• 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:
    1508721 Burning granular material F L SMIDTH & CO AS 20 Dec 1976 [12 Jan 1976] 00962/76 Heading F4B Pulverous raw materials are burnt in a plant comprising cyclone preheaters, a kiln 9 and burnt material cooler unit 8. Air from the cooler unit is divided into two streams, one passing through the kiln and up a kiln string of preheaters 4k-1k while the other stream is passed through a calciner 7 and up a calciner string of pre-heaters 4c-1c. Raw material introduced into the kiln string at 5k and into the calcine string at 5c is subsequently calcined in the calciner 7 before passing to the kiln for sintering. At least part of the flow of material from the calciner string is passed by the pipe lie to the bottom cyclone 4k of the kiln string before being fed into the calciner. Some or all of the material in the kiln string of preheaters may be diverted after the penultimate cyclone 3k directly to the calciner. Some of the air after passing through the kiln may be-pass the preheater at 10 to be used for other purposes.
    公开号:SU847910A3
    申请号:SU772437051
    申请日:1977-01-11
    公开日:1981-07-15
    发明作者:Туборг Ярн
    申请人:Ф.Л. Смидтс Энд Ко, А/С (Фирма)；
    IPC主号:
    专利说明:

    one
    The invention relates to the cement industry, in particular to devices for calcining powdered materials.
    A device for calcining powdered materials is known, comprising two branches of cyclone heat exchangers, one of which is connected via pipelines to a calciner and a cooler, and the other through a gas pipeline of exhaust gases to a rotary kiln.
    A disadvantage of this device is a short service life, since the impurities contained in the exhaust gases from the furnace (a compound of chlorine, sulfur and alkali) are deposited on the material particles and together with them on the inner surfaces of the cyclones and branches of the branch connected to the furnace.
    The purpose of the invention is to increase the service life of the device.
    The goal is achieved by the fact that the lower end of the last cyclone of the branch containing the calciner is connected to the flue of the rotary kiln.
    FIG. 1 shows the device, a general view (solid arrows - the movement of the material, dotted - the movement of gases); in fig. 2 - the same, option.
    The device contains two branches of cyclones 1-3 and 4-7, connected in series with each other by pipelines 8, a rotating furnace 9 with a gas flue 10 and a cooler 11 with a gas flue 12.
    ten
    One branch through the separator 13, the calciner 14 and the duct 12 is connected to the cooler 11, and the other through the duct 10 to the furnace 9.
    The branches are interconnected by pipes 15 and 16, with the pipeline 15 being installed between the last cyclone 3 branches containing the calciner 14 and the gas duct 10 of the furnace 9, and the pipe 16 between the cyclone 7 and the calciner 14. The material is supplied to the furnace 9 pipeline 17..
    The device works as follows.
    25
    The material is fed into the pipes 8 at points 18 and 19 to countercurrent the gaseous coolant leaving the cyclones 2 and 5.
    The passage through the cycloVO is 1-3 and 4-7, the material is processed with heat carrier and heated. Then the material heated in cyclones is fed to the calcinator 14, and the material from the cyclone 7 goes directly to the calciner 14, and from the cyclone 3 through pipeline 15 and the duct 10 into cyclone 7 and further into calcinator 14.
    After processing in the calciner 1, the material enters the separator 13, where it is freed from gases and vapors, fed to the rotary kiln 9 for final processing and then to the cooler 11. Cooling is performed with air, which is then released to pretreat the material in the branch containing the calcinator 14.
    The connection of the last Vevi cyclone containing the calciner to the furnace flue allows the material containing a small amount of impurities to be supplied from the branch with the calciner to the branch connected directly to the furnace, thus reducing the concentration of impurities entering the cyclones of the branch associated with the furnace and eliminating intensive overgrowth internal surfaces of the apparatus.
    This scheme provides for the supply of all the material from the branch containing the calidator to the furnace gas duct, i.e. use of furnace waste gases to process material from both branches.
    Another variant of the operation of the device (Fig. 2) is possible, when part of the exhaust gases from the furnace (approximately plov) is removed from the device via pipeline 20 (for example, for cleaning), and the rest is used for processing the material passing through cyclones. ,
    According to this scheme, all material processed in cyclones 4-7 is sourced to calciner 14 ,. mine
    the furnace 10 duct 9, and the material being processed in cyclones 1-3 after exiting the cyclone 3 is divided into two streams — one in the furnace 10 duct 9 and the other in a calcium generator 14. To accomplish this cross scheme, additional pipelines 21 and 22.
    The ratio of the amount of material supplied to point 18 ,, to the amount of material supplied to point
     19, according to this scheme, is 70:15. In this case, the inevitable increase in the concentration of impurities in the branch containing the calciner does not exceed 1-2%. This device has a long continuous life due to the fact that the possibility of clogging the apparatus is reduced, especially in the branch associated with the furnace. In addition, the use of raw materials is possible.
    0 with a high content of impurities and fuels with a high sulfur content.
    invention formula
    A device for burning powdered materials, containing a rotary kiln, cooler with gas ducts and two cyclone branches, one of which contains a calciner with a separator, the cooler being connected to a branch containing a calciner, and a furnace gas duct with a different branch, characterized by increasing the service life, the lower end of the last cyclone of the branch containing the calciner is connected to the flue of the rotary kiln.
    40 Sources of information
    taken into account in the examination
    1. Patent of Great Britain No. 1404528, cl. F 4 B, 1975.
    权利要求:
    Claims (1)
    [1]
    Claim
    A device for firing powdered materials containing a rotary kiln, a cooler with flues and two branches of cyclones, one of which contains a calciner with a separator, the cooler duct being connected to a branch containing a calciner, and the furnace duct having another branch, characterized in that, for the purpose of to increase the service life, the lower end of the last cyclone of the branch containing the calciner is connected to the duct of the rotary kiln.
    类似技术:
    公开号 | 公开日 | 专利标题
    SU847910A3|1981-07-15|Device for annealing powdered materials
    US3923536A|1975-12-02|Method and apparatus for burning raw materials of cement clinker
    KR930005296B1|1993-06-17|Process for the heat treatment of fine-grained material
    CA1058864A|1979-07-24|Apparatus for calcining raw material
    GB1428680A|1976-03-17|Calcination of pulverous material
    US4022568A|1977-05-10|Method and apparatus for heat treating pulverous raw materials
    RU2349559C2|2009-03-20|Method and device for heating powdered or dust-like material
    FR2405433A1|1979-05-04|METHOD AND APPARATUS FOR DRYING AND GRINDING COAL
    JO1282B1|1985-04-20|Method and apparatus for calcining raw phosphate material
    RU2315736C2|2008-01-27|Method and plant for production of cement clinker
    KR910000710B1|1991-01-31|Apparatus for burning pulverulent raw material
    US4662945A|1987-05-05|Process and apparatus for manufacturing low sulfur cement clinker
    BR0109587A|2003-02-04|Method and apparatus for the manufacture of cement slag from particulate raw cement
    GB2043853A|1980-10-08|Method and apparatus for making cement clinker
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    CA2287368A1|1999-08-26|Removal of sulfur oxides from preheater off gases
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    US4304550A|1981-12-08|Apparatus for handling and utilizing system gas in a pyro-processing system
    EP0152682A1|1985-08-28|Denitration method and device for burning equipment using coal
    SU1191713A1|1985-11-15|Method of dry production of cement clinker
    SU748117A2|1980-07-15|Apparatus for heat-treating of powdered material
    同族专利:
    公开号 | 公开日
    MX144715A|1981-11-18|
    ES454943A1|1978-01-01|
    JPS5287726A|1977-07-22|
    DK9077A|1977-07-13|
    DE2700710C2|1986-05-07|
    PT66057B|1978-06-22|
    CH618004A5|1980-06-30|
    AU500405B2|1979-05-17|
    NO770091L|1977-07-13|
    SE417817B|1981-04-13|
    BE850264A|1977-05-02|
    ATA11777A|1978-03-15|
    US4101336A|1978-07-18|
    FR2337698A1|1977-08-05|
    NO144381C|1981-08-19|
    AR209845A1|1977-05-31|
    SE7700217L|1977-07-13|
    CA1071863A|1980-02-19|
    DK144540C|1982-09-06|
    NO144381B|1981-05-11|
    AU2114277A|1978-07-13|
    BR7700180A|1977-09-06|
    DK144540B|1982-03-22|
    ES460831A1|1978-04-16|
    IN145313B|1978-09-23|
    JPS6224719B2|1987-05-29|
    DE2700710A1|1977-07-14|
    NL7700068A|1977-07-14|
    PT66057A|1977-02-01|
    NZ183047A|1979-06-08|
    GB1508721A|1978-04-26|
    AT346753B|1978-11-27|
    ZA7725B|1977-11-30|
    FR2337698B1|1983-11-04|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    JPS5239407B2|1972-04-27|1977-10-05|
    GB1417011A|1972-07-10|1975-12-10|Smidth & Co As F L|Cement manufacture|
    DE2262213B2|1972-12-19|1975-02-06|7461 Dotternhausen|Process for the heat treatment of powdery material in a rotary kiln system|
    GB1434091A|1973-04-30|1976-04-28|Smidth & Co As F L|Plant for burning or heat treatment of granular or pulverous material|
    GB1404528A|1973-07-31|1975-09-03|Smidth & Co As F L|Methods of and apparatus for heat treatment of pulverulent material|
    GB1453215A|1974-05-10|1976-10-20|Smidth & Co As F L|Calcination of pulverous material|
    DK427274A|1974-08-12|1976-02-13|Smidth & Co As F L|PROCEDURE FOR DIVIDING A STREAM OF POWDERED MATERIAL INTO SUBSTROMS|DE2630907C2|1976-07-09|1984-07-12|Klöckner-Humboldt-Deutz AG, 5000 Köln|Method and device for the thermal treatment of alkaline cement raw material|
    DE2712238C2|1977-03-21|1988-05-05|Klöckner-Humboldt-Deutz AG, 5000 Köln|Method and device for the multi-stage burning of cement clinker|
    JPS54116427U|1978-02-03|1979-08-15|
    JPS5748254B2|1978-08-04|1982-10-15|
    DK410680A|1979-12-11|1981-06-12|Smidth & Co As F L|PROCEDURE AND PLANT FOR THE PREPARATION OF POWDERED OR GRANULATING MATERIALS FOR EXCEMENT|
    DE3000494A1|1980-01-08|1981-07-09|Krupp Polysius Ag, 4720 Beckum|METHOD AND INSTALLATION FOR THE HEAT TREATMENT OF FINE GRAIN GOODS|
    EP0048537B1|1980-09-22|1985-03-20|F.L. Smidth & Co. A/S|Kiln plant for burning granular or pulverulent material|
    US4369067A|1980-12-10|1983-01-18|F. L. Smidth & Co.|Method of and plant for manufacturing pulverous or granular material|
    AT375628B|1981-11-03|1984-08-27|Voest Alpine Ag|METHOD FOR PRODUCING CEMENT AND DEVICE FOR CARRYING OUT THE METHOD|
    EP0082802B1|1981-12-04|1988-02-17|Mitsubishi Jukogyo Kabushiki Kaisha|Calcining apparatus for powdery materials|
    JPS5899148A|1981-12-04|1983-06-13|Mitsubishi Mining & Cement Co|Powdery substance calcining device|
    JPS5899149A|1981-12-04|1983-06-13|Mitsubishi Mining & Cement Co|Powdery substance calcining device|
    DE3248175A1|1982-12-27|1984-06-28|Klöckner-Humboldt-Deutz AG, 5000 Köln|METHOD AND SYSTEM FOR THE THERMAL TREATMENT OF MINERAL RAW MATERIALS|
    DE3411148C2|1984-03-27|1990-04-26|Alexander Dipl.-Ing. 6500 Mainz De Grisar|
    DE102009059110B3|2009-12-18|2011-02-17|Polysius Ag|Process and plant for the production of cement clinker|
    CN104596299A|2015-02-05|2015-05-06|安徽芜湖海螺建筑安装工程有限责任公司|Inner tube hanging sheet replacement construction method for preheater cyclone of cement clinker production line|
    CN104896917A|2015-06-26|2015-09-09|南京恒海水泥工程设计有限公司|Calcining kiln tail system for cement production|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    GB962/76A|GB1508721A|1976-01-12|1976-01-12|Method of burning pulverous alkali-containing raw materials|
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