Water treating method and apparatus treating waste water by using ion exchange resin
    3.
    发明公开
    Water treating method and apparatus treating waste water by using ion exchange resin 失效
    用离子交换树脂处理废水的水处理方法和设备

    公开(公告)号:EP0758627A3

    公开(公告)日:1997-04-16

    申请号:EP96305994.4

    申请日:1996-08-16

    IPC分类号: C02F1/42 B01J49/00

    摘要: A water treating apparatus is provided which can treat waste water for use as raw water in an ultrapure water producing system without addition of various kinds of chemicals. The apparatus includes a first water tank 41 for receiving acid waste water, a second water tank 42 for subjecting the waste water from the first water tank 41 to solid-liquid separation and discharging supernatant liquid, an ion exchange tank 49 including ion exchange resin 93 and an aeration tube 88 for generating treated water through a membrane filter 91, a precipitation tank 50 for settling ion exchange resin 93, an air lift pump 95 for introducing ion exchange resin 93 from the precipitation tank 50 into the first water tank 41, and a return air lift pump 61 for returning ion exchange resin 93 from the second water tank 42 to the ion exchange tank 49. The ion exchange resin 49 acts to exchange ions with fluorine ions of treated water in the ion exchange tank 49 and is regenerated by acid waste water in the first water tank 41.

    摘要翻译: 提供了一种水处理装置,其能够在不添加各种化学品的情况下将废水处理成超纯水制造系统中的原水。 该设备包括用于接收酸性废水的第一水箱41,用于对来自第一水箱41的废水进行固液分离并排出上清液的第二水箱42,包括离子交换树脂93的离子交换箱49 以及通过膜过滤器91产生处理水的曝气管88,沉淀离子交换树脂93的沉淀槽50,用于将离子交换树脂93从沉淀槽50引入第一水槽41的空气提升泵95,以及 返回空气提升泵61,用于将离子交换树脂93从第二水箱42返回到离子交换箱49.离子交换树脂49用于与离子交换箱49中的处理过的水的氟离子交换离子,并且通过 第一水箱41中的酸性废水。

    Water treating method and apparatus treating waste water by using ion exchange resin
    4.
    发明公开
    Water treating method and apparatus treating waste water by using ion exchange resin 失效
    水处理方法和使用离子交换树脂对废水处理装置

    公开(公告)号:EP0758627A2

    公开(公告)日:1997-02-19

    申请号:EP96305994.4

    申请日:1996-08-16

    IPC分类号: C02F1/42 B01J49/00

    摘要: A water treating apparatus is provided which can treat waste water for use as raw water in an ultrapure water producing system without addition of various kinds of chemicals. The apparatus includes a first water tank 41 for receiving acid waste water, a second water tank 42 for subjecting the waste water from the first water tank 41 to solid-liquid separation and discharging supernatant liquid, an ion exchange tank 49 including ion exchange resin 93 and an aeration tube 88 for generating treated water through a membrane filter 91, a precipitation tank 50 for settling ion exchange resin 93, an air lift pump 95 for introducing ion exchange resin 93 from the precipitation tank 50 into the first water tank 41, and a return air lift pump 61 for returning ion exchange resin 93 from the second water tank 42 to the ion exchange tank 49. The ion exchange resin 49 acts to exchange ions with fluorine ions of treated water in the ion exchange tank 49 and is regenerated by acid waste water in the first water tank 41.

    ION EXCHANGE PROCESS
    6.
    发明公开
    ION EXCHANGE PROCESS 审中-公开
    IONENAUSTAUSCHVERFAHREN

    公开(公告)号:EP3131674A1

    公开(公告)日:2017-02-22

    申请号:EP15727721.1

    申请日:2015-04-15

    摘要: This invention relates to a process for carrying out an ion exchange process which involves providing two interacting sets of banks of continuously stirred tank reactors (CSTR's) each containing a bed of ion exchange resin and causing the resin to move in one direction through each bank of reactors and the feed solution and/or or eluant in the opposite direction, in carrying out the process, a feed solution is introduced in a first reactor causing dissolved ions to be captured on the resin, eluant is introduced into a reactor upstream of the first reactor in the direction of resin movement causing ions captured on the resin to be removed into the eluant and eluant rich in ions removed from the resin will be taken from a reactor upstream of the reactor in which the eluant was introduced, for further processing. Thus, in this form of the invention there is, in effect, a loading bank of reactors in which ions from the feed solution are captured followed by a regenerating bank of reactors in which the eluant removes the ions captured on the resin and regenerates the resin.

    摘要翻译: 本文公开了一种用于进行离子交换过程的方法,其包括提供两个相互连接的连续搅拌釜式反应器组(CSTR's)的组,每组包含离子交换树脂床,并使树脂沿一个方向移动通过每一组反应器 和进料溶液和/或洗脱液在相反方向。 在进行该过程中,将进料溶液引入第一反应器中,使溶解的离子捕获在树脂上,将洗脱液沿着树脂运动的方向引入第一反应器上游的反应器,导致在树脂上捕获的离子为 从洗脱剂中除去富含离子的离子的洗脱液将从其中引入洗脱剂的反应器的上游的反应器中取出,用于进一步处理。 因此,在本发明的这种形式中,实际上是反应器的装载组,其中捕获来自进料溶液的离子,随后再生一批反应器,其中洗脱剂除去捕获在树脂上的离子并再生树脂 。

    IMPROVEMENTS IN OR RELATING TO THE REGENERATION OF WATER TREATMENT SUBSTRATES
    7.
    发明公开
    IMPROVEMENTS IN OR RELATING TO THE REGENERATION OF WATER TREATMENT SUBSTRATES 有权
    VERBESSERUNGEN BEI ODERBEZÜGLICHDER REGENERATION VON WASSERBEHANDLUNGSSUBSTRATEN

    公开(公告)号:EP1861336A2

    公开(公告)日:2007-12-05

    申请号:EP06710122.0

    申请日:2006-03-17

    申请人: The BOC Group plc

    IPC分类号: C02F1/42 B01J49/00

    摘要: In a method and apparatus for operating and regenerating ion exchange material a wash fluid or elution solution for rinsing the ion exchange material (1) is prepared, there is collected as a by-product of said preparation a first waste stream including cationic species to be eliminated, the ion exchange material (1) is subjected to a wash step in which there is eluted from the ion exchange material by the wash fluid or solution an anionic species to be eliminated and a second waste stream including the anionic species to be eliminated is obtained, the first waste stream (12) and the second waste stream (14) are combined to form a precipitate SW comprising a reaction product of said cationic species and said anionic species, and the precipitate is removed. The method provides an efficient means of eliminating undesired species from a circuit containing an ion exchange material to be regenerated.

    摘要翻译: 在用于操作和再生离子交换材料的方法和装置中,制备用于漂洗离子交换材料(1)的洗涤液或洗脱溶液,作为所述制备物的副产物收集包含阳离子物质的第一废物流 离子交换材料(1)进行洗涤步骤,其中通过洗涤流体或溶液从离子交换材料洗脱待除去的阴离子物质,并且包括待消除的阴离子物质的第二废物流是 将第一废物流(12)和第二废物流(14)组合以形成包含所述阳离子物质和所述阴离子物质的反应产物的沉淀物SW,并除去沉淀物。 该方法提供了从包含要再生的离子交换材料的回路消除不需要的物质的有效手段。