• 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 furnace product is permitted to flow out by gravity from the opening defined between the lower end of a furnace wall and a furnace bottom and to accumulate on the circumferential portion of the furnace bottom with a reposing angle inherent to the product, with the accumulation being drawn out of the furnace from the circumferential portion of the furnace bottom. The furnace bottom is formed with a diameter larger than the inside diameter of the lower end of the furnace wall and vertically spaced from the lower end of the furnace so as to provide an opening therebetween through which the furnace product is allowed to pass a discharging device comprising a reciprocating raking arm with its end movable across the circumferential portion of the furnace bottom operates to remove product therefrom.
    公开号:SU991958A3
    申请号:SU772465706
    申请日:1977-03-25
    公开日:1983-01-23
    发明作者:Миясита Сатору；Танигучи Масахико；Кобаяси Кацуеси
    申请人:Ниппон Стил Корпорейшн (Фирма)；
    IPC主号:
    专利说明:

    for work on the turntable aamena when performing repairs or the like. The purpose of the invention is to prevent crushing of the discharged material and to facilitate maintenance. This goal is achieved by those that in the device for unloading material from a shaft furnace containing a hearth, whose diameter is larger than the internal diameter, the discharge elements are evenly spaced around the periphery of the bottom, the latter are made in the form of a lever having a swing in a horizontal plane with a center of rotation carried out outside the furnace. The device is equipped with the lower end of the furnace and the bottom of the cylindrical chamber and a frame detachably fixed to it through no bearing, by means of which the axis of rotation of the lever is fixed in the frame, which is connected with the drive of its swing. Work, the end of the lever is removable. The device is equipped with a telescopic skirt attached to the lower end of the furnace. Figure 1 shows the bottom of the shaft furnace, the cross-section in figure 2 the most important parts of the device, the cross-section / on fig.Z - unloading lever; FIG. 4 shows a discharging device comprising a plurality of discharging devices mounted on a shaft furnace body, in cross section. The shaft furnace 1 has shells 2 molded from a steel sheath material of a cylindrical forum. Along the inner circumference of the shell 2 there is a refractory on the wall 3. Under the lower end of the wall 3 of the furnace there is a stationary under 4 furnaces, which is rigidly supported by the beam element 5. There is an interval 6 between the lower end of the wall 3 of the furnace and the upper side of the bottom 4, which is quite large to allow easy passing of a granulated material with a size of 10-30 mm in diameter. The gap b is most preferably adjusted so as to provide a good gap around the entire circumference of the furnace. The diameter of the furnace bottom 4 is larger than the inner diameter of the lower end of the wall 3 of the furnace. The granular substance that spills out after gap 6 can accumulate in it under its characteristic ANGLE of repose (Fig. 2, dotted line). The area of the base of the cluster varies depending on the size of the gap 6. Although usually the upper side of the furnace bottom 4 is flat, the bottom 4 can be made conical in the middle part protruding upward so as to allow the granular substance to accumulate under the action of force t tin, evenly pour out. The substance to be fed into the shaft furnace from above, either in the form of granular lumps, either in a caked form or in the form of pellets, forms a layer compressed in a vertical direction, the weight of which is perceived by the furnace hearth 4. Under this condition, a part of the granulated substance placed on the furnace hearth, under the influence of gravity, pours out through the gap 6 and. thus, it accumulates at the angle of repose characteristic of the granular substance at the peripheral portion of the bottom of the furnace. Since this accumulation is outside the internal diameter of the wall 3 of the furnace, the total weight of the substance with which the internal cavity of the furnace is loaded does not directly affect the accumulation of the substance. In a discharger, the accumulated substance can generally be ejected with very little drive energy. Further, the granular matter is again accumulated at the discharge site due to gravity. The method of digging up the granulated matter from the peripheral portion of the furnace bottom 4 can be carried out by various other possible mechanisms. The proposed unloading device J which includes a plurality of unloading devices is most suitable in terms of the possibility of uniform unloading of the granulated substance, maintenance and control of the discharged quantity. In FIG. 2, the front end portion of the discharge arm 7 is located on the peripheral portion of the furnace bottom 4. The remote end of the discharge arm 7 is fixed on the axis 8; The axis is fixed, having the possibility of rotation, in the frame 9 by means of the bearing 10. The removal ring 9 is attached to the window 11, which is made in a shell that surrounds a part of the lower end of the furnace 1 and the bottom 4 of the furnace. The mechanical gap provided between the axle and the frame is closed by a sealing element 12. The lower end of the axle 8 has a drive mechanism (not shown) such as a piston cylinder connected to this end through a connecting rod 13. Thus, when the drive mechanism operates, 8 rotates, causing the discharge arm 7
    swing horizontally. If the lever 7 is designed to rotate 360 °, then such a device requires the use of large space and the use of larger frames 9. Therefore, in order to effectively solve this problem, it is preferable to unload the lever-7 so that it can swing back and forth. the limits. provided angle, for example 30.
    It is undesirable for the main part of the discharge arm and the axle to be exposed to the hot air of the furnace and granulated to the core. In order to solve this problem, the pill 9, supporting the pivot 8, is equipped with a cooling jacket 14, which is circulated by the chiller, with a goggle as cooling water.
    G - - - -.
    As the discharge lever 7 is urged to swing back and forth in a horizontal direction, the front end of the hook lever crosses the peripheral edge of the furnace bottom 4 in order to carry out the raking action (Fig. 3). Meanwhile, the granular substance accumulates at an angle of repose on the bottom. the furnace, spilling out through the gap 6 A part of a cluster of granulated material placed in the area that the discharge lever engages, as indicated by the hatching in FIG. 3, is dumped from the bottom edge 4 of the furnace with an unloading movement A granulated substance, which has been removed from the shaft furnace 1 and accumulated in this way, is transferred for further processing by means of a distribution valve 16.
    A plurality of discharge devices, each having a discharge lever 7, are located along the outer circumference of the bottom 4 of the furnace with equal gaps between them. If the unloading device includes six unloading devices (FIG. 4), it is necessary that all devices act either simultaneously, one after the other, or in some other combination. Such a device makes it possible to control the amount of granulated material that should be discharged. Six discharge devices, each equipped with a discharge lever, a frame and a drive mechanism for the discharge lever, are spaced from one another along the outer circular part of the furnace. With the help of a cesspool lever 7 adapted to swing in the horizontal plane back and forth at a given angle limit, the amount of discharge can be controlled by adjusting the length of the lever. : The discharge lever 7 is located above the bottom 4 of the furnace with a gap between them and has a length greater than the maximum diameter of the granulated matter, twice as large as the average size of the granule. Providing such a gap reduces the degree of granulation of the granular substance in the process of moving the unloading lever back and forth.
    The amount discharged can be reduced by adjusting the height of the discharge pipe 7. The position of the lever 7 can be fixed by precisely positioning the position of the axis 8 with a gasket (not shown).
    The discharge portion of the discharge arm 7 wears out as
    0 as a discharger, it continues to operate. For this reason, this section should be monitored at-intervals at a convenient time. Also . it is necessary to control the drive part, which is provided with unloading
    5 Noah 7.
    In order to facilitate such control, there is a removable cover 17 at the rear end of the frame (Fig. 2). Routine control can be done by removing the cap as needed. However, in the event of a real need to replace the discharge arm 7 of any of the devices, the damaged discharge member is removed from the housing 18 and replaced with a new discharge feature. Thereafter, the remote discharge device is repaired as needed by Mepie. In the unloading device, the wear part of the unloading lever is usually limited to the front end portion. Because of this, repair can be carried out simply by replacing only the front end portion, after its flange portion 18 has been disconnected for connection to the remote end portion.
    The configuration of the discharge arm 7 can be either circular, elliptical, or rectangular.
    0
    A shaft furnace equipped with the proposed discharge for unloading is an option for unloading high temperature granular material. In cases
    5 when it is not possible to subject the discharging device to high temperatures, the length of the discharge arm can be made shorter, with each discharging device
    0 is made so that the turning part is located closer to the granular substance or deeper inside the furnace.
    The amount of granular matter accumulated at the periphery5
    The height of the bottom of the lechi is governed by the height of the slit gap, which is assumed that the surface arrangement of the granulated substance remains unchanged, t.e. as long as the natural slope angle of a granular substance remains the same. In order to make the accumulated amount of the granulated substance adjustable, there is a skirt 20 that is vertically movable at the lower end of the wall 3 of the furnace. Thus, the accumulated amount can be adjusted by vertical adjustment of the position of the skirt 20. The physical state of the granular substance fed to the furnace is changed. If the size of the granule or the variation in the size of the granule of the supplied granulated substance does not remain the same, the accumulation of the granulated substance can be made unchanged by adjusting the position of the skirt 20.
    In the discharger, there is a gap 6 between the wall of the furnace and the bottom furnace in order to allow the granulated substance fed into the furnace to pour out through the gap b under the action of gravity. The accumulation of granulated material formed at the characteristic angle of repose on the peripheral portion of the furnace bottom 4, which has a larger diameter than the internal diameter of the furnace, is scraped by the action of the discharging devices installed separately. The accumulated part of the substance with which the furnace is loaded, for this reason, is discharged in a state where the total weight of the substance does not directly affect it. Therefore, the crushing to which the granular substance is subjected during the unloading operation can be reduced to a large extent;
    Since the discharging device has a plurality of discharging devices arranged at regular intervals along the outer circumference of the bottom. the furnace, the substance fed to the furnace is discharged in the same amount. Thus, part of the substance inside the furnace is also evenly lowered.
    Since each of the discharge devices is constituted by frame 9, removable mounting on the outer peripheral part of the bottom / recovery operation on these devices can be performed without difficulty.
    After removing the discharger for repair, the discharging lever 7 can be repaired by replacing only the worn front end portion, because the front end portion has a detachable connection with the distal end portion. This device reduces maintenance cost 5. The vertical movable skirt 20 in the lower end of the furnace wall allows you to adjust the gap b. Where the physical conditions of the granular substance are unchanged, the accumulated amount can be adjusted as desired. . the physical state of the granulated substance changes; the accumulated amount can be kept constant.
    Due to the position of the skirt, the length of the discharge arm, the vertical position of the portion of the front end of the lever over the hearth 4 furnace, the number
    0 discharge devices that will work, etc., the discharge devices are configured to control the large amount of the discharged amount of the substance.
    权利要求:
    Claims (4)
    [1]
    1. A device for unloading material from a shaft furnace containing
     a hearth whose diameter is larger than the internal diameter of the furnace, and discharge elements evenly spaced around the periphery of the hearth, characterized in that, in order to prevent crushing of the material being discharged and facilitate maintenance, the discharge element is designed as a lever with swing in the horizontal plane with a center rotation outside the oven.
    [2]
    2. A device according to Claim 1, characterized in that it is provided with a cylindrical chamber which encloses the lower end of the furnace and the bottom of the furnace
    [3]
    and a frame detachably attached to it with a passage through the non-bearing, by means of which the axis of rotation of the lever is fixed in the frame, is connected to its swing drive. 3. The device according to claim 2, about the fact that the working end of the lever is made removable.
    [4]
    4. The device according to claim 1, which is equipped with a telescopic skirt attached to the lower end of the furnace. Sources of information taken into account in the examination
    -one. Japanese patent 4899020, Q class. F 276 1/20, 1973.
    2. Patent of the USSR 5621, cl. F 27 E. 1/20, 1926 ..
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    同族专利:
    公开号 | 公开日
    JPS52116706A|1977-09-30|
    CA1071864A|1980-02-19|
    BR7701886A|1977-11-29|
    GB1574451A|1980-09-10|
    IT1075749B|1985-04-22|
    US4129289A|1978-12-12|
    AR211889A1|1978-03-31|
    IN146503B|1979-06-23|
    MY8500122A|1985-12-31|
    AU509030B2|1980-04-17|
    AU2347877A|1978-09-28|
    JPS5612784B2|1981-03-24|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE449985C|1926-07-11|1927-09-29|Atg Allg Transportanlagen Ges|Device for scraping the vorboeschenden material from large bunkers|
    GB445601A|1935-01-30|1936-04-15|Fritz Ludewig|Ore roasting furnace|
    US2626482A|1948-09-07|1953-01-27|Richard B Munday|Apparatus for irrigation|
    US2602670A|1950-03-04|1952-07-08|Burkart William|Feed spreader|
    US2709537A|1950-05-15|1955-05-31|Chain Belt Co|Feeding apparatus for belt conveyers and the like|
    GB725906A|1952-09-17|1955-03-09|Duisburger Kupferhuette|Improved roasting furnace|
    US3580717A|1967-09-22|1971-05-25|Mikhail Ivanovich Kononov|Method of obtaining a spongy metal ingot in a shaft furnace|
    US3594122A|1969-07-28|1971-07-20|Ethyl C Fornes|Process for extraction of alumina from alumina-containing ore|US4205831A|1979-04-04|1980-06-03|Hylsa, S. A.|Ore reduction reactor discharge regulator|
    US4897113A|1985-09-23|1990-01-30|Hylsa, S.A.|Direct reduction process in reactor with hot discharge|
    US5296015A|1990-01-09|1994-03-22|Hylsa S.A. De C.V.|Method for the pneumatic transport of large iron-bearing particles|
    US5447550A|1994-09-21|1995-09-05|Hylsa S.A. De C.V.|Method and apparatus for the pneumatic transport of iron-bearing particles|
    US6221123B1|1998-01-22|2001-04-24|Donsco Incorporated|Process and apparatus for melting metal|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    JP3324276A|JPS5612784B2|1976-03-26|1976-03-26|
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