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    • 1. 发明专利
    • ELECTROMAGNETIC FILTER
    • JPS60118211A
    • 1985-06-25
    • JP22421583
    • 1983-11-30
    • HITACHI LTD
    • ITOU KAZUYUKIKUBOTA MASAYOSHIIZUMI KENKICHIHIROSE YASUO
    • B01D35/06B03C1/032G21C19/46
    • PURPOSE:To supply a large flow amount of a backwashing liquid within a short time at the time of backwashing without using a valve and a pump, by providing a nozzle and a throttle pipe on the way of piping and providing a flowline branch pipe from the opposed part or throttled part of the nozzle. CONSTITUTION:A raw solution is introduced into a filter tower 1 from a tank 3 and the solid substance in the raw solution is collected by a magnetic body. The treated solution issued from the filter tower 1 reaches a treating tank 32 through the flowline branch pipe of a nozzle or a throttle pipe 34. During this time, the treated solution is stored in a backwashing liquid storage tank 33. Backwashing operation is performed by such a way that an electromagnetic coil 3 is demagnetized after the raw solution in a tank 31 is entirely treated and pressurized gas is sent into the backwashing liquid tank 33 through piping 37. The backwashing liquid in the tank 33 is accelerated in its flow speed by a nozzle part D or a throttle pipe E and made remarkable in its directionality. Therefore, the greater part of the backwashing liquid is supplied to the direction of a pipe A and the treated liquid in the tank 32 is added to the backwashing liquid according to a condition and a large amount of the backwashing liquid is supplied to the filter tower 1 within a short time.
    • 6. 发明专利
    • VAPORIZER FOR LIQUIFIED GAS
    • JPS5672085A
    • 1981-06-16
    • JP14895379
    • 1979-11-19
    • HITACHI LTD
    • ITOU KAZUYUKIEBARA KATSUYANISHIMURA SHIGEOKITAKAHASHI SANKICHI
    • C10L3/06F17C9/02
    • PURPOSE:To reduce pumping energy for driving sea water or the like, in subjecting a liquefied gas and sea water or the like to the direct contact heat exchange under pressure, by utilizing a hydro static pressure of sea water or the like. CONSTITUTION:A surface 8 of sea water or fresh water in a liquefied gas vaporizer 1 is held so as to be positioned at a level lower than a free water surface 7 of sea water or fresh water 3 and, in a lower header 12, a distance H is set in such a condition that a hydrostatic pressure due to water head H between a gas-liquid interface of a liquefied gas and the sea water 3 and a fresh water surface 8 in higher than a desired pressure of a vaporized gas. Then, the sea water 3 is allowed to flow down into the vaporizer 1 through a valve 20 and liquefied gas 2 pressurized by a pump 21 is introduced into the header 12 from an injection nozzle 13 and directly contacted with sea water to be vaporized and the vaporized gas is collected in an upper header 11 while heated in a heat transfer pipe 10, and thereafter taken out as a high-pressure vaporized gas 4. On the other hand, a brine containing a water phase in the header 12 is introduced into a degassing apparatus 15 through a guide 14 to remove the vaporized gas 5.
    • 8. 发明专利
    • COLUMN FOR SEPARATING ION-EXCHANGE RESIN
    • JPS5892464A
    • 1983-06-01
    • JP19085081
    • 1981-11-30
    • HITACHI LTD
    • ITOU KAZUYUKIEBARA KATSUYANISHIMURA SHIGEOKITAKAHASHI SANKICHIKUBOTA SHIYOUJI
    • C02F1/42B01J49/00
    • PURPOSE:To withdrawn anion-exchange resin only without disturbing the layer of cation-exchange resin, by providing a gate in a manner such that its one end is placed at the side wall of a separating column while the other end is placed at a boundary surface between said resins, and means for withdrawing, opening or closing and sprinkling water at said part. CONSTITUTION:In a column 1 for separating ion-exchange resin, a gate 2 whose one end comes in contact with the side wall 1A of the separating column and whose other end is placed at the layer of ion-exchange resin is provided. The end 2A of the gate 2 at the layer of ion-exchange resin in arranged in a manner such that it comes at a boundary surface between the layer A of anion-exchange resin and the layer C of cation-exchange resin during withdrawing the layer A of the anion-exchange resin. In an annular space 3 between the gate 2 and the side wall 1A of the separating column, a means for opening or closing and means 4, 5 for sprinkling water from the upper or inner part of the resin layer are provided. Consequently, a water film is formed at the boundary surface, so that the anion-exchange resin only can be withdrawn without disturbing the layer of the cation-exchange resin during withdrawing the anion-exchange resin.
    • 9. 发明专利
    • Liquefied gas evaporator
    • 液化气体蒸发器
    • JPS57127197A
    • 1982-08-07
    • JP1022081
    • 1981-01-28
    • Hitachi Ltd
    • MUTSUKUSHI TOSHIMIEBARA KATSUYAITOU KAZUYUKITAKAHASHI SANKICHI
    • F17C9/02F17C7/04F17C13/00F23K5/00
    • F17C7/04F17C2201/0109F17C2223/0153F17C2227/0318
    • PURPOSE:To contrive to micrify bubbles flowing out of the jetting part of liquefied gas so as to prevent the heat-exchanging ability of the evaporator from lowering by a method wherein a discharge nozzle of liquefied gas is enclosed with a cover with an open lower end shaped in ziazag. CONSTITUTION:For the liquefied gas evaporator 1 which gasified liquefied gas by directly contacting with a heating medium such as sea water, fresh water or the like, the discharge nozzle 3 of the liquefied gas is enclosed with the cover 4 with the open lower end. The lower end of the cover 4 is located below the liquid surface of the heating medium and the gas-liquid boundary surface 5, which is held by the pressure of evaporated gas, is provided at the lower end 17 shaped in zigzag 19 of said cover 4. Accordingly, no large lump of bubble is generated from the jetting part of liquefied gas, resulting in enabling to obtain the liquefied gas evaporator with excellent heat-exchanging ability.
    • 目的:为了使流出液化气喷射部分的气泡微气雾化,以防止蒸发器的热交换能力降低,其中液化气体的排放喷嘴用敞开的下端封闭 形状在ziazag。 构成:对于通过与诸如海水,淡水等的加热介质直接接触来气化了液化气体的液化气体蒸发器1,液化气体的排放喷嘴3以敞开的下端与盖4一起包围。 盖4的下端位于加热介质的液面的下方,并且由蒸发气体的压力保持的气液边界面5设置在形成为所述盖的之字形19的下端17处 因此,从液化气体的喷射部分不产生大的气泡,从而能够获得具有优异的热交换能力的液化气体蒸发器。
    • 10. 发明专利
    • Method for mixing ion exchange resin for regeneration desalting device
    • 用于再生脱盐装置的离子交换树脂的混合方法
    • JPS5771643A
    • 1982-05-04
    • JP14838480
    • 1980-10-24
    • Hitachi Ltd
    • ITOU KAZUYUKIEBARA KATSUYANISHIMURA SHIGEOKITAKAHASHI SANKICHIKUBOTA SHIYOUJITAKASHIMA YOSHIE
    • C02F1/42B01J47/04
    • PURPOSE:To certainly exhibit capacity of a mixed bed type desalting device by a method wherein a pipe is arranged to a side surface of mixing tower to connect and communicate an upper part and a lower part of said tower and water and air are supplid into the connecting arranged pipe in an upwardly directed stream at a high speed to uniformly mix both anion and cation exchange resins. CONSTITUTION:To a side of a mixing tower, a connecting arranged pipe 2 connecting a lower part and an upper part of said tower is provided. In mixing an ion exchange resin, water 10 and air 11 are supplied into the mixing tower 1 through a nozzle and vigorously stirred in said tower 1. At the same time, water 10 and air 11 are supplied into the connecting arranged pipe 2 in an upwardly directed stream at a speed higher than that of a tower inside and the ion exchange resin in the lower part of the tower 1 is recirculated to the upper part of said tower 1. By this method, a cation exchange resin slurry with a high specific gravity in the lower part of the tower 1 is recirculated into an anion exchange resin part with a low specific gravity in the upper part of the tower 1 and both ion exchange resins are mixed so as to make a ratio thereof uniform. This mixing method can be suitable applied to the regelation desalting device of a boiling water reactor power plant.
    • 目的:通过一种方法来确定混合床式脱盐装置的容量,其中管道布置在混合塔的侧面以连接和连通所述塔的上部和下部,水和空气被供应到 以高速连接布置在向上的流中的管,以均匀混合阴离子和阳离子交换树脂。 构成:设置在混合塔的一侧,连接有塔的下部和上部的连接配置管2。 在混合离子交换树脂时,将水10和空气11通过喷嘴供入到混合塔1中并在塔1中剧烈搅拌。同时,将水10和空气11供应到连接布置的管2中 向上定向的流以比内部的塔的速度高的速度,塔1的下部的离子交换树脂再循环到塔1的上部。通过这种方法,具有高特异性的阳离子交换树脂浆料 塔1的下部的重力在塔1的上部被再循环到低比重的阴离子交换树脂部分中,并且两个离子交换树脂混合以使其比例均匀。 该混合方法适用于沸水反应堆发电厂的再生脱盐装置。