• 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 separator for sorting particulate material suspended in a conveying gas into coarse and fine fractions has a rotor (1) with two sets (9,10) of vanes. Dampers (13,14) in outlet ducts for the fine fraction regulate the relative flow through the two vane sets and hence control the cut between the fine fraction and the coarse fraction which is flung centrifugally outwards by the vanes and falls down inside a casing (3).
    公开号:SU1528334A3
    申请号:SU853938655
    申请日:1985-08-12
    公开日:1989-12-07
    发明作者:Фольсберг Ян
    申请人:Ф.Л.Смидт Энд Ко А/С (Фирма)；
    IPC主号:
    专利说明:

    //
    Iff
    cl
    sixteen

    O4
    0g / g X
    around the vertical axis there is a rotor (P) 1, with two sets of lobes (CL) 9 and 10. At the same time, CL 9 is installed permanently between the upper 7 and lower 6 sections of Г 1, and 1Ш 10 - with the possibility of moving and axial direction relative to CL 9 or vertical movement on its outer edges. A device for adjusting the speed of the air flow can be. made in the form of flat flaps 13 and 14 installed in the upper part of the housing 3 above the P I nozzles (P) 5 and II for outputting the fines fraction, or in the form of a cylindrical damper installed with the possibility of axial movement relative to the upper part P I coaxially P 5. Sortable material.
    0
    five
    0
    suspended in the transporting gas is supplied vertically from the bottom upwards through П 4, located in the lower part of the housing 3. Part of the suspension flows into P 1, UT 9 passage, then through the central hole 8 in the plate 7 - into P 5. The rest of the suspension flows directly up in P 5 through CL 9, the upper zone 12 inside the housing 3 and P 11. During the passage of KP 9 and 10, heavy particles are thrown in the direction of the housing 3 and fall into P to discharge the coarse fraction located under P 1. I adjust the flaps 13 , 14, the flow rate of gas passing through CL 9 and 10, p Obtain the desired particle size distribution in the final product. 2 з, П, ф-л, 3 Il.
    The invention relates to the classification of materials by size.
    The purpose of the invention is to increase the separation efficiency by expanding the possibilities of regulating the possibilities of regulating the granulometric composition.
    FIG. 1 shows a separator with a preferred position of two sets of rotor blades, an axial section; Fig. 2 and Fig. 3 show a separator with alternative embodiments of a device for adjusting the speed of the air flow, an alternative section,
    The separator contains a rotor 1 mounted on the shaft 2 rotatably around a vertical axis inside the cylindrical body 3. In the lower part of the body 3 there is a spout 4 for feeding the raw material suspended in the transporting gas. In the upper part of the housing 3 above the rotor 1 there is placed a nozzle 5 for outputting the fine fraction suspended in the carrier gas. The rotor 1 contains the lower plate 6 and the upper plate 7 with a central outlet 8, from which the nozzle 5 extends. Between the plates 6 and 7 one of the sets of blades 9 is permanently installed, and the second set of lobes
    tay 10 is mounted with the ability to move either axially relative to the set, then 11astey 9, l5
    five
    0
    .with
    0
    0
    five
    bo with the possibility of vertical movement on the outer edges of the blades
    9 (positions 10a, 10b, 10c and lOd in FIG. 2).
    Above the set of blades 10 there are additional nozzles 11 for outputting the fine fraction connecting the upper zone (space) 12 inside the housing 3 with the nozzle 5. The device for controlling the air flow rate is made in the form of flat flaps 13 and 14 installed in the nozzles 5 and 11 for the withdrawal of the fine fraction. I
    The separator works as follows.
    The sortable material suspended in the transporting gas is fed vertically upward through the nozzle 4. Part of the suspension flows into the rotor I, pass into the set of blades 9, then through the central hole 8 in the plate 7 - into the nozzle 5 (direction of flow arrows 15 in Fig. 1 ). The rest of the suspension flows directly upwards and the nozzle enters through the set of blades 10, space 12 and nozzles 11 (direction of flow arrows 16 in Fig. 1).
    During the passage of the blades 9 and
    The 10 particles are discarded by centrifugal forces in the direction of the housing 3 and fall into the nozzle for the coarse fraction, where
    for example, in a mill. Since both sets of blades 9 and 10 have different sorting characteristics, by means of shutters 13 and 14, the flow rates of the gas passing through the blades 9 and 10 can be controlled, thereby obtaining the desired particle size distribution in the final product.
    The combined position of both sets of blades 9 and 10 (c} ig, 1) provides parallel separation i.e. There are two streams 15 and 16 of the slurry, each of which passes through only one set of blades.
    The blades 10a and 10c (fig. 2) work the same as the blades 9 and 10 (fig. 1), whereas the blades 10c and lOd are united in a combination of parallelism and sequence with respect to the blades 9, i.e. The slurry stream can also pass through two sets of blades 9 and 10. The blades can be fixed on the ring 17 surrounding the blades 9 and installed with the possibility of vertical movement.
    The device for adjusting the speed of the air flow (Fig. 3) can be made in the form of a cylindrical valve 18 installed with the possibility of axial movement relative to the upper part of the rotor 1 coaxially with the nozzle 5.
    权利要求:
    Claims (2)
    [1]
    Invention Formula
    1, Separator for separating material particles into fine and coarse, including a housing within which it is rotatable around
    0
    m sets of blades, one of which is installed stationary between the upper and lower plates, nozzles for supplying raw material suspended in the transporting gas and for outputting a large fraction located in the lower part of the housing under the rotor, nozzles for withdrawing the small fraction suspended by the S transporting gas located in the upper part of the body above the rotor, and a device for regulating the velocity, tee-air flow, characterized in that, in order to increase the efficiency of separation by expanding adjusting the granulometric composition, the device for adjusting the speed of the air flow is made in the form of flat flaps installed in the nozzles to output the fines fraction, or in the form of a cylindrical flap mounted axially relative to the upper part of the rotor coaxially to one of the nozzles to output the small fraction while the second set of rotor blades is mounted for movement,
    0
    [2]
    2. Separator according to claim 1, characterized in that the set of blades is mounted for movement in the axial direction relative to the first set of lo-paste.
    3, Separator of PP, 1 and 2, distinguishing with feM that the second set of blades are mounted with the possibility of vertical movement on the outer edges of the first set of blades.
    №7
    ToteReditor L.Zaytseva
    Compiled by L, Kasatochkina Tehred M. Didyk
    Order 7520/58
    Circulation 542
    VNIIPI State Committee for Inventions and Discoveries at the TRFfT USSR 113035, Moscow, Zh-35, Ra-utlska nab. 4/5
    fpy.J
    Proofreader M.Maksnmishinets
    Subject
    类似技术:
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    SU1528334A3|1989-12-07|Separator for dividing material particles into fine and coarse fractions
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    US1962450A|1934-06-12|Material classifier and distributor
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    US3443687A|1969-05-13|Apparatus for classifying particulate material
    US2990063A|1961-06-27|Means for dividing the products of cereal milling operations or the like
    同族专利:
    公开号 | 公开日
    DK335985D0|1985-07-24|
    GB8420566D0|1984-09-19|
    KR860001609A|1986-03-20|
    US4626343A|1986-12-02|
    ES546072A0|1986-06-16|
    DK161810B|1991-08-19|
    EP0171987B1|1989-10-25|
    KR890001390B1|1989-05-02|
    EP0171987A2|1986-02-19|
    DE3573893D1|1989-11-30|
    JPS6157278A|1986-03-24|
    DK335985A|1986-02-14|
    BR8503798A|1986-05-20|
    ES8608349A1|1986-06-16|
    IN165119B|1989-08-19|
    DK161810C|1992-01-20|
    AU569630B2|1988-02-11|
    ZA855352B|1986-03-26|
    MX162916B|1991-07-08|
    AU4505285A|1986-02-20|
    EP0171987A3|1987-03-04|
    GB2163070A|1986-02-19|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US1779993A|1927-10-31|1930-10-28|Sturtevant Mill Co|Air separator|
    US1746686A|1928-06-23|1930-02-11|Sturtevant Mill Co|Air separator|
    US2109478A|1928-09-19|1938-03-01|Elsa Katherine Gay|Air separator|
    US1933604A|1930-07-14|1933-11-07|Sturtevant Mill Co|Air separator|
    US1958816A|1932-08-06|1934-05-15|Bradley Pulverizer Company|Air separator|
    GB411123A|1932-11-30|1934-05-30|Roland Herbert Allen|Improvements in and relating to centrifugal machines for the separation of powdered or granular material or dust from gases|
    US2109476A|1934-10-17|1938-03-01|Atlantic Refining Co|Hydrocarbon oil treatment|
    US2269412A|1940-07-18|1942-01-06|Sturtevant Mill Co|Air separator|
    US2434037A|1943-04-02|1948-01-06|Babcock & Wilcox Co|Material classifier|
    US2762573A|1952-04-14|1956-09-11|Babcock & Wilcox Co|Air-swept pulverizers|
    GB927876A|1960-10-21|1963-06-06|Ass Portland Cement|Improved mechanical air classifier|
    DE1152340B|1960-10-31|1963-08-01|Hauni Werke Koerber & Co Kg|Device for sifting tobacco|
    US3670886A|1970-08-05|1972-06-20|Hosokawa Funtaikogaku Kenkyush|Powder classifier|
    SU421384A1|1971-02-22|1974-03-30|научно исследовательского института новых строительных материалов|AIRWAY CLASSIFIER|
    DE2456970C3|1974-12-03|1981-06-25|Gebr. Pfeiffer Ag, 6750 Kaiserslautern|Through air sifter|
    US4171960A|1975-08-22|1979-10-23|Jarvenpaa Viljo J|Gas-purifying device|
    GB2041251B|1978-11-24|1982-10-20|Hosolawa Funtai Kogaku Kenkyus|Pneumatic classifier|
    US4260476A|1980-01-31|1981-04-07|Union Carbide Corporation|Separation of aromatic hydrocarbons from petroleum fractions|
    AU547465B2|1981-09-01|1985-10-24|F.L. Smidth & Co A/S|Particle sorting method and apparatus|
    JPH0347900B2|1984-04-28|1991-07-22|Kawasaki Jukogyo Kk|JPH0368736B2|1984-09-04|1991-10-29|Kawasaki Jukogyo Kk|
    US4626237A|1984-12-10|1986-12-02|Exxon Production Research Co.|Method and apparatus for separating the components of a wellstream|
    US4818376A|1986-04-28|1989-04-04|Onoda Cement Company, Ltd.|Leakage prevention apparatus for a classifier|
    JPH0383646U|1989-12-15|1991-08-26|
    US4993647A|1990-03-26|1991-02-19|Williams Robert M|Two stage separator apparatus|
    DE4040890C2|1990-12-20|1995-03-23|Krupp Foerdertechnik Gmbh|Air classifier|
    US5899396A|1995-09-04|1999-05-04|Nied; Roland|Air separator and single-rotor air separator mill with such an air separator|
    FR2741286B1|1995-11-21|1998-01-23|Fcb|AIR SEPARATOR WITH CENTRIFUGAL ACTION|
    JPH10370A|1996-06-13|1998-01-06|Kansai Matetsuku Kk|Pulverizing pin type pulverizer|
    KR19990055700A|1997-12-27|1999-07-15|김영환|Circuit arrangement for smooth operation of horizontal deflection circuit|
    DE19945646A1|1999-09-23|2001-04-05|Krupp Polysius Ag|Process and air classifier for classifying shredded feed material|
    US6776291B1|2000-09-27|2004-08-17|Xerox Corporation|Article and apparatus for particulate size separation|
    US6739456B2|2002-06-03|2004-05-25|University Of Florida Research Foundation, Inc.|Apparatus and methods for separating particles|
    US7028847B2|2003-05-29|2006-04-18|Alstom Technology Ltd|High efficiency two-stage dynamic classifier|
    DE102008038776B4|2008-08-12|2016-07-07|Loesche Gmbh|Process for the screening of a millbase fluid mixture and mill classifier|
    DE102016121925A1|2016-11-15|2018-05-17|Neuman & Esser Gmbh Mahl- Und Sichtsysteme|Classifier, mill and method for sifting a gas-solid mixture|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    GB08420566A|GB2163070A|1984-08-13|1984-08-13|Separator for sorting particulate material|
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