• 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 process and apparatus (14) for preheating glass batch ingredients using a heat exchange method that employs a tumbling particulate medium heated e.g. by furnace exhaust gases. The heated batch may then be fed to a glass melting furnace.
    公开号:SU1243618A3
    申请号:SU823426512
    申请日:1982-04-26
    公开日:1986-07-07
    发明作者:Морайс Хоумэн Чарльз；Альберт Пропстер Марк；Сенг Стефен
    申请人:Оуэнс-Корнинг Файберглас Корпорейшн (Фирма)；
    IPC主号:
    专利说明:

    2. A device for preparing the glass melting mixture, containing a rotating drum installed at an angle to the furnace with a charge loader mounted above its upper part, and a coolant supply pipe connected to its lower part, in order to heat exchange, it is equipped with a heat exchanger for heating the heat transfer medium in the form of spheres, the lower part of which is
    The invention relates to glass industry, in particular to technology and devices for the preparation of the charge for melting glass.
    The purpose of the invention is to increase the efficiency
    efficiency of heat transfer.
    The heat carrier formed on the basis of glass, ceramic, steel, stainless steel, aluminum, gravel or similar materials agglomerates is fed to a heat exchanger where it is preheated with gases leaving the furnace.
    The heated heat exchanger in the form of spheres G with sizes larger than the charge granules is introduced into one end of a cylindrical drum, rotated on an inclined axis. The mixture to be preheated is fed oppositely by introducing it from the other end of the drum. The coolant is used in order to ensure the heating of the charge. The cooled coolant is recycled back to the hopper, and the preheated charge enters the kiln.
    Figure 1 shows the flow sheet of the device; Fig. 2 shows a rotary drum heat exchanger; Fig. 3 shows a stretched metal coil that is used to remove the medium from the drum; Fig. 4 is the same that is placed in a rotary drum heat exchanger; Fig. 5 shows the mixing profile inside the drum.
    The heat carrier may be heated by off-gas; when the gas flue is connected to the furnace, the drum is made in the lower part perforated with holes larger than the granule size, but smaller than the size of the spheres, and provided with longitudinal partitions attached to its inner surface and a perforated spiral in the upper part than the size of the spheres, but larger than the size of the granules, and the area of the holes is not less than 70% of the spiral.
    Reratz 482-667 0, obtained from a glass melting furnace (not shown), in a pre-heated hopper. Waste is more gas is introduced into the lower part
    pre-heated hopper 1, and the coolant enters the top of this heated hopper. The flow of gases and the coolant go towards each other. The coolant exits through the bottom of the preheated bunker 1, and the waste gas -1e-gases are removed from it through the top of the bunker 1. The blower or fan 2 is designed to remove the exhaust gases from the preheated bunker in order to cope with bunker negative pressure. Heat carrier can be
    heated to a temperature equal to or close to the flue gas temperature.
    The coolant then flows to one end of the drum 3 heat exchanger along the conveyor 4. In the opposite direction, using conveyors 5 and 6 and a screw loader (not shown), load the batch to produce glass that comes in the form of microparticles transported from storage 7. The drum 3 rotates around the axis using an engine and: drive systems (not localized).
    The centrally located and permanently installed inlet 8 and outlet 9 nozzles communicate with the inner space of the drum. After the coolant is discharged from the drum, it returns to the preheating bunker 1 via the conveyor 10. The charging mixture enters the glass melting furnace as stream 11.
    The heated coolant enters the drum 3 through conduit 12 and the charge is heated through screen 13. The cold charge enters through conduit 14, and the coolant is discharged through conduit 15. Rotation of the drum and bulkheads 16 causes the heat transfer fluid and the charge to move. The drum has a sharp angle with a horizontal line, not exceeding 45 ° and not less than 15 °.
    In order to bring the mixture into direct contact with the coolant, partitions attached to the inner surface of the drum are used as a structural element. Bulkheads
    16 constructively fulfilled each
    in the form of a sequence of partitions (the number of which varies from 3 to 4) located nd the circumference of the drum. The width of these barriers is 5.1 to 7.6 cm. Typically, these barriers are bolted to the walls of the drum and protrude along its entire length. All installed partitions in combination with the rotation of the drum contribute to the mixing of the charge and coolant.
    Stretch Metal Spiral
    17 contains about 70% of holes or voids. The size of the hole in helix 17 is very important, since these holes must be large enough to allow the charge to fall through. Usually the holes have a shape similar to diamond,
    and their size is 2.54-1.91 cm. As the helix 1 rotates, the medium moves in a spiral trajectory from the section formed by the cylindrical wall of the drum to the outlet for the heat transfer fluid, which is usually
    in the middle part or in the center of the baraba- ..na. Spiral. Attached to the drum
    and rotates with it, forcing the coolant to move in a spiral path along the spiral to its center. The charge, if any, falls through the voids back into the interior.
    drum, while eliminating the possibility of its removal when discharging coolant. A screw loader (not shown) usually extends beyond the 5th place of unloading from the helix, so that the charge does not fall on the helix.
    The dimensions of the helix 17 can vary within very wide limits. The coil 10 used in this case has dimensions of 50.8x254 cm, the depth of the drum being 30.5 cm. The inner coil of the spiral has a radius of 10.2 cm, and the following coils have a radius of 17.8 and 25.4 cm, respectively .
    The proposed device for preheating contains a rotating drum, from each end of which a heated coolant and a charge flowing in countercurrent are fed inside. At the input end, where the coolant is loaded, a screen is provided, which reflects back the heated mixture. The coolant flows 5 on top of the inlet for the charge at the inlet end of the drum, through which the charge is introduced into it. To check the countercurrent characteristics of the coolant charge and charge, use the cold Q model. For this, a drum having dimensions of 50.8 and 254 has been manufactured. The mixture is passed through this drum at a speed of 272.16 kg / h with a minimum residence time of 2.5 minutes and a maximum residence time of up to 7 minutes. At any given time, the drum contains at least 27.2 kg of load.
    . Other test options were carried out. During which the load is passed through the drum at a speed of 463.59 kg / h, and the load weight is in the drum, in this case reaches 45.4 instead of 27.2 kg.
    Glass beads are used as the actual medium, the charge is introduced in the form of granules. Usually at any given time in the drum is 227 kg of balls.
    The table shows the data obtained using the cold model for the coolant and the charge.
    five
    0
    five
    The tests are carried out with both spherical and non-spherical 55 agglomerates of various sizes. During these tests, it was established that the medium is spherical and slightly different in diameter.
    , in order to eliminate the problems associated with the flow of charge and coolant. Preferably, the mixture has a form factor whose value is in the range of 0.9 - 1.0. The heat carrier with a good fit has a diameter value that is within wide limits, but the optimal size corresponds to approximately 2.54 cm in diameter.
    Such tests are carried out on heating from bodies,
    The carrier, in turn, heats the mixture to 388 ° C with a heat transfer coefficient reaching over 90%.
    When implementing the proposed method, it is possible to pre-heat any batch of blend
    using heat-transfer fluid heated to 427 C. Heat transfer, on the basis of which it manufactures bottle glass or container glass, window glass, etc.
    q) uz.l
    fig.Z
     fР 7
    17
    F1 / gA
    Editor G. Volkova
    Compiled by T, Poster
    Tehred L.Oleynik Proofreader S.Cherni
    Order 3721/59 Circulation 457 Subscription VNIISH USSR State Committee
    on inventions and discoveries 1.13035, Moscow, 1-35 Raushsk nab ,, d.4 / 5
    Production and printing company, Uzhgorod, Projecto st., 4
    FIG. five
    权利要求:
    Claims (2)
    [1]
    1. The method of preparing the mixture for melting glass in the furnace by preliminary melting the granular mixture in a rotating drum with. by the power of the heat carrier supplied in countercurrent, characterized in that, in order to increase the efficiency of heat transfer, spheres heated with gases leaving the furnace with dimensions larger than the charge granules moving in a drum in a spiral are used as heat carrier.
    1978.
    USSR copyright certificate No. 66444, cl. C 03 B 5/12, 1940.
    J
    5U_. 1243618 AZ
    [2]
    2. A device for preparing a charge for glass melting, comprising a rotating drum mounted at an angle to the furnace with a charge loader mounted above its upper part, and a coolant supply pipe connected to its lower part, characterized in that, in order to increase heat transfer efficiency, it is equipped with a heat exchanger for heating the heat carrier in the form of spheres, the lower part of which is connected to the furnace flue, the drum is made in the lower part perforated with holes larger than the size of the granules, but smaller, cm sizes of spheres, and is provided attached to the inner surface of longitudinal baffles and perforated at the top of the spiral, the dimensions of which apertures is less than the dimensions of the spheres, but larger than the dimensions of the granules, and the area of the apertures is no less than 70% of the area of the helix.
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    同族专利:
    公开号 | 公开日
    FI812484L|1982-02-28|
    WO1982000634A1|1982-03-04|
    DK185282A|1982-04-26|
    DE3163380D1|1984-06-07|
    AU7379781A|1982-03-17|
    JPS57501279A|1982-07-22|
    BR8108759A|1982-07-13|
    US4319903A|1982-03-16|
    ZA814752B|1982-08-25|
    AU548495B2|1985-12-12|
    EP0046630B1|1984-05-02|
    JPS6047210B2|1985-10-21|
    EP0046630A1|1982-03-03|
    AT7290T|1984-05-15|
    CA1166849A|1984-05-08|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    RU2547182C2|2012-06-08|2015-04-10|Общество с ограниченной ответственностью "Эффективные инженерные решения"|Preheating of mix in production of mineral wool fibres from rocks and device to this end|US2592783A|1946-04-17|1952-04-15|Aspegren Olof Erik August|Rotary heat exchanger|
    US2872386A|1952-04-14|1959-02-03|Oil Shale Corp|Heat-treatment of piece-shaped material|
    CH412952A|1964-07-27|1966-05-15|Buss Ag|Rolling element-filled heat exchanger and method of operating the same|
    LU48378A1|1965-04-12|1966-10-12|
    JPS49324B1|1967-08-14|1974-01-07|
    US3953190A|1973-08-06|1976-04-27|Pullman Incorporated|Pellet preheating and volatile recycling structure for glass making furnace|
    US4119395A|1975-09-27|1978-10-10|Central Glass Co., Ltd.|Method of recovering heat of combustion waste gas arising from glass tank furnace|
    LU78447A1|1976-11-12|1978-02-16|
    US4207943A|1979-03-28|1980-06-17|Oros Company|Countercurrent solid-to-solid heat transfer apparatus and method|US4409011A|1980-08-27|1983-10-11|Owens-Corning Fiberglas Corporation|Preheating glass batch|
    US4425147A|1980-08-27|1984-01-10|Owens-Corning Fiberglas Corporation|Preheating glass batch|
    US4386951A|1980-08-27|1983-06-07|Owens-Corning Fiberglas Corporation|Method and apparatus for preheating glass batch|
    US4422847A|1981-12-28|1983-12-27|Owens-Corning Fiberglas Corporation|Preheating glass batch|
    US4778503A|1981-12-28|1988-10-18|Owens-Corning Fiberglas Corporation|Method and apparatus for preheating glass batch|
    US4401453A|1982-04-30|1983-08-30|Owens-Corning Fiberglas Corporation|Preheating glass batch|
    US4478627A|1982-07-16|1984-10-23|Owens-Corning Fiberglas Corporation|Recuperation of heat absorbent media to preheat combustion gases and glass batch|
    US4441906A|1982-10-28|1984-04-10|Owens-Corning Fiberglas Corporation|Method of preheating glass batch|
    US4530166A|1984-02-27|1985-07-23|Owens-Corning Fiberglas Corporation|Preheating particulate material|
    US4565562A|1984-12-24|1986-01-21|Owens-Corning Fiberglas Corporation|Two-stage heating media feeder for a glass batch preheating drum|
    US4592723A|1984-12-24|1986-06-03|Owens-Corning Fiberglas Corporation|Process for reusing scrap glass|
    US4615718A|1985-07-05|1986-10-07|Owens-Corning Fiberglas Corporation|Heating of heat transfer media|
    US4707175A|1985-12-23|1987-11-17|Ppg Industries, Inc.|Method of preheating pulverulent batch material|
    US4853024A|1988-05-17|1989-08-01|Owens-Corning Fiberglas Corporation|Scrap recovery apparatus|
    JPH10101341A|1996-10-02|1998-04-21|Seiji Sakae|Method and device for preheating glass material|
    CN102351401B|2011-08-06|2013-04-24|蚌埠玻璃工业设计研究院|Flue gas preheating apparatus for glass batch|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US06/181,589|US4319903A|1980-08-27|1980-08-27|Method and apparatus for preheating glass batch|
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