• 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 conical centrifuge with continuous action, comprising a cylindrical housing, ending with a cone and a connection in its bottom end for the removal of the solid phase. Inside this cone there is fixed coaxially a cylinder, ending with a cone and a connection for the removal of the liquid phase, and over said cylinder there is disposed a conical rotor attached to a shaft, supported in a bearing box and connected by means of a belt drive to an electric motor, which is fastened to the cover of the housing. Concentrically with the bearing box there is provided a vertical pipe, in which there ends a connection, and this vertical pipe is connected to the bearing box by means of vertical blades, which are inclined with respect to the radius and to their outer ends there are fastened helical-shaped blades.
    公开号:SU737016A1
    申请号:SU762387965
    申请日:1976-08-02
    公开日:1980-05-30
    发明作者:Христов Сендов Стоян；Ангелов Николов Иван；Александров Куклин Иван；Георгиев Мирчев Мирчо
    申请人:Химкомбинат (Инопредприятие)；
    IPC主号:
    专利说明:

    The invention relates to devices for the separation of “one-stop” diagonal systems of pS systems: a solid body is a liquid, and it is “,” but a centrifuge: m, and can be used in the chemical and other Folklore 5 households.
    Closest to the invention, the technical essence is a filtration centrifuge containing a corus with a solid phase receiver, a casing with a reception of the filtrate's sink, a cone-shaped drum installed in the casing of the shaft, a cylinder arranged in the casing |
    In this centrifuge, the material to be centrifuged is carried out from the side of the drum, as a result of which dynamic loads, a drum, lead to a large 20 vibrations, an uneven separation and unloading of the solid phase. Particularly strongly manifest are dynamic loads in the centrifuge when large quantities of material are fed to the separation and at high revolutions of the drum. These loads are not symmetrically: they create instability, unevenness and increase the likelihood of partial damage to centrifuges. 30
    The purpose of the invention is to increase the reliability of the centrifuge at work.
    The goal is achieved by the fact that in a known filter centrifuge, comprising a housing with a solid phase receiver, a housing with a filtrate receiver, a cone-shaped bar-bath mounted in a housing on a shaft located in a bearing (coy bearing and feed pipe) in a drum is concentric a bearing support is provided with a cylindrical shell connected to the bearing support by means of blades inclined to the radius at an acute angle, and in the places where the blades are connected with the shell on the outer surface of the latter are reinforced raleobraznye blade, the shroud Zh1estko associated with the feed pipe.
    The angle of inclination of the blades to the radius is 15-45 °, and the angle of inclination of the spiral-shaped blades to the horizontal is 1-8 °.
    FIG. 1 shows a centrifuge, vertical section; in fig. 2 is a section A-L in FIG. one.
    The centrifuge contains a cylindrical body / with a solid phase receiver 2, terminating at the lower end with a cone and nozzle 3, and a lid 4.
    权利要求:
    Claims (3)
    [1]
    In case 1, the casing 5 ic is strengthened by a filtrate receiver 6, terminating in a cone 1 and pipe 7. In the casing 5 of the shaft 5, the rapeyuchegane in the bearing support I have a cone-shaped drum 10 with a filter sieve. Concentric podSHIPIKOVO support 9 in the bar of the bath 10 is located the cylinders; The feed pipe is rigidly connected by a shell //. The angle of inclination of the blades 12 to the radius of the unit is 15–45 °, and the angle of inclination of the optic profile, of the 13 blades to the horizontal, is 1–8 °. On the cover 4 of the housing / fixed electric motor 15, which | Tsr "water belt 16 is connected to the shaft 5 of the drum 10. The centrifuge operates as follows. The material to be separated is fed into the drum 10 through the feed pipe 14. But the annular gap between the cylindrical shell 11 and the sliding support P it enters the shield portion of the drum. From here, the material tilted to the radius. The vertical blades 12 are evenly distributed at the base of the 6aipabana and are directed to the filter screen of the latter. The filtrate passes through the openings of the sieve into the receiver 6 of the casing 5, flows down and is discharged through the nozzle 7. The solid particles remain on the sieve and thanks to the action of centrifugal 1 force and spiral vane 13 lev. 2, falls down and is discharged through pipe 3.. Thanks to the organized loading, distribution and removal of material in the center of the fugue, the dynamic loads on the drum are reduced. This increases the reliability of the centrifuge. Claim 1. F. Filtration centrifuge, comprising a housing with a solid phase receiver, a housing with a filtrate receiver, a cone-shaped drum mounted in a housing on a shaft located in an ip support, and a supply pipe characterized in that, in order to increase the centrifuge's reliability (in operation, a cylindrical shell is installed in the Drum Concentric bearing support, connected to the dumb support when using blade blades inclined to the radius at an acute angle, and at the junction of the blades with the shell on. The surface of the latter is reinforced with spiral-shaped blades, while the o-bichay is firmly connected with the feed pipe.
    [2]
    2. Centrifuge no. 1, about tl and h and y and the fact that the angle of inclination of the blades. To a radius equal to 15-45 °.
    [3]
    3. Centrifuge for juke. 1, 2, characterized in that the angle of inclination of the spiral-shaped lo-paste to the horizontal is 1-8 °. The source of information taken into account in the examination: 1. The French cousin i№ 2074597, cl. B 04 B 3/00, publ. 1971.
    Aa
    12
    Rig. 2
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    同族专利:
    公开号 | 公开日
    US4065393A|1977-12-27|
    NL7608597A|1977-02-04|
    PL107681B1|1980-02-29|
    CH608977A5|1979-02-15|
    HU176212B|1981-01-28|
    DD125245A1|1977-04-13|
    CS193174B1|1979-10-31|
    DE2634641A1|1977-02-17|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US65923A|1867-06-18|Improvement in centrifugal machines for draining sugab |
    US292705A|1884-01-29|stevens |
    US289565A|1883-12-04|Fred kttffin |
    US661943A|1898-09-19|1900-11-20|Laval Separator Co De|Centrifugal liquid-separator.|
    US715493A|1900-05-24|1902-12-09|Carl Johan Lundstrom|Liner for centrifugal cream-separators.|
    US2575691A|1947-01-21|1951-11-20|Maytag Co|Clothes-washing machine|
    US2748668A|1952-07-11|1956-06-05|Beloit Iron Works|Separator-pumping operation for paper stock|
    DE971713C|1953-10-30|1959-04-09|Kloeckner Humboldt Deutz Ag|Centrifugal separator for dewatering fine-grained material, especially coarse sludge|
    US3204868A|1960-06-06|1965-09-07|Dorr Oliver Inc|Three-product nozzle-type centrifuge|
    US3136722A|1961-10-18|1964-06-09|Pennsalt Chemicals Corp|Pusher-type centrifuge|
    US3409521A|1965-04-22|1968-11-05|Pennsalt Chemicals Corp|Method of manufacturing centrifuge discs by electrochemical machining|
    US3400827A|1966-02-07|1968-09-10|Parker Hannifin Corp|Liquid and chip separator|
    US3737038A|1971-06-03|1973-06-05|Sweco Inc|Up-flow separator|DE4314020A1|1993-04-29|1994-11-03|Rolf Dipl Ing Schnause|Process and apparatus for continuously cleaning and degassing viscous polymer melts|
    US20050054506A1|2003-07-30|2005-03-10|Bradley Bruce J.|Microbial concentration system|
    AT503390B1|2006-03-30|2008-06-15|Erema|DEVICE FOR DRYING WET BREAKABLE GOOD, PREFERABLY OF PLASTIC PARTICLES|
    CN102583601B|2012-03-22|2013-07-24|刘力学|Multifunctional butterfly stroke type solid-liquid separator|
    CN102861676A|2012-09-07|2013-01-09|西安船舶工程研究院有限公司|Centrifuge|
    CN104841158B|2015-05-17|2017-01-25|宁波大学|Dendrobium extraction device|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    BG3071175|1975-08-02|
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