Co|Oxygen steelmaking|
    US4082914A|1973-05-14|1978-04-04|Nikolai Iosifovich Bortnichuk|Method of stabilizing arc voltage in plasma arc furnace and apparatus for effecting same|
    JPS5546266A|1978-09-28|1980-03-31|Daido Steel Co Ltd|Plasma torch|AT375960B|1982-12-07|1984-09-25|Voest Alpine Ag|METHOD AND DEVICE FOR PRODUCING METALS, ESPECIALLY LIQUID PIPE IRON, STEEL PRE-MATERIAL OR REMOTE ALLOYS|
    AT376702B|1983-04-06|1984-12-27|Voest Alpine Ag|METHOD FOR OPERATING A METALLURGICAL SYSTEM|
    JPS614033B2|1983-09-09|1986-02-06|Nippon Steel Corp|
    USRE32908E|1984-09-27|1989-04-18|Regents Of The University Of Minnesota|Method of utilizing a plasma column|
    US4725447A|1984-09-27|1988-02-16|Regents Of The University Of Minnesota|Method of utilizing a plasma column|
    US4918282A|1986-01-10|1990-04-17|Plasma Energy Corporation|Method and apparatus for heating molten steel utilizing a plasma arc torch|
    US4734551A|1986-01-10|1988-03-29|Plasma Energy Corporation|Method and apparatus for heating molten steel utilizing a plasma arc torch|
    US5171491A|1986-02-04|1992-12-15|The Carborundum Company|Method of producing near net shape fused cast refractories|
    US4791077A|1986-02-04|1988-12-13|Stemcor Corporation|Near net shape fused cast refractories and process for their manufacture by rapid melting/controlled rapid cooling|
    US5177763A|1990-03-28|1993-01-05|Kawasaki Steel Corporation|Furnace bottom structure of direct current electric furnace|
    US5286277A|1992-05-26|1994-02-15|Zaptech Corporation|Method for producing steel|
    ATA121393A|1993-06-21|1998-07-15|Voest Alpine Ind Anlagen|CONVERTER AND METHOD FOR PRODUCING STEEL|
    US6125133A|1997-03-18|2000-09-26|Praxair, Inc.|Lance/burner for molten metal furnace|
    US6010658A|1998-11-12|2000-01-04|Esm Iii|Apparatus for desulfurization of iron utilizing two spaced apart lances|
    DE102006029724B4|2006-06-28|2008-12-04|Siemens Ag|Method and furnace for melting steel scrap|
    BR102015003522A2|2015-02-19|2016-08-23|Lumar Metals Ltda|metal manufacturing and refining blow boom assembly|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    AT553381A|AT372110B|1981-12-23|1981-12-23|DEVICE FOR PRODUCING STEEL|
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