首页> 外国专利> MEMBRANE Ultra-microfiltration rolls ELEMENT AND METHOD improve its capacity

MEMBRANE Ultra-microfiltration rolls ELEMENT AND METHOD improve its capacity

机译:膜超微滤辊ELEMENT AND METHOD提高其容量

摘要

1.membrane ultra u043cu0438u043au0440u043eu0444u0438u043bu044cu0442u0440u0430u0446u0438u043eu043du043du044bu0439 first element u0441u043eu0441u0442u043eu00a0u0449u0438u0439 of leachate is u043eu0442u0432u043eu0434u00a0u0449u0435u0439 u043fu0435u0440u0444u043eu0440u0438u0440u043eu0432u0430u043du043du043eu0439 tube, spiral u043du0430u043cu043eu0442u0430u043du043du044bu0445 her through u0442u0443u0440u0431u0443u043bu0438u0437u0430u0442u043eu0440 by the net membrane packages containing suction in the canvas and a semipermeable membrane, and u0443u043fu043bu043eu0442u043du00a0u044eu0449u0435u0439 cuffs located on one of the pane ends endless element and, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 orderthe suction in the painting is composed of two superimposed each other sheets, grooves which are located inside the double u0441u043bu043eu00a0 and form the general drainage channels; u0441u043du0430u0440u0443u0436 and the first element is free to exit u0442u0443u0440u0431u0443u043bu0438u0437u0430u0442u043eu0440u043eu0432, u0440u0430u0437u0434u0435u043bu00a0u044eu0449u0438u0445 membrane packagesand wrapped u0442u0443u0440u0431u0443u043bu0438u0437u0430u0442u043eu0440u043du043eu0439 mesh; u0443u043fu043bu043eu0442u043du00a0u044eu0449u0430u00a0 cuff located at the opposite end of the fluid on the endless element and has u0444u0438u043bu044cu0442u0440u0443u0435u043cu043eu0439 the outer diameter selected from the u0441u043eu043eu0442u043du043eu0448u0435u043du0438u00a0 dm = d + (5 - 10 mm, where d is the diameter of the endless element, mm, d = d + 2, d is the outer diameter of the element after the endless u043cu043eu0442u043au0438 membrane packages.the u0441u043bu043eu00a0 external u0442u0443u0440u0431u0443u043bu0438u0437u0430u0442u043eu0440u043du043eu0439 nets, mm.;2. membrane ultra u043cu0438u043au0440u043eu0444u0438u043bu044cu0442u0440u0430u0446u0438u043eu043du043du044bu0439 element on the first 1, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0, membrane packages have shape close to a square.;3. method u0432u043eu0441u0441u0442u0430u043du043eu0432u043bu0435u043du0438u00a0 efficiency of membrane ultra u043cu0438u043au0440u043eu0444u0438u043bu044cu0442u0440u0430u0446u0438u043eu043du043du043eu0433u043e endless element of design in accordance with the ap.1 and 2, by washing liquid, u043fu043eu0434u0430u0432u0430u00a0 her through the u0434u0432u0438u0436u0435u043du0438u00a0 u0444u0438u043bu044cu0442u0440u0443u0435u043cu043eu0439 environment, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0, which leads in two phases: in the first stage, the first element of the ol wash leachate, owing, u043fu043eu0434u0430u0432u0430u00a0 him across the line of withdrawal u043fu0440u043eu0442u0438u0432u043eu0442u043eu0447u043du043e leachate to flow from 0.5 to 10.0 m3 / h for 2 to 10; in the second stage, the first element of the process the water air mixture in the ratio of 5 to 30 large parts of air to 1 part in 3d yeah, u043fu043eu0434u0430u0432u0430u00a0 this mixture through u0434u0432u0438u0436u0435u043du0438u00a0 u0444u0438u043bu044cu0442u0440u0443u0435u043cu043eu0439 environment with consumption of from 1.0 to 15 m3 / h for from 2 to 10.
机译:1.膜超 u043c u0438 u043a u0440 u043e u0444 u0438 u043b u044c u0442 u0440 u0430 u0446 u0438 u043e u043d u043d u043b u044b u0439第一个元素 u0441 u043e u043e u0442 u043e u00a0 u0449 u0438 u0439的浸出液是 u043e u0442 u0432 u043e u0434 u00a0 u0449 u0435 u0439 u043f u043f u0435 u0440 u0444 u043e u0440 u04438 u043e u043e u0432 u0430 u043d u043d u043e u0439管,螺旋形 u043d u0430 u043c u043c u043e u0442 u0430 u043d u043d u043d u044b u04b她通过 u0442 u0443 u0440 u0431 u0443 u043b u0438 u0437 u0430 u0442 u043e u0440,其中包含在帆布上的吸力和半透膜的网膜包装,以及 u0443 u043f u043b u043e u0442 u043d u00a0 u044e u044e u0449 u0435 u0439位于一个窗格末端无端元件上的袖口,并且 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0顺序绘画中的吸力由两张彼此叠置的薄片组成,位于双 u0441 u043b u043e u00a0内并形成普通排水槽的沟槽通道 u0441 u043d u0430 u0440 u0443 u0436,第一个元素可以自由退出 u0442 u0443 u0440 u0431 u0443 u043b u0438 u0437 u0430 u0442 u0432 u043e u0440 u043e u0432, u0440 u0430 u0437 u0434 u0435 u043b u00a0 u044e u0449 u0438 u0445膜包装并包裹着 u0442 u0443 u0440 u0431 u0443 u043b u0438 u0437 u0430 u0442 u043e u0440 u043e u0439网格; u0443 u043f u043b u043e u0442 u043d u00a0 u044e u0449 u0430 u00a0袖带位于环形元件上流体的另一端,并且具有 u0444 u0438 u043b u043b u043c u044c u0442 u0440 u0443 u0435 u043c u043e u0439选自 u0441 u043e u043e u043e u0442 u043d u043e u0448 u0435 u043d u0438 u00a0 dm = d +(5-10 mm,其中d为环形元件的直径,mm,d = d + 2,d是环形 u043c u043e u0442 u043a u0438膜包装后的元件外径。 u0441 u043b u043e u00a0外部 u0442 u0443 u0440 u0431 u0443 u043b u0438 u0437 u0430 u0442 u043e u0440 u043d u043e u0439蚊帐,毫米; 2。膜超 u043c u0438 u043a u0440 u043e u0444 u0438 u043b u044c u0442 u0440 u0430 u0446 u0438 u043e u043d u043d u043d u044b u0439元素位于前1个元素上, u043e u0442 u043b u0438 u0447 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0,膜包装的形状接近正方形; 3。方法 u0432 u043e u0441 u0441 u0442 u0430 u043d u043d u043e u0432 u043b u0435 膜超膜的效率按照第1章和第2章设计的设计元素,通过洗涤液体 u043f u043e u0434 u0430 u0432 u0430 u00a0通过 u0434 u0432 u0438 u0436 u0435 u043d u0438 u00a0 u0444 u0438 u043b u044c u0442 u0440 u0443 u0435 u043c u043e u043e u0439环境, u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0449 u0438 u0439 u0441 u00a0,导致分两个阶段:在第一阶段,ol洗涤渗滤液的第一个元素欠他 u043f u043e u0434 u0430 u0432 u0430 u00a0他跨越提款线 u043f u0440 u043e u0442 u0438 u0432 u043e u0442 u043e u0447 u043d u043e渗滤液从0.5到10.0 m3 / h的流量为2到10;在第二阶段中,过程的第一个元素是水空气混合物,其比例为5到30大空气与3d中的1空气, u0434 u0432 u0438 u0436 u0435 u043d u0438 u00a0 u0444 u0438 u043b u044c u0442 u0440 u0443 u0435 u043c u043e u0439环境的消耗为1.0到15立方米/小时从2到10

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