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    • 41. 发明授权
    • Centrifugal separator
    • 离心分离器
    • US4698053A
    • 1987-10-06
    • US880884
    • 1986-07-01
    • Klaus Stroucken
    • Klaus Stroucken
    • B04B1/14B04B1/08B04B1/10B04B7/14
    • B04B1/08
    • In a centrifuge rotor, the separation chamber (21) of which contains a set of conical separation discs (10), these are guided radially by means of guiding means (11) extending axially through the discs. At their ends, the guiding means (11) are fixed relative to the rotor body (1,2) in its periphery direction and radially. The rotor body has an upper part (1) and a lower part (2), which are held axially together at their peripheral portions. A distributor has a base portion (7) on which the separation discs (10) rest, and a neck portion (6) which extends centrally up through the disc set. The distributor is radially guided relative to the lower part and the upper part, respectively, of the rotor body. Cylindrical guiding surfaces (9) are present between the neck portion (6) and the upper rotor part (1) and, possibly, also between the base portion (7) and the lower rotor part (2).
    • 在离心机转子中,其分离室(21)包含一组锥形分离盘(10),它们通过轴向延伸通过盘的引导装置(11)径向地引导。 在它们的端部,导向装置(11)在其周向方向和径向上相对于转子体(1,2)固定。 转子体具有在其周边部分轴向保持的上部(1)和下部(2)。 分配器具有分离盘(10)搁置在其上的基部(7),以及通过盘组集中向上延伸的颈部(6)。 分配器相对于转子体的下部和上部分别被径向引导。 在颈部(6)和上转子部(1)之间以及可能还存在于基部(7)和下转子部(2)之间的圆柱形引导表面(9)。
    • 42. 发明授权
    • Centrifugal separation apparatus
    • 离心分离装置
    • US3753336A
    • 1973-08-21
    • US3753336D
    • 1972-04-06
    • ENVIROTECH CORP
    • DREW JELLIOTT MARKS R
    • B01D45/12B04B7/14B04C5/18H01F10/06
    • H01F10/06B01D45/12B04B7/14B04C5/18
    • This application discloses an apparatus for separating entrained liquids and solids from a gaseous stream containing entrained liquids and solids. The apparatus is described as a conical tubular envelope partitioned into a de-entrainment chamber and settling chamber by an apertured diaphragm or baffle plate. The gaseous stream tangentially enters the de-entrainment chamber wherein liquids and solids are centrifugally seapatated. The deentrained liquids and solids pass through the apertured diaphragm into the settling chamber, while gaseous components leave through an outlet in the de-entrainment chamber. The apparatus is particularly effective in removing entrained cooking liquids and woodpulp from the wet gaseous effluent of a woodpulp digester.
    • 本申请公开了一种用于从含有夹带的液体和固体的气流中分离夹带的液体和固体的装置。 该装置被描述为通过有孔隔膜或挡板分隔成解吸室和沉降室的锥形管状包层。 气流切向进入去离子室,其中液体和固体被离心地渗透。 去夹带的液体和固体通过有孔隔膜进入沉降室,而气态组分通过去除室中的出口离开。
    • 49. 发明申请
    • CENTRIFUGAL SEPARATOR
    • US20220072565A1
    • 2022-03-10
    • US17419342
    • 2019-12-18
    • Alfa Laval Corporate AB
    • Jouko PITKÄMÄKIStefan SVENSSON
    • B04B7/14B04B1/08
    • A centrifugal separator bowl, having a vertical rotational axis, the separator bowl defining a separation space, and including an upper bowl section having a first threading, the first threading having a first inner diameter and a first outer diameter and defining an upper surface, and a lower bowl section having a second threading corresponding to the first threading of the upper bowl section, the second threading having a second outer diameter and a second inner diameter and defining a lower surface. The upper surface of the first threading of the upper bowl section and the lower surface of the second threading of the lower bowl section form a screw connection. The upper surface of the first threading is inclined upward with a first angle from the first inner diameter to the first outer diameter and the lower surface of the second threading is inclined downward with a second angle from the second outer diameter to the second inner diameter relative to a horizontal plane extending perpendicular to the vertical rotation axis.
    • 50. 发明申请
    • CENTRIFUGAL SEPARATOR AND METHOD FOR ELIMINATING AIR LOCKS IN A CENTRIFUGAL SEPARATOR
    • US20220023885A1
    • 2022-01-27
    • US17296382
    • 2019-12-09
    • ALFA LAVAL CORPORATE AB
    • Kasper HÖGLUND
    • B04B1/08B04B5/04B04B7/14
    • A centrifugal separator bowl includes a rotor casing enclosing a separation space in which a stack of frustoconical separation discs is arranged to rotate around a vertical axis of rotation, wherein the separation discs are arranged with the imaginary apex pointing to the axially lower end of the rotor casing; a feed inlet at the axially lower end for receiving the fluid mixture to be separated; a distributor for distributing the fluid mixture from the inlet to the separation space, the distributor being arranged for guiding the fluid mixture to be separated continuously from an axially lower position at the inlet to an axially upper position in the separation space. The separator bowl further includes a light phase outlet for discharge of a separated phase of a first density and a heavy phase outlet for discharge of a separated phase of a second density higher than the first density, the heavy phase outlet being arranged at the axially upper end of the rotor casing; at least one outlet conduit for transporting separated phase of the second density from the separation space, the conduit extending from a radially outer position of the separation space to the heavy phase outlet; the conduit having a conduit inlet arranged at the radially outer position and a conduit outlet at a radially inner position.