• 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:
    In order to subject a valve (7) within the rotor of a centrifugal separator to a certain liquid pressure, a chamber (9) on one side of the valve is connected to an axial channel (12) in the vertical drive shaft (13) of the rotor, and a liquid surface is maintained in the channel very close to the axis of the rotor during the operation of the rotor. At the lower end of the drive shaft, the channel (12) opens axially though an orifice (31) having its edge at the desired radial level for the liquid surface, and this end of the shaft is arranged to rotate in a liquid body in a container (25) below the drive shaft (13).
    公开号:SU1512476A3
    申请号:SU853901785
    申请日:1985-06-05
    公开日:1989-09-30
    发明作者:Строуккен Клаус
    申请人:Альфа-Лаваль Сепарейшн Аб (Фирма)；
    IPC主号:
    专利说明:

    one
    (21) 3901785 / 23-13
    (22) 05.06.85
    (31) 8403227-5
    (32) 06/15/84
    (33) SE
    (46) 09/30/89. Bul Number 36
    (71) Alfa Laval Cenapei H AB (SE)
    (72) Klaus Stroukken (SE) (53) 66.067.57 (088.8) (56) Patent of the USSR P 350228, cl. B 04 B 1/14, 1969.
    German Patent N 2822478,: cl. B 04 B 1/14, 1978.
    (54) CENTRIFUGAL SEPARATOR (57) - The invention relates to equipment for the separation of liquids in the field of centrifugal forces. The purpose of the invention is to simplify the design of the centrifugal separator. The centrifugal separator comprises a rotor consisting of a cap 1 and a base 2 fastened together with a retaining ring 3. Inside the rotor there is a separation chamber 4. Inside the rotor there is a piston 7 moving in the axial direction of the rator and forming
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    four
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     04
    1
    the bottom of the separation chamber 4 This
    piston rests on annular end
    into the collar 1, thus the separator under the vertical hollow shaft 13 and filled with the buffer fluid. Inside the channel 12, in the drive shaft 13, a chamber 4 is separated from a row of lateral but new blades. Channel 12 reports
    outlets 8 made in the base 2. Between the said piston 7 and the lower part of the base there is a chamber 9 for the buffer liquid. Chamber 9 is connected through openings 10 and 11 by a channel 12 passing along the axis of the drive shaft 13. A device for maintaining a predetermined. - pressure of buffer fluid in the chamber
    with an internal volume of the tank 23 through an axial orifice whose diameter is smaller than diameter 12. This I design of a centrifugal separator (O does not require a sealing-coupling assembly between the rotor drive shaft and the stationary pipeline for supplying buffer fluid, does not require a pump
    9 contains a tank 25 located 5 filing. 1 hp f-ly, 3 ill.
    The invention relates to equipment for the separation of liquids in a centrifugal field of force.
     The purpose of the invention is to simplify the structure of the centrifugal separator and. 25 improvement of fluid intake through the inlet jHoe hole during rotation.
    Fig. 1 schematically shows the lower part of a centrifugal separator, a longitudinal section; figure 2 - .30 capacity, longitudinal section; on. section aa in figure 2.
    Centrifugal separator contains. a rotor consisting of a lid of a base of 2, fastened together by a retaining ring 3. 3. -.
    Inside the rotor there is a separation chamber 4, in which the ket of conical plates 5 is located. The plates 5 j rest on the lower part of the distribution-.40 body 6, designed to distribute the liquid entering the inside of the rotor through its central part, uniformly throughout the whole body camera 4. 45
    Inside the rotor there is a piston 7 moving in the axial direction of the rotor and forming the bottom of the separation chamber 4. This piston abuts against the annular end 8 of the piston 1, the CMM is divided into a series of lateral exhaust outlets 8, performed at the base, 2 .. i
    Between the aforementioned piston 7 and the lower part of the base 2 there is a chamber 9 for a buffer liquid, in which water is used in most cases. The chamber 9 communicates under the vertical hollow shaft 13 and is filled with a buffer fluid. Inside the channel 12 in the drive shaft 13 installed blades. Channel 12 reports
    with an internal volume of the tank 23 through an axial hole, the diameter of which is smaller than diameter 12. Such a design of the centrifugal separator does not require a sealing-connecting node between the rotor drive shaft and the stationary pipeline for supplying the buffer liquid, it also does not require a pump
    through holes 10 and 11 with a channel 12 passing along the axis of the drive shaft 13. The shaft 13 is rigidly connected with the base 2, ensuring the rotation of the entire rotor from the corresponding drive (not shown).
    In the lower part of the base 2 there are a series of through holes 14 located circumferentially in the end plane of this part and used as outlet channels for discharging the buffer: liquids from chamber 9. The holes 14 are closed outside the rotor housing by plugs 15 located on the longitudinal movable disc cage 16. This cage is pressed upward together with plugs 15 by means of several helical compression springs
    17 between the cage and the supporting plate element
    18, rigidly bonded to the bottom of the base 2.
    There is an additional chamber between the central part of the end face of the plate cage 16 and the bottom of the base 2.
    19, filled with buffer fluid. The camera 19 has in the center a large number of holes 20, made in the wall, forming an annular groove 21, open at the top. In addition, the chamber 19 has one or more outlets 22, made in its outer wall. The sizes of the holes 20 and 22 are chosen so that during the operation of the rotor more liquid enters the chamber 19 than
    could enter.
    (.
    A ring nipple 24 is connected to line 23 to provide an extra 51512A76
    jerky fluid supply in the mentioned; about
    thuy groove 21.
    The device for maintaining the predetermined pressure of the buffer liquid in chamber 9 contains a tank 25 located under the vertical hollow shaft 13. This tank has a supply pipe 26 and a drain-drain pipe 27 and is filled with a buffer liquid. The upper end of the drainage pipe 27 serves as a nadurovny inlet for draining the fluid during tank overflow, thus maintaining a certain level of this fluid. To compensate for disturbances created in the fluid during the rotation of the lower end of the rotor drive shaft 13, 29, placed accordingly in the specified capacity. There can be more than two such partitions in tank 25, and they can be located in any convenient way.
    In Fig. 2, the reservoir 25 is shown without the above-mentioned barriers and piping, but filled with liquid, the level of the liquid is indicated by a triangle. It also shows the lower end portion of the rotor drive shaft 13.
    As follows from Figures 2 and 3, blades 30 are mounted inside channel 12 in drive shaft 13. Channel 12 communicates with the internal volume of tank 25 through an axial bore 31 whose diameter is less than the diameter of channel 12 ..
    Centrifugal separator operates as follows.
    When the drive shaft 13 is rotated, the buffer fluid inside its channel 12 is pressed against the walls to form a cylindrical surface, rushing up along the walls of the channel and then out through the holes 11 and 10 into the chamber 9 in the rotor. A new portion of the liquid enters the channel 12 through the opening 31 to replace the gone up liquid at this stage. After filling the chamber 9, the flow of fluid into the separator through the opening 31 will stop, and it will have an annular cylindrical shape in the channel 12 with a cylindrical inner surface whose radius corresponds to the edge surrounding the inlet
    ; hole 31. In the annular column of liquid thus formed, the inner surface of which is very close to the rotor axis, a pressure will be created that surpasses the fluid pressure in chamber 9 and, among other things, generates a force, tightly pressing the piston 7 along the axis.
    The specified force acting on the bottom of the piston 7 exceeds the force acting in the opposite direction.
    0
    0
    five
    the piston on the side of the fluid in the separation chamber 4. As a result, the outlet openings 8 will remain in the closed state. If it is necessary to briefly open the outlet openings 8, the fluid is supplied to the chamber 19 through the conduit 23 through the annular plug 4, the groove 21 and the inlet openings 20. As a result, the inlet of the fluid to the chamber 19 creates an appropriate pressure, superior force of the spring 17, acting in the opposite direction on the plate holder 16. As a result, the holder 16 is displaced axially downward, opening the outlet openings 14 from the chamber 9.
    The consequence of this will be an accelerated release of fluid from chamber 9 with a flow rate that exceeds the rate of arrival of its new portions through channel 12 in the rotor drive shaft. This will lead to the displacement of the piston 7 down and opening the outlet openings 8 of the separation chamber 4.
    When the supply of fluid to chamber 19 is stopped through conduit 23, this chamber is drained through outlet openings 22. As a result, the submersible tray 14 of the cage 16 returns to its upper position under the action of the return force generated by the springs 17. As a result, the outlet openings
    0 14 from chamber 9, which begins to fill up again with liquid, which all this time has been flowing into it through openings 10, 11 from axial channel 12 in the rotor drive shaft. Once
    e pressure acting on the piston. 7
    from the side of the fluid in chamber 9, it will exceed the pressure acting on it from the side of the fluid in the separation chamber 4,
    0
    said piston returns to its upper position, in which the outlets 8 are blocked.
    After the completion of each step of the cycle (and in front of it), the replacement of the above-mentioned annular shape of the liquid column in the axial channel 12 of the rotor drive shaft 13 occurs .- - 10
    . If necessary, the lower end part of the drive shaft 13, i.e. The part in which the blades 30 are located may be made as a separate easily removable part, for example, as a plastic nozzle. Positive in this embodiment is the possibility of using several such removable parts with an inlet orifice 31 of various sizes (with a 20 constant channel in the rotor drive shaft).
    Further, if necessary, that part of the channel 12 in which the blades 30 are located can be made with an enlarged diameter exceeding the diameter of the rest of the channel.
    The proposed design of the centrifugal separator is simpler than the known, since it does not require the use of a sealing-disconnecting unit between the rotor drive shaft and the stationary pipeline, in addition to supplying the buffer fluid.
    In addition, there is also no need to use a pump to supply the buffer fluid to the rotor.
    权利要求:
    Claims (2)
    [1]
    1. A centrifugal separator comprising a rotor having a separation chamber for a liquid subjected to a seperation, a piston mounted in the rotor for opening the orifice openings, a buffer liquid chamber beneath it, the lower vertical rotor drive shaft having inside a channel communicated with the buffer chamber liquids, and a device for maintaining a predetermined pressure of a buffer liquid in the latter, characterized in that, for the purpose of simplifying the construction, said device comprises a container disposed below m hollow shaft
    and filled with buffer fluid - while the lower part of the shaft is placed inside the container and has an inlet at the end, the diameter of which is smaller than the diameter of its internal channel.
    [2]
    2. The separator according to claim 1, about tl and h and-y and with the fact that, in order to improve the intake of fluid through the inlet during rotation, the blades are reinforced in the inner channel of the shaft above the inlet.
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    FIG. 2
    FIG. J
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    同族专利:
    公开号 | 公开日
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    KR920010883B1|1992-12-21|
    JPS614552A|1986-01-10|
    CA1252076A|1989-04-04|
    US4636319A|1987-01-13|
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    SE8403227D0|1984-06-15|
    PL144344B1|1988-05-31|
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    RU2492935C1|2009-07-10|2013-09-20|Альфа Лаваль Корпорейт Аб|Gas cleaner|US1050720A|1912-11-05|1913-01-14|Harald De Raasloff|Art of centrifugal separation.|
    US2454929A|1944-07-17|1948-11-30|Dole Valve Co|Flow control|
    US3079069A|1958-05-16|1963-02-26|Separator Ab|Self-opening sludge centrifuge|
    US3255958A|1962-12-04|1966-06-14|Westfalia Separator Ag|Centrifugal desludging separator|
    US3403849A|1965-12-15|1968-10-01|Alfa Laval Ab|Sludge centrifuge with intermittent discharge|
    US3460750A|1966-04-21|1969-08-12|Cuccolini Silla|Centrifugal separator|
    DE2054968C3|1970-11-09|1980-05-29|Hans-Joachim 6148 Heppenheim Titus|Rotary filter|
    SE376177B|1972-02-23|1975-05-12|Westfalia Separator Ag|
    SE408838B|1975-02-04|1979-07-09|Prazska Akumulatorka Np|PROCEDURE FOR THE MANUFACTURE OF ACCUMULATOR ELECTRODES CONSISTING OF A MIXTURE OF AN ACTIVE SUBSTANCE AND A PLASTIC AND OF A POWER DISCHARGE|
    SE405213B|1976-06-11|1978-11-27|Alfa Laval Ab|CENTRIFUGAL SEPARATOR|
    GB1591811A|1977-05-24|1981-06-24|Jackson J F|Desludger type disc bowl centrifuges|
    SE436839B|1979-06-20|1985-01-28|Alfa Laval Ab|CENTRIFUGAL SEAT MANOVER SYSTEM|
    DE3009669C2|1980-03-13|1988-09-08|Kloeckner-Humboldt-Deutz Ag, 5000 Koeln, De|
    DE3109346A1|1981-03-12|1982-11-04|Klöckner-Humboldt-Deutz AG, 5000 Köln|Centrifuge which can be emptied hydraulically|DE3606522C1|1986-02-28|1987-05-21|Westfalia Separator Ag|Centrifugal centrifuge for clarifying or separating liquid mixtures|
    SE458507B|1987-06-24|1989-04-10|Alfa Laval Marine Power Eng|PROCEDURE IN OPERATION OF A Centrifugal Separator and Centrifugal Separator BEFORE THE IMPLEMENTATION OF THE PROCEDURE|
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    法律状态:
    优先权:
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