• 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:
    THE DEVICE FOR CLEANING OF THE POLLUTED. WASTE, comprising a housing in the form of a cylindrical tank open at the bottom with a filter element, under which a support base is installed with a slot between the walls of the tank and the support base, the tank is mounted on radial bearings and provided with an inlet in the upper part and a discharge device in the lower part for the waste view, located inside the tank and communicating in the upper part with the atmosphere of perforated pipes, one of which extending along the axis. the tank is made with an open lower end located at the support base above the discharge opening located in the center of the support base, while the lower end of one part of the pipes is located in the aerobic fermentation zone, and the other part in the ay ferrous fermentation zone, the discharge device is made in the form of a radial screw, mounted on a support base with the possibility of angular movement around a central outlet opening, characterized in that with the aim of obtaining waste, used, for example, in It is a combustible substance (L is equipped with a central discharge pipe installed in the support base and a pneumatic line with a fan and a separation device for heavy particles containing a chamber with a screw, equipped with a downward channel open from the bottom and containing at the open end adjustable gate valve.
    公开号:SU1160929A3
    申请号:SU813340596
    申请日:1981-09-22
    公开日:1985-06-07
    发明作者:Пинеда Ровира Фелипе
    申请人:Д.Фелипе Пинеда,С.А. (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to devices for cleaning contaminated waste, in particular gaseous, liquid, pasty. A device for cleaning contaminated waste is known, comprising a housing in the form of an open cylindrical reservoir with a filtering element under which a support base is installed with a slot between the walls of the tank and the support base, the tank is installed on radial bearings and provided with an upper part 1 pipe. for inlet and in the lower part - discharge device for waste disposal, located inside the tank and communicating in the upper part with the atmosphere of perforated pipes, one of which is a passage, the tank axis is made with an open lower end located at the stop base above the discharge opening located at the center of the support base, while the lower core of one part of the pipes is located in the aerobic fermentation zone of the fermentation, and the other part is in the the form of a radial screw mounted on a support base with the possibility of angular movement around the central hole D A disadvantage of the known device is the lack of a centralized unloading devices and the impossibility of using the obtained product as a solid fuel, since the liquid phase remains in the final product. The purpose of the invention is to obtain wastes used; for example, as a combustible substance. This goal is achieved due to the fact that the device for cleaning contaminated detours, comprising a housing in the form of an open-bottom cylindrical tank with a filtering element, under which a support base is installed with a slot formed between the walls of the tank and the support base in the upper part there is a nozzle for inlet and in the lower part an unloading device for the withdrawal of waste, located inside the tank and communicating with the atmosphere a perforated pipe and, one of which extending along the axis of the tank ,; made with an open lower end located at the support base above the discharge opening located in the center of the support base, while the lower end of one part of the pipes is located in the aerobic fermentation zone, and the other part in the anaerobic fermentation zone, the discharge device is made in the form of a radial screw, mounted on a support base with the possibility of angular movement around the central outlet hole, equipped with a central discharge pipe installed in the support base, and pneumatically a line having B (a fan and a separator device of heavy particles containing a tamer with a screw, equipped with a downwardly directed channel open from the bottom and containing an adjustable valve at the open end. In Fig. 1 is a schematic of the proposed CPP top device; Fig. 2 - a tank in which fermentation is carried out, a vertical section; in Fig. 3 - section A-A in Fig. 1; in Figo 4 - a section B-B in fi. 3. The device is designed in such a way that all three stages of fermentation are carried out in one; same tank. These steps can be performed under aerobic conditions. At the same time, the mass of which the filtering element is composed has a corresponding height. Air is introduced into it for the aerobic fermentation stage and the anaerobic fermentation gas is introduced through pipes introduced into the specified mass of the corresponding depth. In this case, contaminated cleanable waste is introduced at the most preferred fermentation stage. The device comprises a cylindrical tank 1 with a vertical axis in which three stages of fermentation are carried out. The loading of the organic material forming the filter element is carried out via the bucket conveyor 2, but any other loading device can be used. The material is organic, waiting, coming from the fields. The feeder is fed into the dispenser 3, from which the belt conveyor 4 leaves, which loads the mill 5. The dispenser 3
    regulates the amount of material entering the mill 5 so that it does not clog. Mill 5 roughly grinds material, such as trash bags, crates, bottles, etc.
    From mill 5, the product enters a screen or separating device 6, where only large objects of plastic, metal, glass, etc. are separated. Separated objects exit through pipe 75a and the rest of the product is sent to conveyor 2. The conveyor is discharged into chamber 8. from which the product enters tank 9 via line 9. The tank 1 (Fig. 2) with walls 10 is lined with a material that is not subject to fermentation. A locking lid 11 is provided at the top,
    the lower end of which remains open. Krishka 11 has a loading device for the material, for example a cyclone 12, to which the loading line 9 is suitable. The tank 1 is mounted on a supporting frame or external supports 13. Under the tank there is a base 14 with a central opening that can be made of concrete or metal the lower edge of the wall 10 is at some distance, a central opening of the base 14 or 14 is equipped with a discharge pipe 15, from which the pneumatic discharge line 16 extends radially outwards.
    A vertical central perforated tube 17 is installed in the tank, suspended, for example, by means of clamping bolts 18, with the tube starting at the top from the point of the uppermost level that the filter element reaches. At the bottom of the pipe ends above the discharge pipe 15. The upper end of the pipe 17 can be provided with a cover 19, which prevents the inlet of the material supplied by the cycle 12.
    This pipe may have holes along its entire length, 20, protected. on top of the flaps 21, which prevent the inlet material of the filter element and serve to suck the gases and vapors formed at each stage of the reflux. In case of use of these gases - vertical by-pass
    piping 22 extending out through lid 11 and originating in the anaerobic fermentation zone.
    Vertical pipelines 23 are provided for air intake in the aerobic fermentation zone. These pipelines have radial holes in the wall sections extending in the aerobic fermentation zones. Tubes 22 have holes in a portion extending in the anaerobic fermentation zone.
    Between the lower edge of the wall 10 of the tank and the base 14 is installed in the radial direction of the screw 24, which transports the filtering mass at the end of the third fermentation stage, to the central discharge pipe 15. The screw 24 is driven outside by the motor 23 and the inner end is mounted on a rotating support 26. The engine 25 using gears or some other device is mounted on a transmission mechanism 27 mounted between the supports of the tank 13 and the base 14. The engine moves on the gear to the new mechanism in such a way that it informs the screw 24 not only rotational, but also angular movement, as a result of which the screw 24 captures the fermentation product from the third fermentation zone over its entire cross section. The motor driving the power unit | has a force less than a certain size, so the screw encountering a large resistance when gripping, which prevents further angular movement, only rotates and engages the front side of the material that resists for as long as the angular movement continues.
    . This effect is possible, for example, by sliding the drive gears of the power unit along track 28, if the resistance that the auger encounters during angular displacement exceeds a certain value.
    The inner screw bearing 29 is mounted in such a way that it is not an obstacle to the flow of air formed between the central discharge pipe 15 through the central discharge pipe 15.
    central tube and pneumatic suction.
    A separation device 30 for heavy particles (Fig. 3) is installed in the discharge line 16, which contains a chamber 31. placed under the line 16 and connected to it by an open channel, the value of which can be changed using a valve 32. In the chamber 31, a horizontal auger 33 is installed, moving in the transverse direction relative to the discontinuous line 16 and driven by the engine 34. The chamber 31 goes into the channel 35, which is open at its lower end and has an adjustable valve 36 here, driven by, for example, by oschyu mechanism 3 in the same line 16 (Fig.1) for razdelitelnm device 30 is mounted a fan 38, a suction force which acts on linits 16 from the discharge chute 15 (Figure 2). Due to suction in the pipeline, a vacuum is created by means of which the material advanced by the screw 24 is sucked up to the pipe 15. In addition, the aspiration creates air flow through the perforated pipe 17 and the hole, which prevents clogging of the discharge pipe 15. The suction through the perforated pipe 17 provides air flow through the upper cyclone 12. At the same time, a vacuum in line 16 provides air through the opening, the intensity of which depends on the degree of opening of the valve 36 (Fig. 3 and 4). The material that is sucked through the pneumatic line 16 falls into the separation device 30 as soon as the valve 32 is opened. The screw 33 turns the products over and simultaneously moves them to the channel 35. The backside 36 is adjusted so that the air flow through the outlet port captures a small amount of particles in the pneumatic line 16 so that they continue their journey, and heavy parts, such as stones, metal objects, glass, etc., fall into the channel 32, through which they through the opening and closing The openings of the valve fall out. Line 16 behind fan 38 enters mill 39, which crushes the fermented material to the required grain size. This operation is facilitated by the reduced consistency of the particles after fermentation. The crushed material then enters the screen or passes through the supershlen chamber 40, in which some of the separated waste is burned. The moisture content of the material at this location has already been significantly reduced, since the moisture evaporates from the material heated during the various stages of the fermentation. The dried product can be placed in a bunker 41, from which it is sucked off by a pneumatic conveying system with a blower 42 and sent to a cyclone 43, from which a fine-grained powder is fed to the combustion chamber, and the powder is stored in the bunker 44. a briquette set 45, which forms briquettes of solid fuel, which is an excellent fuel for various applications. These briquettes from the briquette unit are supplied, for example, by a belt conveyor 46, to the storage area 47. The device may additionally have bunkers in places where storage seems appropriate. It is also possible to provide two parallel tanks 1 operating with the same loading and unloading device. / Near tank 1, a tank 48 is installed, containing the treated waste loaded into tank 1 via conduit 49. When fed to the first fermentation stage, this waste can be mixed with the material forming the filter element. This process is carried out on cyclone 12 of reservoir 1 and prior to delivery to the reservoir. If waste is fed to the second stage of fermentation, pipes for feeding waste are provided in tank 1, and pipes 22 can also be used for this (Fig. 2).
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    权利要求:
    Claims (1)
    [1]
    DEVICE FOR CLEANING CONTAMINATED. WASTE, comprising a body in the form of a cylindrical vessel open at the bottom with a filter element under which is installed the support base to form between the walls of the tank and the support base gap, a reservoir mounted on radial supports and provided at the top of pipe to enter, and at the bottom - the discharge a device for removing waste located inside the tank and communicating in the upper part with the atmosphere of perforated pipes, one of which passing along the t axis of the tank is made open the lower end located at the thrust base above the discharge hole located in the center of the support base, while the lower end of one part of the pipe is located in the aerobic zone : fermentation, and the other part in the aaerobic fermentation zone, the discharge device is made in the form of a radial screw mounted on supporting base with the possibility of angular movement around the central outlet, characterized in that. in order to obtain waste used, for example, as a combustible substance, it is provided In Central discharge pipe installed in the support base and pneumatic line having a fan and a device for separating heavy particles, comprising a chamber with a screw provided with a downwardly directed channel bottom and open at the open end comprising an adjustable valve.
    类似技术:
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    US4165289A|1979-08-21|System for the clarification of waste water and utilization of waste products
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    同族专利:
    公开号 | 公开日
    RO83712B|1984-05-30|
    OA06906A|1983-04-30|
    US4451372A|1984-05-29|
    ZA816618B|1982-10-27|
    KR830007437A|1983-10-21|
    FI812937L|1982-03-24|
    ES8201507A1|1981-12-16|
    DE3169056D1|1985-03-28|
    DK419481A|1982-03-24|
    BE890182A|1982-01-04|
    JPH0143598B2|1989-09-21|
    JPS5787890A|1982-06-01|
    DD201877A5|1983-08-17|
    CA1170790A|1984-07-10|
    ES495266A0|1981-12-16|
    PT73622A|1981-10-01|
    DOP1981003032A|1987-03-27|
    IL63888D0|1981-12-31|
    GB2084559A|1982-04-15|
    AU7512181A|1982-04-01|
    MA19279A1|1982-04-01|
    AR226920A1|1982-08-31|
    IE812035L|1982-03-23|
    GB2084559B|1983-07-06|
    EP0048683B1|1985-02-20|
    FR2490621B1|1985-01-04|
    YU213681A|1983-12-31|
    NO813225L|1982-03-24|
    NZ198237A|1983-12-16|
    IE51544B1|1987-01-07|
    EP0048683A1|1982-03-31|
    HU186425B|1985-07-29|
    PL233121A1|1982-05-24|
    BR8106061A|1982-06-08|
    PT73622B|1982-11-16|
    PL130037B1|1984-07-31|
    RO83712A|1984-04-12|
    GR74691B|1984-07-04|
    FR2490621A1|1982-03-26|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3241943A|1962-04-13|1966-03-22|Bystrom Sven Gustav|Method for the production of a fertilizer or soil improvement agent from sulfite waste liquor while recovering acids and combustible gases formed in the process|
    DE2334107A1|1973-07-04|1975-01-23|Siemens Ag|Sintered perforated plate column - for activated sludge effluent treatment|
    DE3006536A1|1975-05-06|1980-09-11|Yamato Setsubi Koji Kk|Treatment of effluent water streams - using settling tank followed by activated sludge treatment in tray tower with air lift pump to provide recirculation|
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    SE405351C|1975-04-25|1987-06-10|Svenska Sockerfabriks Ab|PROCEDURE FOR BIOLOGICAL CLEANING OF CARBOHYDRATE AND / OR PROTEINRIC WASTE WATER|
    JPS5744393B2|1975-04-30|1982-09-21|
    JPS5330774U|1976-08-24|1978-03-16|
    DE2641750A1|1976-09-16|1978-03-23|Vysoka Skola Chem Tech|Purifying waste water of high organic content - first acid anaerobic, then aerobic, then anaerobic methane fermentations|
    BE885575Q|1977-01-07|1981-02-02|Shattock Geoffrey F|TREATMENT OF SLUDGE BY BIOLOGICAL DEGRADATION|
    DE2723581C2|1977-03-08|1984-11-29|Techtransfer GmbH, 7000 Stuttgart|Process for the aerobic rotting of animal excrement or sewage sludge as well as a system for carrying out the process|
    DE2757144C2|1977-12-21|1983-12-22|Gebrüder Weiss KG, 6340 Dillenburg|Device for ventilating organic waste|
    US4281266A|1979-09-14|1981-07-28|Westinghouse Electric Corp.|Dynamoelectric machine with flux screen|
    US4323367A|1980-06-23|1982-04-06|Institute Of Gas Technology|Gas production by accelerated in situ bioleaching of landfills|
    DE3024813C2|1980-07-01|1988-05-26|Gebrueder Weiss Kg, 6340 Dillenburg, De|
    US4350588A|1980-08-14|1982-09-21|Junjiro Tsubota|Biological fermentation device|DE3571965D1|1985-04-02|1989-09-07|Organic Waste Systems Nv|Vessel for anaerobic fermentation|
    FR2614017B1|1987-04-15|1989-07-28|Ciden|PROCESS FOR THE TREATMENT OF ORGANIC POLLUTANT ELEMENTS WITH EFFLUENTS AND PLANT FOR IMPLEMENTING SAME|
    DE3738295C2|1987-09-03|1992-08-06|Tecon Gmbh, 3392 Clausthal-Zellerfeld, De|
    US6059972A|1995-07-18|2000-05-09|Mahrer; Francois-Regis|Apparatus for receiving and conditioning organic waste by anaerobic bioconversion|
    NL9500171A|1995-01-31|1996-09-02|Pacques Bv|Aerobic wastewater treatment method.|
    US5840571A|1995-12-12|1998-11-24|E. I. Du Pont De Nemours And Company|Biological degradation of halogenated components in the unsaturated soil zone|
    JP3292717B2|1999-12-20|2002-06-17|株式会社第一コンサルタント|Organic waste fermentation treatment apparatus and method|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ES495266A|ES495266A0|1980-09-23|1980-09-23|PROCEDURE AND INSTALLATION FOR THE TREATMENT OF CONTAMINANT WASTE|
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