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    High capacity portable exchange single bed deionizer
    22.
    发明申请
    High capacity portable exchange single bed deionizer 失效
    高容量便携式交换单床去离子

    公开(公告)号：US20040099594A1

    公开(公告)日：2004-05-27

    申请号：US10713635

    申请日：2003-11-14

    Inventor： Michael M. Barlow

    IPC: B01D024/16

    CPC classification number: C02F1/42 ,  B01J47/012 ,  B01J47/022 ,  B01J47/04

    Abstract: A device for the deionization of incoming water is disclosed. The device includes a tank and a generally hollow distributor tube in the tank for ingress into and downward movement of unpurified water through the tank. An opening adjacent the bottom of the generally hollow distributor tube and near the bottom of the tank distributes the unpurified water out of the generally hollow distributor tube. A mixed bed of purifying resin is within the tank, and surrounds the generally hollow distributor tube. The unpurified water travels upwardly through the tank where it is deionized to a high purity water by the mixed bed of purifying resin, after egress from the opening. The deionized water passes through a distributor and a filter before leaving the tank through an outlet.

    Abstract translation: 公开了一种用于进水去离子的装置。 该装置包括罐中的一个中空的分配管，用于使未经净化的水通过罐进入和向下运动。 在大致中空的分配器管的底部附近的开口和容器的底部附近的开口将未净化的水分配出大致中空的分配器管。 净化树脂的混合床位于罐内，并且围绕着大致中空的分配器管。 未经净化的水在从开口排出之后，通过净化树脂的混合床向上通过槽去除高纯度水。 去离子水通过分配器和过滤器，然后离开水箱通过出口。

    Method for separating ion exchange resins and for removing metallic foulants from the resins
    23.
    发明授权
    Method for separating ion exchange resins and for removing metallic foulants from the resins 失效
    用于分离离子交换树脂和从树脂中除去金属污垢的方法

    公开(公告)号：US5428074A

    公开(公告)日：1995-06-27

    申请号：US704709

    申请日：1991-05-17

    Applicant: Frances M. Cutler

    Inventor： Frances M. Cutler

    IPC: B01J47/04 ,  B01J49/00 ,  B01D15/04

    CPC classification number: B01J47/04 ,  B01J49/0021

    Abstract: In a method for separating and regenerating a mixed bed of exhausted anion and cation resins and for removing metallic foulants from the mixed bed, substantially all of the cation and anion resins in the bed are separated by their respective buoyancies and metallic foulants are displaced from the resins using an amine salt solution having a density between the densities of the anion and cation resins. A composition formed during this method comprises the anion resin, the metallic foulants, the cation resin, and the amine salt solution.

    Abstract translation: 在用于分离和再生排出的阴离子和阳离子树脂的混合床并从混合床中除去金属污垢的方法中，床中的基本上所有的阳离子和阴离子树脂通过它们各自的浮力分离，金属污染物从 使用具有密度在阴离子和阳离子树脂的密度之间的胺盐溶液的树脂。 在该方法中形成的组合物包含阴离子树脂，金属污垢，阳离子树脂和胺盐溶液。

    Method for preparing ultrapure water
    24.
    发明授权
    Method for preparing ultrapure water 失效
    制备超纯水的方法

    公开(公告)号：US5292439A

    公开(公告)日：1994-03-08

    申请号：US796389

    申请日：1991-11-22

    Applicant: Takamitsu Morita ,  Junya Watanabe ,  Toyokazu Sugawara

    Inventor： Takamitsu Morita ,  Junya Watanabe ,  Toyokazu Sugawara

    IPC: B01J41/14 ,  B01J47/04 ,  C02F1/42

    CPC classification number: B01J47/04 ,  B01J41/14 ,  C02F1/42 ,  Y10S210/90

    Abstract: A method for preparing an ultrapure water, from which impurities including inorganic salts, organic substances, fine particles and microorganisms are removed, by treatment including an ion exchange treatment, which comprises using an ion exchange resin comprising a copolymer of a polyvinyl compound and a monovinyl aromatic compound which may contain a monovinyl aliphatic compound, as the matrix, at least in a mixed bed ion exchange treatment of the ion exchange treatment, said ion exchange resin used comprising at least a regenerated form ion exchange resin A eluting an organic compound of a molecular weight of less than 3,000 but substantially not eluting an organic compound of a molecular weight of not less than 3,000 when dipped in a hot water at 50.degree. C. for 7 days.

    Abstract translation: 一种通过包括离子交换处理在内的包括使用包含聚乙烯基化合物和单乙烯基共聚物的离子交换树脂的离子交换树脂制备超纯水的方法，其中除去包括无机盐，有机物质，细颗粒和微生物在内的杂质， 至少在离子交换处理的混合离子交换处理中，可以含有单乙烯基脂族化合物的芳香族化合物作为基质，所述离子交换树脂至少包含再生形式的离子交换树脂A， 分子量小于3000但当浸入50℃的热水中7分钟时，基本上不洗脱分子量不小于3,000的有机化合物。

    Removal of contaminants and recovery of metals from waste solutions
    25.
    发明授权
    Removal of contaminants and recovery of metals from waste solutions 失效
    从废液中去除污染物和回收金属

    公开(公告)号：US5066371A

    公开(公告)日：1991-11-19

    申请号：US316201

    申请日：1989-02-24

    Applicant: Irving W. DeVoe ,  Olwyn A. D'Sylva ,  David A. Fine

    Inventor： Irving W. DeVoe ,  Olwyn A. D'Sylva ,  David A. Fine

    IPC: B01J47/00 ,  B01J47/04 ,  B01J47/10 ,  B01J49/00 ,  C02F1/42 ,  C02F9/00 ,  C02F11/00

    CPC classification number: C02F9/00 ,  B01J47/001 ,  B01J47/04 ,  B01J47/10 ,  B01J49/0026 ,  C02F1/42 ,  C02F11/004 ,  C22B3/42 ,  C02F2101/20 ,  Y02P10/234

    Abstract: A method for removal of at least one contaminant from a liquid is described, wherein a first step in liquid is introduced into a first of a plurality of liquid treatment containers and brought into contact in a liquid-medium suspension with a first quantity of a solid contaminant recovery medium for removing the contaminant for a period of time sufficient to achieve a desired efficiency of recovery of the contaminant. The liquid is then cycled from the first liquid treatment container sequentially through each of the plurality of liquid treatment containers to a final liquid treatment container while contacting the liquid in each of the liquid treatment containers with additional quantities of the medium in liquid-medium suspension for periods of time sufficient to achieve the desired efficiency of recovery in each of the liquid treatment containers. At least a portion of the medium is cycled from the final liquid treatment container through the plurality of liquid treatment containers to the first liquid treatment container in a direction countercurrent to flow of the liquid so as to maintain essentially a constant medium concentration in each of the liquid treatment containers, with the medium being substantially separated from liquid prior to cycling from one container to another container. At least a portion of the medium is transferred from the first liquid treatment container into a medium recycling means, in which the medium is treated with a contaminant recovery liquid for regenerating the medium.

    Abstract translation: 描述了从液体中去除至少一种污染物的方法，其中将液体中的第一步骤引入到多个液体处理容器中的第一个中，并在液体介质悬浮液中与第一量的固体 污染物回收介质，用于去除污染物一段足以实现期望的污染物回收效率的时间段。 然后将液体从第一液体处理容器顺序地通过每个液体处理容器循环到最终的液体处理容器，同时使每个液体处理容器中的液体与液体介质悬浮液中的附加量的介质接触 足以在每个液体处理容器中达到期望的回收效率的时间段。 介质的至少一部分从最终的液体处理容器通过多个液体处理容器循环到与液体流动逆流的方向到第一液体处理容器，以便在每个液体处理容器中保持基本上恒定的介质浓度 液体处理容器，在从一个容器循环到另一容器之前，介质基本上与液体分离。 介质的至少一部分从第一液体处理容器转移到介质循环装置中，其中介质用用于再生介质的污染物回收液处理。

    Method of separating and transferring ion-exchange resin
    27.
    发明授权
    Method of separating and transferring ion-exchange resin 失效
    分离和转移离子交换树脂的方法

    公开(公告)号：US4891138A

    公开(公告)日：1990-01-02

    申请号：US137714

    申请日：1987-12-24

    Applicant: Kanroku Chonan ,  Kazuyuki Koyama ,  Masahiro Hagiwara

    Inventor： Kanroku Chonan ,  Kazuyuki Koyama ,  Masahiro Hagiwara

    IPC: A61K47/04 ,  B01J47/04 ,  B01J49/00 ,  C02F1/42

    CPC classification number: B01J49/0021 ,  B01J47/04

    Abstract: A method for separating and transferring an ion-exchange resin having the lower specific gravity from an ion-exchange resin having the higher specific gravity in an ion-exchange resin separating tank that is indispensable to a pure or ultrapure water producing plant and which is packed with a mixed bed of ion-exchange resins having different specific gravities is disclosed.This method contains the following essential steps: (1) a first step in which the mixed resin bed is separated into two layers by backwashing and the greater part of the ion-exchange resin (SBR) having the lower specific gravity is transferred by means of a perforated sluicing pipe that is disposed below the interface between the separated resin layers and a resin transfer pipe that is disposed above said sluicing pipe; (2) a second step in which SBR that is left untransferred in the first step is separated to be situated above the layer of the ion-exchange resin (SAR) having the higher specific gravity; and (3) a third step in which sluicing water is introduced into the tank at high flow rate through the sluicing pipe so that the particles of SBR are lifted in the water in the freeboard above the resin layer, while pressurized water is introduced from the top of the tank so as to transfer the residual SBR through the resin transfer pipe.According to the process of the present invention, substantially complete separation and transfer of SBR can be accomplished by operations in a fully automatic and unattended way, with the volume of SAR being held constant at all times after the transfer of SBR. If the process is applied to the condensate demineralizing system in a PWR power plant which requires stricter control of water quality that a thermal power plant, the sequence of the second and third steps may be repeated after the third step so as to reduce the total level of residual SBR to 0.05% of the total anion resin and below.

    Abstract translation: 离子交换树脂的分离和转移方法包括以下必要步骤：（1）通过反冲洗将混合树脂床分离成两层的第一步骤，并且大部分离子交换树脂（SBR）具有 较低的比重通过设置在分离的树脂层之间的界面下方的穿孔的流道管和设置在所述的流水管上方的树脂传送管道传送; （2）第二步骤，其中在第一步骤中未转印的SBR被分离以位于具有较高比重的离子交换树脂（SAR）的层之上; 和（3）第三步骤，其中将洗涤水以高流速通过流水管引入罐中，使SBR颗粒在树脂层上方的干舷内的水中提起，同时从 以便通过树脂输送管转移剩余的SBR。

    Three component resin system and method for purifying aqueous solutions
    28.
    发明授权
    Three component resin system and method for purifying aqueous solutions 失效
    三组分树脂体系和净化水溶液的方法

    公开(公告)号：US4564455A

    公开(公告)日：1986-01-14

    申请号：US560806

    申请日：1983-12-13

    Applicant: George C. Flynn ,  Eli Salem ,  Robert Kunin

    Inventor： George C. Flynn ,  Eli Salem ,  Robert Kunin

    IPC: B01D15/04 ,  B01J47/04 ,  B01J49/00 ,  C02F1/42

    CPC classification number: B01J49/0043 ,  B01J47/04

    Abstract: The present invention relates to a method for purifying aqueous solutions or condensate in a three component resin system comprising a mixed bed of a strongly basic anion exchange resin, a strongly acidic cation exchange resin and a weakly acidic cation exchange resin. According to the present method, aqueous solutions can be treated to remove metal ions and corrosion products along with ammonia and other volatile amines so that metal ion leakage is substantially reduced and the run length of the resin system is increased. A method for separating and isolating the resins of the three component system is also described.

    Abstract translation: 本发明涉及一种包含强碱性阴离子交换树脂，强酸性阳离子交换树脂和弱酸性阳离子交换树脂的混合床的三组分树脂体系中的水溶液或冷凝物的净化方法。 根据本方法，可以处理水溶液以与氨和其它挥发性胺一起除去金属离子和腐蚀产物，从而显着降低金属离子泄漏并增加树脂体系的流动长度。 还描述了用于分离和分离三组分体系的树脂的方法。

    Process for internal regeneration of ion exchanger resins in mixed bed filters, and mixed bed filters for carrying out the process
    29.
    发明授权
    Process for internal regeneration of ion exchanger resins in mixed bed filters, and mixed bed filters for carrying out the process 失效
    混合床式过滤器中的离子交换树脂的内部再生方法，以及用于进行该方法的混合床过滤器

    公开(公告)号：US4519916A

    公开(公告)日：1985-05-28

    申请号：US592164

    申请日：1984-03-22

    Applicant: Friedrich Martinola

    Inventor： Friedrich Martinola

    IPC: B01J47/04 ,  B01J49/00 ,  B01J49/09

    CPC classification number: B01J47/04 ,  B01J49/0021

    Abstract: The invention relates to a process for internal regeneration of mixed bed filters in which, after the exhausted ion exchanger mass has been separated into the two components and these have been regenerated and washed out, the exchanger layer in the region of the cation exchanger/anion exchanger interface is selectively removed from the mixed bed filter, the cation exchanger remaining in the filter is mixed with the anion exchanger remaining in the filter for the new loading stage, the ion exchanger mass removed from the filter is added again, when the work cycle has ended, to the exhausted ion exchanger mass before or during the separation into cation exchanger and anion exchanger, and, after the separation, the loading stage is started again with the regeneration of the cation exchanger and anion exchanger; and also to a mixed bed filter for carrying out the process.

    Abstract translation: 本发明涉及一种混合床过滤器的内部再生方法，其中在排出的离子交换剂物质已经分离成两种组分并且已被再生和洗出后，在阳离子交换剂/阴离子区域中的交换剂层 交换器界面从混合床过滤器中选择性地除去，残留在过滤器中的阳离子交换剂与残留在过滤器中的阴离子交换剂混合，用于新的装载阶段，再次加入从过滤器移除的离子交换剂质量，当工作循环 在分离成阳离子交换剂和阴离子交换剂之前或期间已经结束了排出的离子交换剂物质，分离后，再次通过阳离子交换剂和阴离子交换剂的再生开始加载阶段; 以及用于进行该过程的混床过滤器。

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