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    • 9. 发明申请
    • NON-BRAIDED REINFORCED HOLLOW FIBRE MEMBRANE
    • 非增强加强中空纤维膜
    • WO2010108285A1
    • 2010-09-30
    • PCT/CA2010/000469
    • 2010-03-26
    • ASTEIA TECHNOLOGY INC.COTE, Pierre Lucien
    • COTE, Pierre Lucien
    • B01D67/00B01D63/04B01D69/08
    • B01D69/08B01D69/02B01D69/085B01D2325/40Y10T29/49826
    • A hollow fiber membrane has a reinforcing structure with a plurality of reinforcing filaments embedded in the wall of the membrane. The reinforcing filaments may include warp filaments, which are substantially continuous along the length of the membrane, and one or more warp filaments, which extend obliquely between two or more warp filaments. The warp filaments may be in the form of a spiral, a zigzag or a set of discontinuous filament segments. The reinforcing filaments are not woven together, but they may be bonded at points of contact where they intersect each other. The bonding may be by heat, solvent, or UV-activation. The filaments may have an outer layer with a polymer that responds to the bonding method. The membrane preferably has an inside diameter to outside diameter ratio larger than 0.60. The reinforcing structure may be impregnated with a membrane dope in a continuous operation in which the reinforcing structure formation and dope impregnation are done one after the other at the same speed.
    • 中空纤维膜具有加强结构,其中多个加强丝嵌入膜的壁中。 增强丝可以包括沿着膜的长度基本上连续的经丝,以及在两根或多根经丝之间倾斜延伸的一根或多根经丝。 经丝可以是螺旋状,锯齿形或一组不连续的细丝段的形式。 增强丝不织在一起,但是它们可以在它们彼此相交的接触点处结合。 接合可以通过加热,溶剂或UV活化。 长丝可以具有对结合方法作出响应的聚合物的外层。 膜的内径与外径的比优选大于0.60。 加强结构可以在连续操作中浸渍膜掺杂物,其中以相同的速度一个接一个地进行加强结构形成和掺杂浸渍。
    • 10. 发明申请
    • WASTEWATER TREATMENT WITH AEROBIC GRANULES
    • 废水处理与无机颗粒
    • WO2008141413A1
    • 2008-11-27
    • PCT/CA2007/000893
    • 2007-05-18
    • ZENON TECHNOLOGY PARTNERSHIPCOTE, Pierre LucienBEHMANN, HenryCHANG, Sheng
    • COTE, Pierre LucienBEHMANN, HenryCHANG, Sheng
    • C02F9/14C02F1/52C02F11/04C02F3/30
    • C02F3/223C02F3/006C02F3/1268C02F3/30C02F3/301Y02W10/15
    • A wastewater treatment system using aerobic granules has a large number of sequencing batch reactor tanks with high volumetric exchange rate, a variable cycle length and constant batch volume. The batch reactors are operated for C, N removal and P is removed chemically. SS are removed in a downstream separation step. A continuous flow reactor may comprise an aerobic zone, an alternately aerobic and anoxic zone or discrete aerobic and anoxic zones, and a settling zone. An anaerobic zone may be located at the bottom of a mass of settled granules. Feed may be introduced through the settled granules. An aerobic/anoxic zone may be like a CSTR but with aeration varying in space or time. Sludge granules may move intermittently from an aerobic zone to an aerobic/anoxic zone. A settling zone may have an upflow rate to wash off flocculated biomass. A dual sludge process may be used in which a fraction of unsettled floc is recycled to a region upstream of the granules settler. A fermentation zone may be used to pre-treat feed water or to treat a recycled waste stream, for example a waste stream contain floc.
    • 使用有氧颗粒的废水处理系统具有大量的具有高体积交换速率,可变循环长度和恒定批量体积的间歇式反应釜。 操作间歇式反应器用于C,N去除,P被化学去除。 SS在下游分离步骤中被去除。 连续流动反应器可包括需氧区,交替需氧和缺氧区或离散的有氧和缺氧区以及沉降区。 厌氧区可以位于大量沉降颗粒的底部。 饲料可以通过沉降的颗粒引入。 有氧/缺氧区域可能类似于CSTR,但是曝气在空间或时间上变化。 污泥颗粒可以间歇地从需氧区移动到需氧/缺氧区。 沉降区可以具有上升流速以洗脱絮凝生物质。 可以使用双重污泥方法,其中一部分不稳定的絮体再循环到颗粒沉降器上游的区域。 发酵区可用于预处理给水或处理回收的废物流,例如含有絮凝物的废物流。