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    Portable Multi-Stage Prospecting Centrifuge
    2.
    发明申请
    Portable Multi-Stage Prospecting Centrifuge 审中-公开

    公开(公告)号：US20170312762A1

    公开(公告)日：2017-11-02

    申请号：US15583888

    申请日：2017-05-01

    申请人： AU.L, LLC

    发明人： LeRoy P. Hershberger ,  Perry Hershberger, JR.

    IPC分类号： B04B9/08 ,  B03B5/32 ,  B04B7/16 ,  B04B15/00

    CPC分类号： B04B9/08 ,  B03B5/32 ,  B04B1/00

    摘要： A compact and portable multi-stage centrifuge apparatus comprising a cart, a housing mounted onto the cart, and an engine mounted onto the cart adjacent to the housing, wherein the housing comprises an inlet in the top of the housing, an outlet in the wall of the housing, and a bowl contained within the housing, wherein the bowl comprises an engagement member that is operatively coupled to the engine's drive shaft, such that the bowl can be rotated by engaging the engine, thus removing undesirable materials from the bowl and out of the housing through the outlet.

    Spiral microchannel particle separators, straight microchannel particle separators, and continuous particle separator and detector systems
    3.
    发明授权
    Spiral microchannel particle separators, straight microchannel particle separators, and continuous particle separator and detector systems 有权
    螺旋微通道颗粒分离器，直通微通道颗粒分离器和连续颗粒分离器和检测器系统

    公开(公告)号：US08208138B2

    公开(公告)日：2012-06-26

    申请号：US12890580

    申请日：2010-09-24

    申请人： Ian Papautsky ,  Ali Asgar S. Bhagat

    发明人： Ian Papautsky ,  Ali Asgar S. Bhagat

    IPC分类号： G01N15/02

    CPC分类号： B03B5/32 ,  B01D21/0087 ,  B01D21/265 ,  B01L3/502753 ,  B01L2300/0864 ,  B01L2300/0883 ,  G01N15/0255 ,  G01N2030/002

    摘要： A spiral microchannel particle separator includes an inlet for receiving a solution containing particles, at least two outlets, and a microchannel arranged in a plurality of loops. Particles within a solution flowing through the spiral microchannel experience a lift force FL and a Dean drag force FD. The spiral radius of curvature R and the hydraulic diameter Dh of the spiral microchannel are such that for a flow rate U of the solution, the lift force FL and a Dean drag force FD are approximately equal and act in opposite directions for particles of a first size. The particles of the first size are focused in a single stream located at an equilibrium position near an inner wall of the microchannel. In another embodiment, a straight microchannel particle separator separates particles by modulating shear rates via high aspect ratios that focuses particles of a first size along two first walls.

    摘要翻译： 螺旋微通道颗粒分离器包括用于接收含有颗粒的溶液的入口，至少两个出口和布置在多个环中的微通道。 流过螺旋微通道的溶液中的颗粒经受提升力FL和Dean阻力FD。 曲线的螺旋半径R和螺旋形微通道的水力直径Dh使得对于溶液的流量U，提升力FL和Dean牵引力FD近似相等，并且对于第一 尺寸。 第一尺寸的颗粒聚焦在位于微通道内壁附近的平衡位置的单一流中。 在另一个实施方案中，直的微通道颗粒分离器通过高纵横比调制剪切速率来分离颗粒，所述高纵横比通过沿着两个第一壁聚焦第一尺寸的颗粒。

    Vortex structure for high throughput continuous flow separation
    5.
    发明申请
    Vortex structure for high throughput continuous flow separation 有权
    用于高通量连续流分离的涡旋结构

    公开(公告)号：US20080230458A1

    公开(公告)日：2008-09-25

    申请号：US11725358

    申请日：2007-03-19

    申请人： Meng H. Lean ,  Jeonggi Seo

    发明人： Meng H. Lean ,  Jeonggi Seo

    IPC分类号： B01D36/00 ,  B04C3/00

    CPC分类号： B01D45/12 ,  B01D21/265 ,  B01D2221/10 ,  B03B5/32 ,  B04C1/00 ,  B04C5/26

    摘要： A system to facilitate separation and concentration of particles based on centrifugal force on suspended particles, including biological matter, which are made to flow in a vortex structure is provided. The centrifugal force urges larger particles to collect along outer portions of the vortex flow. Conversely, within a vortex structure, a radial hydrodynamic pressure drop is also amplified to urge smaller particles toward inner portions of the vortex flow. This force created by the pressure can reach magnitudes that encourage a sharp cut-off and improved resolution discrimination between particle sizes. Thus, separated streams of particles can be collected with both increased concentration and purification.

    摘要翻译： 提供了一种用于基于离心力分离和浓缩颗粒的系统，所述悬浮颗粒（包括生物物质）被制成在涡流结构中流动。 离心力促使较大的颗粒沿涡流的外部部分收集。 相反，在涡流结构内，径向流体动压压降也被放大，以将较小的颗粒推向涡流的内部。 由压力产生的这种力可以达到鼓励锐利截止和提高颗粒尺寸分辨率的大小。 因此，分离的颗粒物流可以以增加的浓度和纯化收集。

    Method and system for separating particulate matter
    6.
    发明申请
    Method and system for separating particulate matter 失效
    颗粒物分离方法及系统

    公开(公告)号：US20060081503A1

    公开(公告)日：2006-04-20

    申请号：US11254600

    申请日：2005-10-19

    申请人： Paul Wegner

    发明人： Paul Wegner

    IPC分类号： B03B7/00 ,  B07B13/05 ,  B07C5/12

    CPC分类号： B09C1/02 ,  B03B5/32 ,  B03B7/00 ,  E21B21/065 ,  Y10S209/915

    摘要： The present invention is directed to a system and method for continuously or substantially continuously separating particulate matter based on particle size and/or density of the matter. The system includes a separation chamber having a bottom portion disposed within a cavity of a rotatable bowl having fluid therein, preferably water. The internal cavity of the separation chamber is maintained under negative pressure such that fluid is drawn through the separation chamber at a predetermined velocity to separate the solids. Larger, dewatered and/or denser solids are directed to the cavity of the rotatable bowl and can be removed by rotation of the bowl while the smaller and/or less dense solids and fluid travel up through the separation chamber.

    摘要翻译： 本发明涉及一种用于基于物质的粒度和/或密度连续或基本上连续分离颗粒物质的系统和方法。 该系统包括分离室，其具有设置在其中具有流体的可旋转碗的空腔内的底部，优选地为水。 分离室的内腔保持在负压下，使得流体以预定速度被抽吸通过分离室以分离固体。 更大，脱水和/或更致密的固体被引导到可旋转碗的空腔，并且可以通过碗的旋转而移除，同时较小和/或较不致密的固体和流体向上通过分离室。

    Agent for the separation of dissolved and/or undissolved materials of different buoyancy densities or densities by means of solutions of true metatungstates
    7.
    发明授权
    Agent for the separation of dissolved and/or undissolved materials of different buoyancy densities or densities by means of solutions of true metatungstates 失效
    通过真正的偏钨酸盐溶液分离不同浮力密度或密度的溶解和/或未溶解材料的试剂

    公开(公告)号：US4557718A

    公开(公告)日：1985-12-10

    申请号：US567693

    申请日：1984-01-03

    申请人： Rainer Kamps ,  Bodo Plewinsky ,  Manfred Miehe ,  Klaus Wetz

    发明人： Rainer Kamps ,  Bodo Plewinsky ,  Manfred Miehe ,  Klaus Wetz

    IPC分类号： B03B5/32 ,  B03B5/44 ,  B01D21/26

    CPC分类号： B03B5/442 ,  B03B5/32 ,  B03D3/00

    摘要： The separation of dissolved and/or undissolved materials having different densities or different buoyancy densities can be effected with the aid of agents comprising solutions of true metatungstates. In the case of a separation of materials having different buoyancy densities by means of a density gradient centrifugation, the agent has the form of an aqueous solution of an alkali, ammonium or alkaline earth metal metatungstate and, if desired, may be augmented by the addition of at least one low molecular weight electrolyte. The agent can have a density of up to 3.1 g.cm.sup.-3, has a low viscosity at high concentrations, and is neutral and chemically insert. In the case of a separation of water-insoluble solid mixtures of different densities, the densities of the solutions of the true metatungstates can be increased up to 4.6 g.cm.sup.-3 by adding to the solutions high density materials such as sodium tungstate or tungsten carbide of suitable grain size so as to form a suspension.

    摘要翻译： 借助于包含真正的偏钨酸盐溶液的试剂，可以分离具有不同密度或不同浮力密度的溶解和/或未溶解材料。 在通过密度梯度离心分离具有不同浮力密度的材料的情况下，试剂具有碱金属，铵或碱土金属偏钨酸盐的水溶液的形式，并且如果需要，可以通过加入增加 的至少一种低分子量电解质。 该试剂的密度可达3.1g·cm-3，在高浓度下具有较低的粘度，且为中性和化学插入。 在分离不同密度的水不溶性固体混合物的情况下，通过向溶液中加入高密度材料如钨酸钠或钨，可以将真正的偏钨酸盐溶液的密度增加至4.6g / cm 3 碳化物合适的晶粒尺寸以形成悬浮液。

    Centrifuge processing of high-solids clay
    8.
    发明授权
    Centrifuge processing of high-solids clay 失效
    离心机处理高固体粘土

    公开(公告)号：US4018673A

    公开(公告)日：1977-04-19

    申请号：US662135

    申请日：1976-02-27

    申请人： Randall E. Hughes ,  Edward P. Jordan

    发明人： Randall E. Hughes ,  Edward P. Jordan

    IPC分类号： B03B5/32 ,  B03B1/04

    CPC分类号： B03B5/32

    摘要： Method of removing coarse materials and chemical and mineral impurities from clay in order to produce a purified high solids suspension of said clay which method involves mixing a crude clay with water and a dispersing agent to form a high solids slurry; subjecting said slurry to intense centrifugal forces for a short period of time; separating said coarse material and said chemical and mineral impurities; and recovering the suspended clay as a fine fraction having a reduced content of coarse material and impurities.

    摘要翻译： 从粘土中除去粗物质和化学和矿物杂质以便产生所述粘土的纯化高固体悬浮液的方法，该方法包括将粗粘土与水和分散剂混合以形成高固体浆料; 在短时间内对所述浆料进行强烈的离心力; 分离所述粗物质和所述化学和矿物杂质; 并将悬浮的粘土作为粗品和杂质含量低的精细馏分进行回收。

    Method and apparatus for continuous classification of solid particles dispersed in afluid carrier
    9.
    发明授权
    Method and apparatus for continuous classification of solid particles dispersed in afluid carrier 失效
    固体颗粒分散在载体中的连续分级方法和装置

    公开(公告)号：US3351195A

    公开(公告)日：1967-11-07

    申请号：US35277164

    申请日：1964-03-18

    申请人： TAPANI HUKKI RISTO

    发明人： TAPANI HUKKI RISTO

    IPC分类号： B01D21/00 ,  B03B5/32 ,  B03B5/62 ,  B04C5/107

    CPC分类号： B04C5/107 ,  B01D21/0018 ,  B01D21/02 ,  B01D21/26 ,  B01D21/267 ,  B03B5/32 ,  B03B5/623

    摘要： 962,386. Centrifugal classifiers. INSINOORITOIMISTO - ENGINEERING BUREAU R. T. HUKKI. April 8, 1963, No. 13847/63. Heading B2P. An open-topped vessel for the continuous hydraulic classification of pulps and suspensions of finely divided solid particles comprises a cylindrical top portion 1, a conical bottom portion 2, a pipe 13 for admitting feed, preferably by gravitational flow, a rotary impeller 4 for imparting circular motion to the feed in the portion 2 and for effecting discharge of the coarse size fraction via the apex of the cone, and braking means to eliminate the circular motion of the feed within an annular layer situated against the inside wall of the portion 1, whereby the fine size fraction is obtained in the form of an ascending, substantially laminar, continuous flow over the edge 10 of the portion 1 and is collected into a launder 11. The diameter of the top portion 1 may be smaller than that of the top of the conical portion 2. The braking means comprise vanes 8 mounted on an open-topped cylinder 8 which may be provided with a truncated cone 7 at its lower end. The braking means may be vertically adjustable and may be so designed as to provide a narrowing annular channel for the ascending fine fracton flow. The vanes 8 may be angularly adjustable. The coarse fraction may be washed by water admitted tangentially under pressure through a pipe 12. A manually or automatically operated valve 5 is provided for the discharge of the coarse fraction. A number of classifiers may be arranged in series or parallel.