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    • 6. 再颁专利
    • Vertical cylindrical skein of hollow fiber membranes and method of maintaining clean fiber surfaces
    • 中空纤维膜的垂直圆柱形丝杠和保持清洁的纤维表面的方法
    • USRE42669E1
    • 2011-09-06
    • US09621234
    • 2000-07-20
    • Wayne Jerald HenshawMailvaganam MahendranHenry Behmann
    • Wayne Jerald HenshawMailvaganam MahendranHenry Behmann
    • B01D65/02B01D61/00B01D63/00C02F9/00
    • B01D65/08B01D61/18B01D61/20B01D63/02B01D63/021B01D63/022B01D63/023B01D63/026B01D63/043B01D65/02B01D69/02B01D2313/26B01D2315/06B01D2321/04B01D2321/185B01D2321/2066C02F1/444
    • A gas-scrubbed vertical cylindrical skein of “fibers” has their opposed terminal portions held in headers unconfined in a modular shell, and aerated with a cleansing gas supplied by a gas-distribution means which produces a mass of bubbles serving the function of a scrub-brush for the outer surfaces of the fibers. The skein is surprisingly effective with relatively little cleansing gas, the specific flux through the membranes reaching an essentially constant relatively high value because the vertical deployment of fibers allows bubbles to rise upwards along the outer surfaces of the fibers. The effectiveness is critically dependent upon the length of each fiber in the skein. That length is in the range from at least 0.1% more than the fixed distance between opposed faces of the skein's headers, but less than 5% greater than the fixed distance. Lack of tension allows the fibers to sway in bubbles flowing along their outer surfaces making them surprisingly resistant to being fouled by buildup of deposits of inanimate particles or microorganisms in the substrate. For use in a large reservoir, a bank of skeins is used with a gas distributor means which has fibers preferably >0.5 meter long, which together provide a surface area >10 m2. The terminal end portions of fibers in each header are kept free from fiber-to-fiber contact with a novel method of forming a header.
    • 气体洗涤的“纤维”的垂直圆柱形绞丝具有相对的端部部分保持在集管中,未封闭在模块化壳体中,并且由气体分配装置供应的清洁气体充气,其产生用于擦洗功能的大量气泡 刷子用于纤维的外表面。 通过相对较少的清洁气体,绞丝是非常有效的,通过膜的比流量达到基本上恒定的相对高的值,因为纤维的垂直展开允许气泡沿着纤维的外表面向上升起。 其效果在很大程度上取决于丝束中每根纤维的长度。 该长度在比绞合头的相对面之间的固定距离多至少0.1%的范围内,但小于固定距离的5%。 缺乏张力允许纤维在其外表面流动的气泡中摆动,使得它们惊人地抵抗由于底物中无生命的颗粒或微生物沉积物的沉积而被污染。 为了在大型储存器中使用,一串绞线与气体分配器一起使用,该装置具有优选> 0.5米长的纤维,它们一起提供了大于10m 2的表面积。 通过形成集管的新颖方法,使每个集管中的纤维的末端部分保持无纤维与纤维的接触。
    • 7. 发明授权
    • Flow-through aerobic granulator
    • 流通好氧造粒机
    • US07459076B2
    • 2008-12-02
    • US11642544
    • 2006-12-21
    • Pierre Lucien CoteHenry Behmann
    • Pierre Lucien CoteHenry Behmann
    • B01D24/00
    • C02F3/301C02F3/223C02F2203/004Y02W10/15
    • A continuous flow reactor or method promotes aerobic granule formation. The reactor may comprise three or four zones that may comprise one or more of an aerobic zone, an alternately aerobic and anoxic zone or discrete aerobic and anoxic zones, and a settling zone. The reactor may have a single sludge removal flow. An anaerobic zone may be located at the bottom of a mass of settled granules. Feed may be introduced through the settled granules generally in a plug flow. An aerobic/anoxic zone may be structured or operated partially like a continuously stirred tank reactor (CSTR) but with aeration varying in space or time. Sludge granules may move intermittently from an aerobic zone to an aerobic/anoxic zone, for example by an air lift pump. A settling zone may have an upflow of >4 m/hr or >5 m/hr and wash off flocculated biomass.
    • 连续流动反应器或方法促进好氧颗粒形成。 反应器可以包括三个或四个区域,其可以包括好氧区,交替需氧和缺氧区或离散的需氧和缺氧区中的一个或多个,以及沉降区。 反应器可以具有单个污泥去除流。 厌氧区可能位于大量沉降颗粒的底部。 进料可以通过沉淀的颗粒通常以活塞流引入。 有氧/缺氧区域可以像连续搅拌的罐式反应器(CSTR)一样构造或部分运行,但是在空间或时间上具有变化的曝气。 污泥颗粒可以从好氧区间歇地移动到需氧/缺氧区域,例如通过空气提升泵。 沉降区可以具有> 4m / hr或> 5m / hr的上流,并且清除絮凝生物质。
    • 9. 发明申请
    • Flow-through aerobic granulator
    • 流通好氧造粒机
    • US20070158265A1
    • 2007-07-12
    • US11642544
    • 2006-12-21
    • Pierre CoteHenry Behmann
    • Pierre CoteHenry Behmann
    • C02F3/30
    • C02F3/301C02F3/223C02F2203/004Y02W10/15
    • A continuous flow reactor or method promotes aerobic granule formation. The reactor may comprise three or four zones that may comprise one or more of an aerobic zone, an alternately aerobic and anoxic zone or discrete aerobic and anoxic zones, and a settling zone. The reactor may have a single sludge removal flow. An anaerobic zone may be located at the bottom of a mass of settled granules. Feed may be introduced through the settled granules generally in a plug flow. An aerobic/anoxic zone may be structured or operated partially like a continuously stirred tank reactor (CSTR) but with aeration varying in space or time. Sludge granules may move intermittently from an aerobic zone to an aerobic/anoxic zone, for example by an air lift pump. A settling zone may have an upflow of >4 m/hr or >5 m/hr and wash off flocculated biomass.
    • 连续流动反应器或方法促进好氧颗粒形成。 反应器可以包括三个或四个区域,其可以包括好氧区,交替需氧和缺氧区或离散的需氧和缺氧区中的一个或多个,以及沉降区。 反应器可以具有单个污泥去除流。 厌氧区可能位于大量沉降颗粒的底部。 进料可以通过沉淀的颗粒通常以活塞流引入。 有氧/缺氧区域可以像连续搅拌的罐式反应器(CSTR)一样构造或部分运行,但是在空间或时间上具有变化的曝气。 污泥颗粒可以从好氧区间歇地移动到需氧/缺氧区域,例如通过空气提升泵。 沉降区可以具有> 4m / hr或> 5m / hr的上流,并且清除絮凝生物质。