• 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:
    The invention relates to ferrous metallurgy, and more specifically to installations for the continuous loading of a steel-smelting unit with solid material and preheating of this material by means of heat exchange with gases formed during the production of steel from iron in a converter. The purpose of the invention is to increase the intensity of heating of a solid material by ensuring its uniform progress. The installation allows you to continuously load the reactor 1 with solid material and heat this material by heat exchange with the gases coming from reactor 1. The solid material 2 is introduced into the heating chamber 3 having an outlet 5 placed above the converter 6 hot gas outlet 6 the solid material to the outlet 5, the hot gases coming in from the reactor 1 are sucked in to circulate these gases through the solid material 2 in countercurrent with respect to the direction of movement of the solid material. The heating chamber 3 is configured to be horizontally displaced to the position of alignment of the outlet openings of the heating chamber and the steelmaking unit. In addition, two-stage bunkers 22-26 are located above the opening 4 for loading materials into the chamber 3, each stage of which is closed by a hatch 27. 5 z. P. f-ly, 9 ill.
    公开号:SU1611219A3
    申请号:SU853872001
    申请日:1985-03-27
    公开日:1990-11-30
    发明作者:Литшинко Катрин；Литшинко Игорь；Литшинко Виктор
    申请人:Катрин Литшинко, Игорь Литшинко и Виктор.Литшинко (FR)；
    IPC主号:
    专利说明:

    Invention (The concept of qepHoii metallurgy, more specifically, the installation of a triplet for non-conventional metal and metal, an aggregate of solid, materials and heating of these materials, heat and heat, iai1) imer. -1m gases formed by liri iroiz; i5let e etali from luguna n converter.
    Purpose And eoboteli - fox lpee and 1 Noeti nugreglt 1L Erd; | 1x materials by not even uniform.
    ; 1a of FIG. 1 c; hematology nocase. proposed uetanok 1, sheathed the view from the I vny; pro / tlny;) ozzrezo, cha fig. 2 - the same, v / g. eve;) xy ,, yia fig. 3 - section LL ha fig. one; in fig. 4 - section bb ha .rig. one; cha
    5 - section bb ha-lig. one ; on
    6- cross-section of D-H ha (hf. 1; on
    7-section D- / ilinr. :;
    8-section Е-К on |} и1г. ; ;
    9- section Ж-Ж на ф1. one . Installation for non-translational
    Converter 1 ekraiom 2 l lologa rela this ekraia by heat exchange with hot gases, which are located on the converter 1, has a chamber 3 heating.1, containing the top points: TL (4 packs of scrap and lower than 5 units) loads of this ekrapa, ralcheschechloe fret exhaust hole 6 oor chlh gazvt converter 1 so that this is hot ;; gases can lro} L1kat1, in stone. 3
    There are envisioned1; a for transferring scrap 2 between the hatching hole and the discharge chamber from chamber 3 and to create between this: kraps1m and the exhaust surface of the exchange surface.
    The heating chamber 3 has openings (out (5la g aow, and x xpertefig, fig. Fig. Fig. Fig.,
    0
    five
    0
    five
    0
    five
    0
    five
    rum 1, located opposite the opening 5 of these gases under the texture of 4 l of scrap loading 2, so that these 1, 1, slightly crossed, lick npoTFtBOTOKOM (eagle keys in figure 1); .
    Inside the converter 1, the circuit breaker: l1e: cho coating 8 I - an accessory material, inside the chamber 3 there is provided a coating 9 of refractory material.
    Honeycomb okay t liepxiiee a hole for loading hamer 3 is mixed relative to the bottom: about the outlet 5 in the direction (the movement of the flare is 11L 2. JTO is the displacement between the two holes h and -, so that the solid 2 forms between; i .paeM openings 4 for loading and the top edge of the outlet 5 I3TKOC; i as a top for interconnecting-1 dHell gases.
    n;, dull about virtue 5 of chamber 3 has a surface that is extended downward
    O, the free edge of which is located at a certain distance from the outlet–– openings of the 6 gases of the converter 1. (H) Razrovana1lee thus space- (llch) no3Boj: 4eT to create air circulation (arrows ha fig.) For suction 1 gas or air in the direction of the heating chamber 3. The cross section of the outlet 3 of the chamber 3 is smaller than the cross section of the outlet (L o screw the 6 hot gases of the converter 1. Along the axis of these openings 5 and 6, an oxygen lance 11 is installed, which is oxygen in the flask 1 in the converter 1 3 Particular: a beam of acid purging; ioM from above.
    The upper wall 13 of the chamber 3 has in the zone between the upper filling opening 4 and the lower outlet (with a curvature of 5, inclined downward
    five
    the surface that connects to the pusher hole 5 through the curved surface 14.
    The outlet 7 of the gases of the chamber 3 is covered with a grill starting from the bottom 15 of the chamber 3 and having a slope markedly identical to the inclination of the surface formed by the slope of scrap 2. In addition, the bottom 15 of the chamber 3 can be tilted towards the bottom outlet 5. This slope changes depending on the characteristics of the scrap used 2.
    Referring to FIG. 1, section 1), chambers 3 are movable on rollers 16 or sliders mounted on a horizontal or inclined rolling surface 17, movable in the general direction of movement of the scrap 2. The end of this movement corresponds to the position at which the outlets 5, 6 of the chamber 3 and converter 1 are located one above the other. This position is determined by the fixed stop 18 and the movable stop 19- fixed on the bottom 15 of the chamber 3. For advancing the chamber 3 to the fixed stop 18, means such as a pusher 20 abutting are provided to collide this compartment when contacting the two stops 18, 19 to the fixed part 21. In addition, this pusher 20 allows the camera 3 to return to its original position. Above the opening 4 of the compartment loading 3 two-stage hoppers 22-26 are installed containing solids of different composition. At each stage there is a hatch 27 operating independently of the hatch of the other step.
    In the example shown, the first hopper 22, adjacent to the bottom edge of the 16
    10 chambers 3 capacity 46
    The openings 4 contain lime to collect accidentally fallen scrap. 28, the next hopper contains oil. On the other hand, this tank serves as a scraper 29, and the other bins to close the outlet 10 contain a conventional scrap 2. Each of —Camera 3, when not in use, has two hatches 27 of each stage of the hoppers 22-26. action of the pusher 30 (Fig. 6 and 7) for discharging a solid into chamber 3. Continuing the vertical walls, the section -) solid hoppers 22-26, under the sliding
    50
    installation.
    The installation works as follows.
    In the initial MON eHT, the outlet 5 of the heating chamber 3 is centered with the outlet of the convertible
    55
    gaskets 31 are installed divider 1, and the container 46 is separated (figure 1)
    ki 32 that penetrate the solid
    substance and prevent passage
    gases above scrap 2. Between the bottom
    part bunkers 22-26 and top edge
    loading opening 4 installed
    The lance 1 1 is lowered, the purge and at the same time the exhauster 37 begin to suck in the gases of the converter 1 and the surrounding combustion air. The intake air volume is regulated
    ,
    ten
    П2196
    gaskets 31 (Figs. 1 and 5), which ensure tightness between the various bunkers 22-26 and the interior of chamber 3, allow the latter to move relative to the bunker.
    An inclined grate for closing the opening 7, through which gases are discharged from chamber 3 after passing the scrap 2, is connected to a device for cleaning these gases. This device contains a pipe 33 installed hermetically slidable in
    15 to a pipe 34 by means of an annular gasket 35 (Figs. 1 and 9), wherein the pipe 34 is connected by a gas cleaning unit 36, at the outlet of which there is an exhauster of 37m gases which directs
    20, these flue gases into the exhaust pipe 38. The volumes of the flue gases, the passage of gas through the pipe 33, are controlled by the rotating trimmers 39 superimposed on each other, controlled by serums 40 engines (Figs. 1 and 8). A rotary trimmer 41 is installed at the bottom of the exhauster 37 to adjust the main volume, driven by a servomotor 42 (FIG. 2). The bottom 15 of the chamber 3 has a hole 43 above the outlet 5, which is equipped with a chamber 44 for collecting colored materials, melting at an average melting point of scrap in this place. - To facilitate the removal of these fusible materials, grooves 45 (Fig. 4) are made in the oFFieynopHOM coating through both sides of the hole 43
    9 bottom chambers 3. These cut-outs are made at a sufficient height of the side walls of the chamber 3. In addition, next to the extended exhaust surface
    10 chambers 3 capacity 46
    thirty
    35
    40
     for collecting accidentally fallen scrap. On the other hand, this container serves to close the outlet 10 of the chamber 3 in the off position
    for collecting accidentally fallen scrap. On the other hand, this container serves to close the outlet 10 of the chamber 3 in the off position
    installation.
    The installation works as follows.
    In the initial MON eHT, the outlet 5 of the heating chamber 3 is centered with the outlet of the convertible
    tera 1, and the container 46 is separated (figure 1)
    tera 1, and the container 46 is separated (figure 1)
    The lance 1 1 is lowered, the purge and at the same time the exhauster 37 begin to suck in the gases of the converter 1 and the surrounding combustion air. The intake air volume is regulated
    , so that the flue gases are neutral vibiMH pa v chodo ustlshkn. In this case, the installation of the Naholits p worker g; o-, Yuzhen AI,
    Dsbanlanyu 1 tick 2 if etsgo requires or utilizes the temperature of the panel 12. For one; 1, they are merged: (ayut: sammera 3 to the right (Fig. 1) so that the outlet 5 is eternally distributed 6 klg-werter I. This is a fast moving relatively | --1sleep and around-the-pusher pusher 20 or similar pro-wollow: m pusher. Then quickly move the hamer 3 to the left using the pusher 20. As soon as the outlet 5: amers 3 deactivate the crust with a vent hole of the converter, oetr, -: -jaBJiHEaiOT move it1; not with a mobile phone 18. IIoji, by the action of this stop, he cracked the 2nd pr, by the inertia of Lerelezatie, and falls under the force of gravity of the converter 1. The additional quantity of scrap can be settled either by the frequency of the blows or by their intensity, oo Oh:: 1 time: to these two factors.
    The movement of the movement of the scrap 2 can be done for the small installations by connecting the utility chamber 3 with a flexible system or using a system with the cyclic horizontal component of a single camera 3 for a resonant: choker: second movement. 5 ets. In the case of the inertia of scrap 2, a loss of speed of chamber 3 occurs and as a result of the fact that scrap 2 can move only) skid: the slope of the bottom 15 of the moving chamber 3.
    In the example shown, the chamber 3 is loaded with cold scrap 2 from stationary bunks. 22-26 to reduce the transfer weight: However, bins B can also be seen as partitions 32, which are integral with chamber 3.
    The proposed installation can be used at 1TLOEVS; from cast iron - in converters; (1p (blown from the top or bottom. This unit can also be used for the installation of production furnaces, as well as; any reaction-, HcnycKaiOQieM gas containing heat (a certain heat-fined-orejTi-in) that can be heated by solid things 1121
    five
    five
    0
    You can return to hot as 1 reactor.
    Media for moving scrap can be changed or replaced by other means, for example a movable wall mounted behind the scrap and driven to move the scrap in the direction of the outlet of the compartment. In addition, means l can be provided: 1 to overturn a compartment to increase the slope of the bottom of the compartment.
    The device according to the invention makes it possible to carry out a thermal river for more than 90% while simultaneously loading the solid substance into the reactor in the form of hot melt introduced into KotiBepTep during the production of steel.
    In this case a lawsuit: losses are lost; 1 time for loading the scrap outside the period-; i, a oxygen blowing, as well as significant cooling of the coolant during loading (the scrap is mainly loading- C ts simultaneously; O1 with cast iron) with all the ensuing mi: more med- ula: 1a reaction and more irregularity in time. At the same time, several changes in growth, growth; 1 load of mountains — H: C Cpanrij can positively,.; Act1, i; a;
    pocht- radio; 1-1 ;; medden; 1o returns .chachuyu energy from which it was on: guche; 1a; The amount of scrap used in metal1; 1xte | The amount of dust entering the gas purification unit is significantly reduced, as dust accumulates in the | - scrap and returns continuously to the coke: ter.
    In addition, since the installation allows e / g to efficiently capture the thermal energy of the exhaust gases, it is possible to use only cyxyi ;; gas cleaning, while excluding the wet one, moreover, continuous modulation of the materials forming the plug, permeable to the length of the gas, which functions reliably, despite the temperature of the exhaust gases, is ensured continuously. . f p m u l and inventions
    权利要求:
    Claims (1)
    [1]
    I. Installation for continuous charge. became the heat of VIL1P1OHO; i gregata
    solid material and its heating by (heat exchange with hot gases from the unit, containing a heating chamber with an upper opening for loading solid material offset from the lower outlet opening for unloading it into a steelmaking unit, which is connected to the hot gas outlet a steelmaking unit, means for transferring solid material between the upper and lower holes of the heating chamber, the grill-closed opening of the gas outlet from the heating chamber, located opposite in the openings for entry of hot gases and connected with- flue for discharging flue gas cleaning, exhauster organizing venting so that they extend to meet the direction of movement of solid material, wherein those that, in order to increase
    .The intensity of heating of a solid material by ensuring its uniform advancement, it is provided above the opening for
     loading a solid material with two-stage bunkers, a chamber for collecting molten materials, fixed on the heating chamber with a movable stop and a fixed stop, means for ensuring the chamber is pushed to the stationary stop and means for returning the camera to its original position, and the heating chamber is horizontal in position aligning the outlet openings of the heating chamber and the steelmaking unit.
    Q 2, Installation according to claim 1, characterized in that the outlet of the heating chamber is located with a gap above the opening for the exit of hot gases of steelmaking
     unit and expanding downwards.
    3. The installation according to claim 1, wherein the grating for closing the opening for exiting
    The Q of exhaust gases from the heating chamber is set at an angle to its bottom.
    4. Installation on PP. 1–3, which is associated with the fact that each stage of a two-stage bunker is closed by a hatch, and dividing partitions are made in their lower part.
    5. The installation according to claims 1–4, about 10 and 10 hours, so that the chamber for collecting molten materials is installed under the bottom of the heating chamber near the hole and communicated with the heating chamber by means of holes.
    eleven
    58
    16 53
    2
    Aa
    b b
    FIG.
    YYY
    29 23
    eleven
    23
     х х “,, у У У i h
    Ty l-: -
    Fig-6
    7E
    FIG. five
    Dd
    FIG. 7
    HER
    0
    P
    D
    FIG. eight
    FIG. 9
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US2247823A|1937-08-09|1941-07-01|Budd Wheel Co|Process of making metal for castings|
    FR1138829A|1954-10-08|1957-06-20|Oesterr Alpine Montan|Process for the use and purification of gases given off by refining cast iron baths or other iron baths containing carbon|
    GB933353A|1960-12-08|1963-08-08|Consett Iron Company Ltd|Improved metallurgical apparatus|
    FR1331339A|1961-09-06|1963-07-05|South African Iron & Steel|Process and plant for the preparation of steel and for other iron refining operations|
    FR1312160A|1961-12-19|1962-12-14|Calderon Automation Inc|Improved process and equipment for steelmaking|
    US3301662A|1962-12-10|1967-01-31|Mcdowell Wellman Eng Co|Basic oxygen steel making process|
    US3234010A|1962-12-31|1966-02-08|Harold A Mahony|Apparatus and process for high speed scrap smelting|
    FR1401905A|1963-07-24|1965-06-04|Rheinische Stahlwerke|Process for operating chamberless melting furnaces, intended in particular for melting steel, and installation of melting furnaces for the implementation of this process|
    FR1387077A|1963-10-22|1965-01-29|Method and installation for increasing the share of solid agents in the feeds of scrap, solid pig iron, ore, shot, iron sponge and other cooling agents in the manufacture of steel, in particular of steel. after the oxygen insufflation process, using the heat of the exhaust gases|
    FR1434287A|1965-02-23|1966-04-08|Siderurgie Fse Inst Rech|Heating process for pre-reduced products|
    US3425676A|1965-09-30|1969-02-04|United States Steel Corp|Molten metal producing furnace|
    DE1508297A1|1966-05-24|1969-10-16|
    ES341821A1|1966-06-16|1968-07-01|Koppers Co Inc|A method for manufacturing steel. |
    FR1494536A|1966-09-26|1967-09-08|Voest Ag|Fixed reaction vessel, comprising a refractory lining, and steelworks installation with such a reaction vessel|
    US3533612A|1966-12-28|1970-10-13|Sunbeam Corp|Steel making apparatus including scrap preheater|
    FR91683E|1967-01-17|1968-07-26|Voest Ag|Fixed reaction vessel, comprising a refractory lining, and steelworks installation with such a reaction vessel|
    DE1804098A1|1967-10-23|1969-07-03|Krupp Gmbh|Method and device for preheating scrap for electric arc furnaces|
    JPS5147135B2|1972-10-11|1976-12-13|
    JPS5626684B2|1976-04-13|1981-06-20|
    JPS5747247B2|1979-11-22|1982-10-08|
    FR2498309B1|1981-01-20|1986-04-11|Clesid Sa|ELECTRIC OVEN FOR SCRAP MELTING AND CONTINUOUSLY SUPPLIED|
    DE3219984C2|1981-05-30|1989-03-30|Daido Tokushuko K.K., Nagoya, Aichi, Jp|US5073607A|1989-09-15|1991-12-17|E. I. Du Pont De Nemours And Company|Polyimide compositions containing polyorganosiloxane for improving atomic oxygen resistance|
    FR2652411B1|1989-09-28|1994-12-16|Siderurgie Fse Inst Rech|
    AT404842B|1992-10-19|1999-03-25|Voest Alpine Ind Anlagen|METHOD FOR CONTINUOUSLY MELTING SCRAP|
    JP2861794B2|1994-03-18|1999-02-24|日本鋼管株式会社|Melting furnace with raw material preheating tank|
    EP0772015B1|1995-03-31|2001-06-13|Nippon Steel Corporation|Method and apparatus for preheating and melting scrap|
    US5785737A|1997-04-08|1998-07-28|Bethlehem Steel Corporation|Method for recycling iron bearing sludges in a steelmaking operation|
    US6306337B1|2000-02-22|2001-10-23|General Kinematics Corporation|Nosepiece for directing a charge into a furnace|
    US6383250B1|2000-04-28|2002-05-07|Bethlehem Steel Corporation|Steel making revert and process for preparing|
    JP4828211B2|2005-11-25|2011-11-30|新日本製鐵株式会社|Steelmaking method and refining equipment for steelmaking|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR8404827A|FR2562222B1|1984-03-28|1984-03-28|INSTALLATION AND METHOD FOR CONTINUOUSLY LOADING A REACTOR IN SOLID MATERIAL AND HEATING THE SAME WITH THE GAS EMITTED BY THE REACTOR|
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