• 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:
    1463124 Heat treating pulverous material; preheating raw materials F L SMIDTH & CO AS 9 June 1975 [18 June 1974] 27052/74 Heading F4B Preheated lime-bearing pulverous raw material is calcined in an upright cylindrical chamber 1, having a central bottom inlet 4 for air and oxygen containing gas, separate inlets 6, 7 for raw material and a fuel, which may be a gas, to give off combustible gases at the temperature in the chamber, and an outlet 5 at the top for the calcined material entrained in waste gases. The conical bottom 2 of the chamber may have grooves in to which the raw material and fuel are delivered. The grooves may be radial or tangential to the air inlet, and the raw material may be delivered radially or tangentially, the fuel inlet being radially inward from the material inlet, or spaced round the chamber from the material inlet. There may be more than one fuel and/or material inlet. In a cement plant, Fig. 7, the raw meal is preheated in a cyclone string, the air for the calcination chamber 1 is taken from a cooler 9, which also supplies combustion air to a rotary kiln 15, and a cyclone 16, with its gas outlet connected to the inlet of the lowest cyclone 18 of the preheating string, separates the partly calcined meal from the gases discharged from the chamber 1. The waste gases from the kiln 15 may be fed to the final preheater cyclone 18, by-passing the cyclone 16.
    公开号:SU923378A3
    申请号:SU752147449
    申请日:1975-06-16
    公开日:1982-04-23
    发明作者:Туборг Йорн
    申请人:Ф.Л.Смидт И Ко.,А/С (Инофирма)；
    IPC主号:
    专利说明:

    The invention relates to the building materials industry, primarily to devices for burning cement raw mix.
    A device for calcining a preheated powder material is known, comprising a vertical cylindrical chamber with an axial gas inlet in a conical bottom, inclined in the direction of the gas inlet, an axial outlet for removing the mixture of waste gases with a calcined material connected to the separator, the material inlets installed above bottom of the camera and directed obliquely down, the fuel inlets located in the bottom,
    A disadvantage of the known device is the insufficient intensification of fuel combustion and the uneven temperature distribution over the volume of the firing chamber,
    The purpose of the invention is to intensify the combustion of fuel and to evenly distribute temperatures over the volume of the chamber.
    This goal is achieved by the fact that S is a device for firing a heated 5 powdered material containing a vertical cylindrical chamber with an axial gas inlet in a conical bottom, inclined toward the gas inlet, with an axial retraction to remove the mixture
    10 waste gases - with a bakeable material connected to a separator, material inputs installed above the chamber bottom and directed obliquely downwards, fuel inlets,
    18 located in the bottom, the fuel inlets are located under the material inlets, and each material input corresponds to a fuel inlet.
    thirty
    In addition, the conical bottom of the chamber is made with grooves located along a generatrix of a cone from the vertical walls of the chamber to the axial entry, and above the upper part
    权利要求:
    Claims (2)
    [1]
    25 are the inputs of the material, and in the bottoms of the grooves - the inputs of the fuel. The drawing shows a device for burning a heated powdered material. The device comprises a cylindrical body 1 with a vertical axis and walls 2 and 3, made in the form of a truncated cone, a pipe k for oxygen containing gas connected to the wall 2, a pipe 5 for unloading material connected to the upper wall 3. a pipe 6 for pre-feeding heated powdered raw material, fuel supply pipe 7, which passes through wall 2, rotating drum cooler 8 with cooling pipes 9, bunker 10, connecting chamber 11, rotating furnace 12, cyclone 13i connected through a vertical pipe with a cycle With a boom 15, which in turn is connected through a vertical pipe 16 to a cyclone 17, the exhaust gases from which pass through pipe 18, blower 19, filter 20, outlet 21, hopper 22, pipe 23, valves 2 and 25 pipe 26 , valves 27 and 28. The device also contains a pipe 29, a connecting chamber 30, a burner 31, a pipeline 32. e The device operates as follows. The raw material is fed to the plant through a hopper 22 and pipe 23, heated in the usual way and passed through a vertical pipe 16, separated in a cyclone 17 and passed through a rotating valve 25 and pipe 26 into a vertical pipe 14, where it is heated again and then separated in the cyclone 15. The heated raw material is fed into the kiln through the tube 6, the entrance to which is equipped with a valve 27. Part of the raw material entrained in the gas leaving 9 84 from the kiln through the tube 5 is separated from the gas in the cyclone 13 and passed through valve 28 and pipe 29 connecting chamber 30 and then to the furnace 12 for combustion. Waste gases from the furnace are passed through conduit 32 to preheat the raw material. The use of the proposed device will allow to intensify the combustion of fuel and evenly distribute the temperature regime over the volume of the firing chamber. 1. An apparatus for firing a pre-heated powdered material comprising a vertical cylindrical chamber with an axial gas inlet in a conical bottom, inclined towards the gas inlet, an axial retraction to remove a mixture of exhaust gases with a calcined material connected to the separator, material inputs mounted above the bottom of the chamber and directed obliquely downwards, the fuel inlets located in the bottom, characterized in that, in order to intensify the combustion of fuel and to evenly distribute The temperature of the chamber volume, the fuel inlets are located under the material inlets, and each material input corresponds to a fuel inlet.
    [2]
    2. The device according to claim 1, wherein the conical bottom of the chamber is made with grooves located along a generatrix of the cone from the vertical walls of the chamber to the axial gas inlet, with the material inlets above the top of the groove and in the bottom of the grooves - fuel inputs. Sources of information taken into account during the examination 1. US patent N 2639132, CL.263-21, published. 1953.
    类似技术:
    公开号 | 公开日 | 专利标题
    SU923378A3|1982-04-23|Apparatus for roasting preheated pulverulent material
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    KR910000710B1|1991-01-31|Apparatus for burning pulverulent raw material
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    RU2723793C1|2020-06-17|Method for burning fine-dispersed carbonate materials
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    同族专利:
    公开号 | 公开日
    FR2275418A2|1976-01-16|
    DK271875A|1975-12-19|
    BR7503827A|1976-07-06|
    AU8214375A|1976-12-16|
    DE2527149A1|1976-01-08|
    DK141242B|1980-02-11|
    IN143479B|1977-12-03|
    IE43056B1|1980-12-17|
    ES438665A2|1977-07-01|
    AR212430A1|1978-07-14|
    ZA753804B|1976-06-30|
    ATA467075A|1982-10-15|
    DD120277A6|1976-06-05|
    AT371085B|1983-05-25|
    NL7507279A|1975-12-22|
    CA1057492A|1979-07-03|
    YU155775A|1982-02-28|
    FI61024C|1982-05-10|
    JPS5113828A|1976-02-03|
    GB1463124A|1977-02-02|
    IT1046416B|1980-06-30|
    FI751771A|1975-12-19|
    DE2527149C2|1986-08-07|
    FI61024B|1982-01-29|
    YU146780A|1983-10-31|
    IE43056L|1975-12-18|
    CH611584A5|1979-06-15|
    ES455916A2|1978-02-16|
    US4025295A|1977-05-24|
    CS212298B2|1982-03-26|
    JPS602265B2|1985-01-21|
    RO64724A7|1979-06-15|
    DK141242C|1980-08-04|
    SE7506871L|1975-12-19|
    BE830325R|1975-10-16|
    FR2275418B2|1982-10-08|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    JPS4727593Y1|1964-09-02|1972-08-22|
    DE1282232B|1965-08-26|1968-11-07|Rohrbach Rudolf|Process and device for the utilization of inferior solid fuels in the manufacture of cement clinker|
    JPS5527022B2|1972-09-04|1980-07-17|
    DE2247172C3|1972-09-26|1981-07-02|Krupp Polysius Ag, 4720 Beckum|Plant for the production of cement, lime, clay and the like.|
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    DE2324519C3|1973-05-15|1982-07-08|Krupp Polysius Ag, 4720 Beckum|Processes and devices for the heat treatment of fine-grained material|
    US3891382A|1974-02-27|1975-06-24|Fuller Co|Apparatus for calcining raw material|US4187071A|1975-03-10|1980-02-05|Klockner-Humboldt=Deutz Aktiengesellschaft|Method for the treatment of finely grained material, particularly for the precalcining of cement|
    YU247476A|1975-11-10|1982-05-31|Krupp Polysius Ag|Device for burning or sintering a fine granular material|
    DE2601776A1|1976-01-19|1977-07-21|Polysius Ag|DEVICE FOR HEAT EXCHANGE BETWEEN FINE MATERIAL AND GAS|
    DE2712238C2|1977-03-21|1988-05-05|Klöckner-Humboldt-Deutz AG, 5000 Köln|Method and device for the multi-stage burning of cement clinker|
    DE2724654C2|1977-06-01|1984-01-26|Klöckner-Humboldt-Deutz AG, 5000 Köln|Method and device for burning fine-grained to powdery material, in particular raw cement meal|
    NO791174L|1978-04-20|1979-10-23|Smidth & Co As F L|PROCEDURE FOR MANUFACTURE OF WATERLESS ALUMINUM OXIDES|
    US4419964A|1979-10-26|1983-12-13|F. L. Smidth & Co.|Combustion plant|
    JPS6053267B2|1980-12-15|1985-11-25|Chichibu Semento Kk|
    DE3107710A1|1981-02-28|1982-09-16|Creusot-Loire Entreprises, 92150 Suresnes|METHOD FOR PRODUCING CEMENT CLINKER|
    DE3107711A1|1981-02-28|1982-10-07|Creusot-Loire Entreprises, 92150 Suresnes|METHOD FOR PRODUCING CEMENT CLINKER|
    IN159327B|1982-09-02|1987-05-02|Smidth & Co As F L|
    DE3239023A1|1982-10-21|1984-04-26|Krupp Polysius Ag, 4720 Beckum|Plant for the heat treatment of finely divided material|
    DK157442C|1982-12-07|1990-06-05|Smidth & Co As F L|PROCEDURE AND APPARATUS FOR CALCINATING PHOSPHATE|
    DK443383A|1983-09-28|1985-03-29|Smidth & Co As F L|METHOD AND APPARATUS FOR DISPOSAL OF ORGANIC INGREDIENTS IN RAW PHOSPHATE|
    DE3725512C2|1987-07-29|1992-10-15|Kettenbauer Gmbh & Co Verfahrenstechnik, 7886 Murg, De|
    GB2227301A|1989-01-18|1990-07-25|Smidth & Co As F L|Method and apparatus for producing cement clinker|
    DK167004B1|1990-07-11|1993-08-16|Smidth & Co As F L|METHOD AND PLANT FOR HEAT TREATMENT OF POWDER-SHAPED MATERIAL|
    US5533276A|1994-07-18|1996-07-09|Vandergriff, Inc.|Fountain dryer unit|
    US5816795A|1996-05-24|1998-10-06|Cadence Environmental Energy, Inc.|Apparatus and method for providing supplemental fuel to a preheater/precalciner kiln|
    US5975892A|1998-11-25|1999-11-02|Jones; Michael Andrew|Pneumatic flash calciner thermally insulated in feed storage silo|
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    DE102015106417A1|2015-04-27|2016-10-27|Thyssenkrupp Ag|Plant and process for the thermal treatment of flyable raw material|
    CN108373275B|2018-02-01|2021-01-15|中冶长天国际工程有限责任公司|Dynamic monitoring device and monitoring method for dangerous cases of lime shaft kiln|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    GB2705274A|GB1463124A|1974-06-18|1974-06-18|Calcination of pulverous material|
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