• 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:
    Minerals such as gypsum in powdered condition are calcined with increased thermal efficiency in a vessel having a lower region of small cross section by means of hot gas delivered by a downwardly extending tube directly into the lower region of the vessel. The preferred vessel is an inverted cone (1) and has a lid (3) which is fitted with a mineral inlet (4) and exhaust outlet (5), and through which the hot gas tube (6) passes. The hot gas may be produced in the tube by a burner (17). Discharge from the vessel is preferably through an overflow weir (11) and an internal protuberance (15) may be used to assist in distributing the gas flow across the bottom of the vessel to avoid accumulation of calcined material, <IMAGE>
    公开号:SU1232136A3
    申请号:SU802865904
    申请日:1980-01-07
    公开日:1986-05-15
    发明作者:Джордж Терри Вард Артур；Тодд-Дэвис Кристофер
    申请人:Бпб Индастриз Лимитед (Фирма)；
    IPC主号:
    专利说明:

    ". one
    The invention relates to a device for the heat treatment of minerals, in particular gypsum.
    The purpose of the invention is to intensify the heat treatment of gypsum.
    The drawing shows the proposed device, a longitudinal section.
    The device contains a tank 1, made in the shape of an inverted cone with a rounded bottom 2, a cover 3, equipped with a feed pipe 4 for the material to be baked, an exhaust pipe 5, connected to the dust collector, and a gas supply pipe 6 installed vertically and tank 1, which reaches to the bottom 2. The feeding tube 4 is provided with a rotary feeder 7 connected to a gypsum bin 8. The container is made with lining 9. The material in the tank f reaches level 10. The discharge opening is made in the form of an overflow threshold 11 connected to the convex pipe 12. The gas supply pipe 6 is open at the lower end 13 and is made with symmetrically arranged openings 14 for distribution hot gases in the calcined material. In the bottom 2, there is a conical protrusion 15 placed under the opening of the gas supplying pipe 6 and contributing to the further distribution of hot gases in the calcined material.
    The device works as follows.
    32136-
    Fuel gas is supplied through pipe 16 and a gas burner 17 located in the gas supply pipe 6 at about 10 of the material.
    5 Air is supplied to the burner 17 through the air tube 18 by the fan 19. The air-fuel mixture ignites with the spark probe 20, then enters the open end 13 and through the holes 14 into the calcined material. In the bottom 2 there is a bottom closure 21 provided with a valve and used to clean the container and unload the product in case of accidents. The material is supplied by the rotary feeder 7 through the feed tube 4. The presence of the conical protrusion 15 in the bottom 2 allows the upward flow of solids to the bottom for circulation, which ensures the mixing of the entire mass of material and efficient heat transfer from the gases.
    In order to increase the dust separation 25, the upper part of the tank can be cylindrical.
    Material liquefaction due to supplied gas or self-burning
    The use of separated vapors ensures efficient mixing of the material and heat transfer and, during continuous operation, facilitates unloading of the calcined product without the use of a stirrer, which allows saving electric power.
    21
    sixteen
    Editor A. Lezhnin
    Compiled by L. Matsuk
    Tehred V. Kadar Proofreader M. Sharoshi
    2664/60
    Circulation 561 Subscription VNIIPI USSR State Committee
    for inventions and discoveries 113035, Moscow, Zh-35, Raushsk nab., d, 4/5
    Production and printing company, Uzhgorod, st. Project, 4
    权利要求:
    Claims (2)
    [1]
    1. DEVICE FOR GIPSA COOKING, containing a container with loading and unloading openings and a vertical supply pipe installed in it, vertically not reaching the bottom, characterized in that, in order to intensify the heat treatment of gypsum, the side walls are made with long arms and the bottom with at least one protrusion under the outlet of the gas supply pipe. '
    [2]
    2. The device according to claim 1, with the fact that, in order to improve dust separation, the upper part of the tank is made cylindrical.
    "" 1232136
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    同族专利:
    公开号 | 公开日
    UA6321A1|1994-12-29|
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    CH644531A5|1984-08-15|
    KR830000942B1|1983-05-14|
    JPS609852B2|1985-03-13|
    NO794110L|1980-07-09|
    ES8100903A1|1980-12-16|
    DE3000314C2|1991-09-26|
    NL185896C|1990-08-16|
    NO152000B|1985-04-09|
    IT8019073D0|1980-01-08|
    JPS5594634A|1980-07-18|
    FR2445941A1|1980-08-01|
    GB2043219A|1980-10-01|
    LV5640A3|1994-05-10|
    AU530893B2|1983-08-04|
    AU5409679A|1980-07-17|
    AR221521A1|1981-02-13|
    JPS5916533A|1984-01-27|
    GB2043219B|1983-11-02|
    IE49127B1|1985-08-07|
    AT381695B|1986-11-10|
    DE3000314A1|1980-07-24|
    SE8000020L|1980-07-09|
    DK155244C|1989-07-24|
    ES487430A0|1980-12-16|
    FI65417B|1984-01-31|
    FR2445941B1|1987-08-21|
    IE792428L|1980-07-08|
    BE881016A|1980-07-07|
    PL221189A1|1980-09-22|
    NZ192447A|1983-11-30|
    CA1141157A|1983-02-15|
    NL185896B|1990-03-16|
    BR8000067A|1980-09-23|
    FI800055A|1980-07-09|
    NO152000C|1985-07-17|
    NL7909045A|1980-07-10|
    SE447475B|1986-11-17|
    JPS6158406B2|1986-12-11|
    DK155244B|1989-03-13|
    DK8980A|1980-07-09|
    IT1130199B|1986-06-11|
    PL126556B1|1983-08-31|
    US4629419A|1986-12-16|
    FI65417C|1984-05-10|
    ATA7580A|1986-04-15|
    ZA796983B|1980-11-26|
    IN152261B|1983-12-03|
    引用文献:
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    DK130338C|1968-01-25|1975-07-07|Vychodoceske Chemicke Z Synthe|
    AT285533B|1968-11-18|1970-10-27|Chemie Linz Ag|Device for the continuous dewatering of aluminum fluoride hydrates|
    GB1488665A|1973-11-27|1977-10-12|Bpb Industries Ltd|Calcining calcium sulphate dihydrate|
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    JPS534935A|1976-07-03|1978-01-18|Yasuhiro Okamoto|Method of determining stop position of vehicle and automobile|
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    ZA817558B|1980-11-10|1983-02-23|Bpb Industries Plc|Improvements in calcining calcium sulphate dihydrate|
    DE3234911A1|1982-09-21|1984-03-22|Herbert 7853 Steinen Hüttlin|FLUID BED APPARATUS|
    US4626199A|1985-04-25|1986-12-02|United States Gypsum Company|Submerged combustion calcination|
    US4744961A|1985-04-25|1988-05-17|United States Gypsum Company|Submerged combustion calcination|
    DE3520718A1|1985-06-10|1986-12-11|Herbert 7853 Steinen Hüttlin|FLUID BED APPARATUS|
    DE3530744C2|1985-08-28|1989-02-23|Herbert 7853 Steinen De Huettlin|
    GB2185419B|1986-01-07|1990-04-18|Bpb Industries Plc|Improvements in calcination apparatus|
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    法律状态:
    优先权:
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    GB7900593|1979-01-08|LV931197A| LV5640A3|1979-01-08|1993-11-11|Pleated plaster varnish|
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