Sedimentation field flow fractionation
    3.
    发明公开
    Sedimentation field flow fractionation 失效
    现场流场分析

    公开(公告)号:EP0081315A3

    公开(公告)日:1985-05-29

    申请号:EP82306229

    申请日:1982-11-23

    CPC classification number: B04B5/0442 B03B5/00 G01N30/0005 G01N30/62 G01N30/42

    Abstract: Sedimentation field flow fractionation apparatus having a rotor-mounted fractionation column, has detectors positioned to observe the fluids from the column while still in the rotor. Designs include parallel reference and fractionation columns having their outflows compared in a rotor-mounted fluid flow density balance. Optionally weired channel columns provide a free fluid surface for more efficient resolution. Horizontal rotational axes are preferred. Rotor-mounted fluid flow density balances are also provided which are suitable for detecting liquid density changes in the other applications, such as liquid chromatography.

    Apparatus for field flow fractionation
    4.
    发明公开
    Apparatus for field flow fractionation 失效
    现场流量分析装置

    公开(公告)号:EP0035394A3

    公开(公告)日:1983-03-16

    申请号:EP81300839

    申请日:1981-02-27

    Abstract: A long, thin annular belt-like channel is shown for use in sedimentation field flow fractionation. This channel, which may be contained in the rotor of a centrifuge, has a generally rectangular cross-section and inner and outer walls 22, 23. It has an inlet tube 100 which extends through the inner channel wall 23 and is positioned to introduce particulates 25 (including particles and/or macromolecules) approximately at the radial distance 1 from the outer wall where 1 is the equilibrium distance resulting from the average force field exerted on each particulate by the centrifugal force field and by the opposing normal diffusion forces due to Brownian motion. An outlet tube 104 for the channel is similarly located. A modified design tapers the channel at the inlet and/or outlet.

    Rotor for sedimentation field flow fractionation
    6.
    发明公开
    Rotor for sedimentation field flow fractionation 失效
    转子用于沉降场流分馏

    公开(公告)号:EP0035398A3

    公开(公告)日:1983-03-23

    申请号:EP81300843

    申请日:1981-02-27

    CPC classification number: B04B5/0442 B03B5/00 B04B2005/045 G01N2030/002

    Abstract: A long, thin annular belt-like channel is designed for use in sedimentation field flow fractionation. This channel, which is the rotor of a centrifuge, is designed to maintain its thickness dimension constant and yet facilitate its manufacture and cleaning by forming the rotor of a double mating ring in which the inner ring 58 is split at 60. This permits the inner ring 58 to conform to the outer load carrying ring 56. The channel is defined by groove 70 and the inner ring is urged against the outer ring 56 by wedges 69. Ports 12 and 14 give fluid access to the channel 70.

    Abstract translation: 长而薄的环形带状通道设计用于沉积场流分馏。 该通道是离心机的转子,其被设计成保持其厚度尺寸恒定,并且通过形成其中内环58在60处分开的双配合环的转子来促进其制造和清洁。这允许内部 环58与外承载环56相一致。通道由凹槽70限定并且内环通过楔69被推靠在外环56上。端口12和14给流体通道70提供流体通路。

    WET PROCESS FOR THE CLASSIFICATION OF SUPER FINES
    7.
    发明申请
    WET PROCESS FOR THE CLASSIFICATION OF SUPER FINES 审中-公开
    方法湿FEINSTKORNKLASSIERUNG

    公开(公告)号:WO1998005429A1

    公开(公告)日:1998-02-12

    申请号:PCT/EP1997004212

    申请日:1997-08-01

    Abstract: Wet process for the classification of super fine particles, especially to obtain fines with a very small maximum grain size and to produce particles with a narrow particle-size distribution. The average and maximum size of fines can be significantly reduced in comparison with previous wet classification methods for fine grains. The process is characterized by low energy consumption and a constructively simple design. According to the invention the process consists of two steps. In the first step the suspension to be classified is filtered using a cross flow filtration module (2) with a constant flow rate of the suspension in the module and a constant regulated filtrate flow (6, 7), whereby the fines (3) are deposited as a layer of particles on the microporous filter areas or membrane surfaces of the module. In the second step a fine grained product is obtained from the deposited layer of particles by placing cross flow filtration modules in the circulatory or cascade system.

    Abstract translation: 一种用于在超范围内的颗粒的湿分级工艺,特别是用于获得具有非常小的上部粒径微细的固体和用于与窄粒径分布的颗粒制造。 相比bisherigem湿Feinstkornklassieren细材料的中部和上部粒径可以显著降低。 该方法的特征在于,低功率消耗和简单的结构。 本发明的方法包括的步骤的两个阶段。 在第一处理步骤中,细料(3)具有在模块中的悬浮液的恒定流速和设定的常数滤液流(6,7)通过过滤所保持的颗粒层被分类悬浮液与错流过滤模块(2),并在微孔过滤器表面上的预先设定的 从模块或膜的表面。 在第二工艺步骤中沉积的颗粒层通过干式或湿式清洗作为Feingutprodukt获得。 本发明方法的有利的实施例从在循环或级联电路交叉流过滤模块的安排产生的。

    A METHOD, DEVICE AND COMPOSITION IN MATERIAL SPRAYING
    8.
    发明申请
    A METHOD, DEVICE AND COMPOSITION IN MATERIAL SPRAYING 审中-公开
    材料喷涂中的方法,装置和组成

    公开(公告)号:WO1995009696A1

    公开(公告)日:1995-04-13

    申请号:PCT/SE1994000925

    申请日:1994-10-05

    Applicant: WILJE, Oscar

    CPC classification number: B07B1/46 B03B5/00 B05B3/0427 B07B1/22 B07B1/55

    Abstract: The invention relates to a method for spraying a material (5), characterized in that a spraying medium is supplied to the material as a movable member (2), which is provided with outlets (4) for the spraying medium, is set in motion. The invention also relates to a device for spraying a material, characterized in that it comprises a movably arranged, movable member (2) provided with first outlets (4) for a spraying medium. Thereby, a spraying medium is given such a motion in relation to the material that the outcome of the spraying, e.g. during washing, is just as good as or better than that of the prior art, in spite of the considerably lower consumption of the medium in question. The invention also relates to a rotatably arranged nozzle.

    Abstract translation: 本发明涉及一种用于喷涂材料(5)的方法,其特征在于向所述材料供应喷射介质作为可移动构件(2),所述可移动构件设置有用于喷射介质的出口(4) 。 本发明还涉及一种用于喷射材料的装置,其特征在于,其包括可移动地布置的可移动构件(2),其设置有用于喷射介质的第一出口(4)。 因此,给予喷涂介质相对于材料的这种运动,例如喷涂的结果。 在洗涤期间,与现有技术同样好或更好,尽管所讨论的介质的消耗相当低。 本发明还涉及可旋转地布置的喷嘴。

    APPARATUS FOR THE RECLAMATION OF AGGREGATE FROM WASTE CONCRETE
    9.
    发明申请
    APPARATUS FOR THE RECLAMATION OF AGGREGATE FROM WASTE CONCRETE 审中-公开
    废弃物混合物回收装置

    公开(公告)号:WO1992009369A1

    公开(公告)日:1992-06-11

    申请号:PCT/GB1991002082

    申请日:1991-11-25

    Abstract: Aggregate is reclaimed from waste plastic concrete in apparatus which comprises a container (1) hinged (17) to a base (16). The container is divided by partitions (2, 3) into a washing tank (4), a settling tank (5) and a drain tank (6). The upper edge of each partition defines a weir (7, 8). Waste concrete is deposited into the washing tank (4) and subjected to the jetting action of water, together with entrained air, from pipes (9). Cement and fine aggregate are carried over the first weir (7) into the settling tank (5), coarse aggregate remaining in the washing tank (4). Cement and some aggregate fines are carried over the second weir (8), whilst the major proportion of the fine aggregate settles in the second tank (5). An oscillating paddle (13) assists the separation in that tank. A slurry of cement and aggregate fines is discharged from the third tank (6) via drain outlets (12) for further treatment in a settlement tank/pit or hydrocyclone. The separated aggregates are removed by tipping the container (1) about the hinge (17) to a discharging position.

    METHOD AND APPARATUS FOR CAPILLARY HYDRODYNAMIC FRACTIONATION
    10.
    发明申请
    METHOD AND APPARATUS FOR CAPILLARY HYDRODYNAMIC FRACTIONATION 审中-公开
    毛细血液动力分离方法与装置

    公开(公告)号:WO1990011832A1

    公开(公告)日:1990-10-18

    申请号:PCT/US1990001666

    申请日:1990-03-30

    Abstract: This invention provides an apparatus and method for the complete fractionation of submicron particles according to size by capillary hydrodynamic fractionation. This objective is achieved by using small diameter capillaries (18); introducing a minor fraction of a liquid dispersion of particles to be separated into at least one capillary fraction; passing the minor fraction through the capillary (18); and, at the exit of the capillary (18), diluting the minor fraction with the same liquid as is carrying the fractionated sample. These modifications in the flow patterns are essential to the use of capillaries (18) with diameters smaller than 60 microns. This invention is especially adapted for rapid analytical separation of not only rigid colloidal particles but also of soft latexes.

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