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    • 1. 发明专利
    • Continuous electrophoretic apparatus
    • 连续电泳装置
    • JPS6110758A
    • 1986-01-18
    • JP13101584
    • 1984-06-27
    • Hitachi Ltd
    • ODA CHIKAONAKATSUI FUJITSUGUYOSHINAGA SHIYOUJIMUROI KATSUMINOMURA SEIJI
    • G01N27/26B01D57/02G01N27/447
    • G01N27/44769
    • PURPOSE:To elevate separation performance removing adverse effect due to the flow of a dispersion liquid, by providing two grooves along the length of an electrophoretic layer to mount an outlet nozzle at each of demarcated chambers which are formed by demarcating the grooves. CONSTITUTION:A lamellar electrophoretic layer 2 is provided horizontally and two grooves 3 are provided at the bottom of the body 1. The grooves 3 are demarcated by a plurality of weir 12 and an outlet nozzle 4 is provided at the bottom of each f the demarcated chambers. Then, a dispersion liquid is fed into the electrophoretic layer 2 from an inlet nozzle 8 and is electrically migrated with electrode chambers 5 on both sides thereof. The dispersion liquid flows through electrophoretic layer 2, moving as shown by the dotted line 13 and drops to the bottom of the grooves 3 and the dispersion liquid entering the demarcated chambers is withdrawn from the outlet nozzle 4. The dispersion liquid kept from entering the grooves 3 is allowed to flow out of an outlet nozzle 11. Thus, as the grooves provided on the electrophoretic layer are demarcated to withdraw the dispersion liquid, effect due to turbulence in the flow thereof can be eliminated to elevate the separation performance.
    • 目的:提高分离效果,消除由于分散液的流动引起的不利影响,通过沿着电泳层的长度设置两个凹槽,以便在通过划定凹槽形成的每个分隔室上安装出口喷嘴。 构成:水平地设置层状电泳层2,在本体1的底部设置有两个槽3.槽3由多个堰12划分,出口喷嘴4设置在每个f的划分的底部 房间。 然后,将分散液从入口喷嘴8供给到电泳层2中,并在其两侧的电极室5中电迁移。 分散液体流过电泳层2,如虚线13所示移动,并下降到槽3的底部,并且进入分界室的分散液体从出口喷嘴4排出。分散液保持不进入槽 允许从出口喷嘴11流出。因此,由于设置在电泳层上的凹槽被划分以抽出分散液,可以消除由于其流动中的紊流引起的影响,从而提高分离性能。
    • 2. 发明专利
    • BACK EXTRACTION METHOD FOR URANIUM
    • JPS5816035A
    • 1983-01-29
    • JP11368381
    • 1981-07-22
    • HITACHI LTD
    • YOSHINAGA SHIYOUJITOUDOU MATSUZOUFUJIWARA KIYOSHI
    • B01D11/04C01G43/00C22B60/02
    • PURPOSE:To improve back extraction rate considerably by using a centrifugal extractor for a back extractor, and an aq. ammonium carbonate for back extracting liq., and regulating the temps. of an org. solvent and the aq. ammonium carbonate soln. to specific temps. or above. CONSTITUTION:In the neighborhood of the outside circumference of a rotating body 2 under high speed revolution around the axial center of a revolving shaft 1, an org. solvent wherein amine type chemicals are dissolved in a diluting agent such as kerosene extracted with uranium is heated to about >=40 deg.C and is introduced on the outside circumferential side of the body 2 through an introduction passage 3, and an aq. ammonium carbonate soln. heated to the same temp. is introduced to the inside circumferential side of the body 2 through a back extracting liq. introducing passage 4. In the body 2, the continuous layer 6a on the org.solvent side is formed on the inside circumferential side of the body 2 with a main interface as a boundary and the continuous layer 6b of the aq. ammonium carbonate layer is formed on the outside circumferential side on account of a difference in specific gravity. The respective dispersed liquid drops 7a, 7b flow to the continuous layers 6a, b facing each other and collide against each other at the main interface 5, by which back extraction is progressed. The aq. ammonium carbonate wherein uranium is extracted is discharged through a discharge port 9.
    • 5. 发明专利
    • CENTRIFUGAL TYPE COUNTERRFLOW CONTACT APPARATUS
    • JPS5511002A
    • 1980-01-25
    • JP8090278
    • 1978-07-05
    • HITACHI LTD
    • FUJIWARA KIYOSHINAGATOMO KATSUAKIYOSHINAGA SHIYOUJITAMURA ZENSUKESHIBATA FUMIOKANEKIYO HIROSHI
    • B01D11/04B01J19/00B04B5/06
    • PURPOSE:To increase the extraction efficiency, by attaching a ring member inside the rotating body, being inclined with respect to the axis, by providing a clearance to a member adjoining in the axial direction. CONSTITUTION:A heavy liquid is introduced into each partitioned chamber in the central part in a rotating body 2 through a heavy liquid lead-in pipe 14, and a light liquid is introduced into each partitioned chamber through a light liquid lead-in pipe 15. The heavy liquid runs in the axial direction in each partitioned chamber along the slope of an inclined cylinder 16, and passes through a clearance 19 provided in the circumferential direction to run in the outer circumferential direction, and is taken out from a heavy liquid lead-out passage 6 through passage 6a from the peripheral part of the rotating body 2. The light liquid, on the other hand, runs in the axial direction along the slope of the inclined cylinder 16 similarly as in the case of heavy liquid, towards the central direction in each partitioned chamber, and is caused to counter-contact with the heavy liquid running in the outer circumferential direction along the clearance 19, and taken out from a light liquid take-out passage 7 through a passage 7a from the central part of the rotating body 2. By repeating the joining and dispersion of heavy liquid and light liquid between V-rings and side walls, the extraction efficiency is increased.
    • 6. 发明专利
    • Centrifugal desalting method
    • 离心脱盐方法
    • JPS54150371A
    • 1979-11-26
    • JP5892378
    • 1978-05-19
    • Hitachi Ltd
    • FUJIWARA KIYOSHISHIBATA FUMIONOMURA KIYOSHIINOUE YUKIOYOSHINAGA SHIYOUJI
    • B01D11/04C10G31/10
    • PURPOSE: To desalt raw oil or heavy oil easily, charging a centrifugal extractor with a mixt. of raw material oil and water having been used for washing the oil as the light liq., and a small amount of fresh water as the heavy liq. in order to make both the liqs. contact with each other countercurrently.
      CONSTITUTION: Raw material oil 1 is mixed with salt-contg. recycle water 20 having been used for washing, and the mixt. is heated in a preheater 19 to 40W 80°C, and is introduced through a mixing value 18 to a liq./liq. countercurrent centrifugal extractor 17 by way of a light liq. inlet side (the outer periphery side of the rotor). Simultaneously, fresh water 9 in an amount 1W5% based on the raw material oil is charged through a heavy liq. inlet side (the inner periphery of the rotor). The oil admitted from the light liq. side is separated from water at the outer periphery of the rotor and flows into the inner periphery side, and is washed with fresh water 9 admitted from heavy liq. side, it is then discharged as desalted oil 12'. Hereby, by use of only one centrifugal extractor, the salt content is decreased to 0.5 ppm at relatively low temp., without use of an emulsion breaker.
      COPYRIGHT: (C)1979,JPO&Japio
    • 目的:为了将原油或重油轻松脱盐,用离心萃取器加入混合物。 用作清洗油的原料油和水,以及少量淡水作为重液体。 为了使两者都有利。 相互接触。 构成:原料油1与盐混合。 已经用于洗涤的再循环水20和混合物。 在预热器19中加热至40-80℃,并通过混合值18引入液体/液体。 逆流式离心萃取器17通过光液体进行。 入口侧(转子的外周侧)。 同时,以原料油为基础的1-5%的淡水9通过沉重的液体填充。 入口侧(转子的内周)。 石油从轻盈进口。 侧面与转子外周的水分离,流入内周侧,用沉重的液体进入清水9洗涤。 然后以脱盐油12'的形式排出。 因此,通过仅使用一个离心萃取器,在相对低的温度下,盐含量降低至0.5ppm,而不使用破乳剂。