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    • 76. 发明申请
    • JET MILL
    • 喷气机
    • US20130186993A1
    • 2013-07-25
    • US13812638
    • 2011-07-28
    • Masahiro YoshikawaTomoyuki ChibaTakashi Shibata
    • Masahiro YoshikawaTomoyuki ChibaTakashi Shibata
    • B02C19/06
    • B02C19/06B02C19/066B02C19/068B02C23/12B07B7/083B07B7/086
    • Disposed is a jet mill that has a cylindrical pulverization chamber (10) and a classification chamber (6) that connects to the pulverization chamber (10). A fine-powder discharge port (4a) and a classification rotor (7) are provided in the classification chamber (6). A feedstock supply port (5) and at least one gas emission nozzle (11) are provided in the pulverization chamber (10). The shape of the classification chamber (6) is a cone that starts on the inner wall of the pulverization chamber (10), and is angled towards the classification rotor (7). This configuration gives the jet mill high efficiency of pulverization and reduces the amount of powders left in the chamber when the jet mill has finished running.
    • 设置有具有连接到粉碎室(10)的圆柱形粉碎室(10)和分级室(6)的喷射式粉碎机。 在分级室(6)中设置有细粉末排出口(4a)和分级转子(7)。 原料供给口(5)和至少一个排气喷嘴(11)设置在粉碎室(10)中。 分级室(6)的形状是从粉碎室(10)的内壁开始朝向分级转子(7)倾斜的锥体。 这种配置给喷射磨机提供了高效率的粉碎,并且当喷射磨机运行完毕时,减少了腔室中留下的粉末的量。
    • 77. 发明申请
    • DRY GRANULATION IN A GAS STREAM
    • 气流干燥造粒
    • US20110220745A1
    • 2011-09-15
    • US13127865
    • 2009-11-04
    • Giovanni Politi
    • Giovanni Politi
    • B02C23/24
    • B01J2/22B07B7/086B30B11/16
    • An apparatus wherein the gas enters from an opening 4 located in a part of a compaction chamber 3 and is dragged through a granulator 5, a fractioning device 12, a special cyclone 11 and a filter system 8A to a suction fan, which creates a gas stream. In such apparatus the bulk to be compacted 1, the fine particles to be compacted again and the compacted bulk have the same flow direction than the carrier gas. Due to its complete or partial impermeability, the structure of the apparatus makes also possible the use of a gas different from normal air. This is important when the bulk is sensible to oxygen.
    • 一种装置,其中气体从位于压实室3的一部分的开口4进入,并且通过造粒机5,分馏装置12,特殊旋风分离器11和过滤器系统8A拖到吸风机上,从而产生气体 流。 在这种装置中,要压实的体积1,再次压实的细颗粒和压实块体具有与载气相同的流动方向。 由于其完全或部分不可渗透性,装置的结构也可能使用与正常空气不同的气体。 当体积对氧气敏感时,这很重要。
    • 79. 发明授权
    • Classification apparatus for powdery substance
    • 粉状物质分类仪器
    • US07735658B2
    • 2010-06-15
    • US12161906
    • 2007-01-23
    • Jusuke HidakaShinzo YoshikadoYoshiyuki ShirakawaYoshiaki ItoKiyoshi HayakawaYuuko Watanabe
    • Jusuke HidakaShinzo YoshikadoYoshiyuki ShirakawaYoshiaki ItoKiyoshi HayakawaYuuko Watanabe
    • B04C5/12
    • B01F13/0818B01F13/0255B03C1/286B03C3/14B07B7/01B07B7/086
    • A classification apparatus including a magnetic stirrer composed of main body (1) and rotor (2) and, arranged on the main body of the magnetic stirrer, classification tube (3). The interior of the classification tube is provided with classification compartments (A-E) partitioned from each other by divider plates (5a-5b). The lowermost classification compartment (A) is furnished with gas emission conduit (7). In the classification compartment (A), the rotor (2) of the magnetic stirrer is arranged. From gas supply source (8), a high-pressure gas is fed into the gas emission conduit. By means of the gas emitted from the gas emission conduit, a vortex flow rising from the lowermost classification compartment sequentially toward higher classification compartments is generated in the classification tube. Simultaneously, the rotor of the magnetic stirrer is rotated, so that powdery substance (O) within the classification compartment (A), while being conveyed by the vortex flow, undergoes particle size classification in each of the classification compartments.
    • 一种分级装置,包括由主体(1)和转子(2)组成的磁力搅拌器,并且配置在磁力搅拌器的主体上,分级管(3)。 分级管的内部设置有通过分隔板(5a-5b)彼此分隔的分级室(A-E)。 最下面的分类室(A)配有气体排放导管(7)。 在分级室(A)中,设置磁力搅拌器的转子(2)。 从气体供给源(8)向高压气体供给气体。 通过从气体排放导管排出的气体,在分级管中产生从最下层分级室顺序向上分级室升起的涡流。 同时旋转磁力搅拌器的转子,使分类室(A)内的粉末状物质(O)在被涡流输送的同时在每个分级室中进行粒度分级。