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    Moving bed apparatus for the treatment of fluid
    71.
    发明授权
    Moving bed apparatus for the treatment of fluid 失效
    用于处理流体的移动床装置

    公开(公告)号：US3667604A

    公开(公告)日：1972-06-06

    申请号：US3667604D

    申请日：1970-06-04

    Applicant: FILTRES VERNAY

    Inventor： LAGOUTTE PIERRE

    IPC: B01D24/30 ,  B01D33/00 ,  B01J47/10 ,  B01D33/16

    CPC classification number: B01D24/30 ,  B01D24/4689 ,  B01J47/10

    Abstract: A fluid is filtered by passing a stream of fluid through a porous wall of an inlet chamber through a treatment zone filled with treatment material and then through another porous wall into a collecting chamber. The flow from the inlet chamber to the collecting chamber is substantially horizontal and a vertically upwardly directed liquid stream passes through the treatment material at the bottom of the container to entrain particles of the treatment material and lift them to the top of the container to provide for recirculation of the treatment material. The treatment material is regenerated during the circulation with the impurities being removed from the container near the top portion thereof above the treatment material.

    Abstract translation: 通过使流体流通过入口室的多孔壁通过填充有处理材料的处理区域然后通过另一多孔壁进入收集室来过滤流体。 从入口室到收集室的流动基本上是水平的，并且垂直向上指向的液体流在容器的底部通过处理材料，以夹带处理材料的颗粒并将其提升到容器的顶部，以提供 处理材料的再循环。 处理材料在循环期间再生，杂质从处理材料上方的顶部附近从容器中取出。

    Continuous method for treating liquids
    72.
    发明授权
    Continuous method for treating liquids 失效
    连续处理液体的方法

    公开(公告)号：US3642616A

    公开(公告)日：1972-02-15

    申请号：US3642616D

    申请日：1968-08-16

    Applicant: WATER TREATMENT CORP

    Inventor： BURNS WILLIAM C

    IPC: B01D15/04 ,  B01J47/10 ,  B01D15/06 ,  C02B1/76

    CPC classification number: B01J47/11

    Abstract: A continuous method for producing treated water by utilizing at least three zones containing ion-exchange material in which one zone is utilized as a treating or deionization unit, another zone is utilized for regenerating exhausted ion-exchange material and a third zone is utilized for rinsing the regeneration solution from the ion-exchange material, all three zones being operated simultaneously, and when the ion-exchange material in the deionization zone is exhausted the influent water is then transferred to the rinsing zone and the ion-exchange material in the original deionization zone is then regenerated with a regeneration solution while the ion-exchange material in the original regeneration zone is rinsed. Preferably the rinsing operation is conducted by passing a portion of the deionized water through the regenerated ion-exchange material to rinse the salt solution therefrom. It is also preferred to deionize the water by passing the influent water upwardly through the ionexchange material and to regenerate the ion-exchange material by passing regeneration solution downwardly through said material. Moreover, very good results are obtained if each zone has a freeboard sufficient to allow for expansion of the ion-exchange material and the water to be treated is passed through the ionexchange material at a flow rate sufficient to force and hold the ion-exchange material against the top of the zone and in the freeboard space, thereby preventing said ion-exchange material from being mixed.

    Abstract translation: 通过利用含有离子交换材料的至少三个区域来生产处理水的连续方法，其中一个区域用作处理或去离子单元，另一个区域用于再生耗尽的离子交换材料，并且第三区域用于冲洗 来自离子交换材料的再生溶液，所有三个区域同时操作，并且当去离子区域中的离子交换材料被排出时，流入的水然后被转移到漂洗区域中，并且原始去离子物质中的离子交换材料 然后用再生溶液再生区，同时漂洗原始再生区中的离子交换材料。 优选地，通过使去离子水的一部分通过再生的离子交换材料从其中冲洗盐溶液来进行漂洗操作。 还优选通过使流入水向上通过离子交换材料并使再生溶液向下通过所述材料来再生离子交换材料来去离子水。 此外，如果每个区域具有足够允许离子交换材料膨胀的干舷，并且待处理的水通过离子交换材料以足以迫使和保持离子交换材料的流速，则获得非常好的结果， 交换材料抵抗区域的顶部和干舷空间，从而防止所述离子交换材料混合。

    Continuous countercurrent ion exchange method and apparatus
    73.
    发明授权
    Continuous countercurrent ion exchange method and apparatus 失效
    连续逆流离子交换方法和装置

    公开(公告)号：US3595784A

    公开(公告)日：1971-07-27

    申请号：US3595784D

    申请日：1968-10-14

    Applicant: ECODYNE CORP

    Inventor： BUTTERWORTH DONALD J

    IPC: B01D15/04 ,  B01J47/10 ,  B01D15/02

    CPC classification number: B01J47/10

    Abstract: IN A CONVENTIONAL CONTINUOUS COUNTERCURRENT ION EXCHANGE RESIN SYSTEMS, WHEREIN THE REGENERATION TANK HAS AN UPPER RESIN INLET, AN UPPER LIQUID OUTLET, A REGENERANT INLET BELOW THE LIQUID OUTLET, SEPARATION LIQUID INLET MEANS BELOW THE REGENERANT INLET, AND A LOWER RESIN OUTLET BELOW THE SEPARATION LIQUID INLET, A METHOD FOR TRANSFERRING RESIN IS PROVIDED WHICH INSURES A CONTINUOUS UPFLOW DURING THE INTRODUCTION OF REGENERANT. THE TANK IS FILLED WITH RESIN, REGENERANT IS INTRODUCED AT THE REGENERANT INLET, AND A SEPARATION LIQUID AND SUPPLEMENTAL SEPARATION LIQUID ARE INTRODUCED AT THE SEPARATION LIQUID INLET MEANS TO PRESSURIZE THE TANK AND COMPACT THE RESIN OUT THROUGH THE RESIN OUTLET. THE INTRODUCTION OF SUPPLEMENTAL SEPARATION LIQUID AND THE REMOVAL OF RESIN FROM THE TANK AND TERMINATED AT ABOUT THE SAME TIME. THE INVENTION ALSO PROVIDES APPARATUS FOR CARRYING OUT THE METHOD, AND COMPRISING SUPPLEMENTAL SEPARATION LIQUID INLET MEANS COMMUNICATING WITH THE REGENERATION TANK BELOW THE REGENERANT INLET, AND HAVING VALVE MEANS THEREON.

    Installation for the treatment of water and aqueous solutions
    75.
    发明授权
    Installation for the treatment of water and aqueous solutions 失效
    安装水和水溶液的处理

    公开(公告)号：US3581894A

    公开(公告)日：1971-06-01

    申请号：US73709868

    申请日：1968-06-14

    Applicant: GRENOBLOISE ETUDE APPL

    Inventor： MINART PAUL

    IPC: B01D15/04 ,  B01J8/12 ,  B01J8/18 ,  B01J8/20 ,  B01J47/10

    CPC classification number: B01J8/1881 ,  B01J8/12 ,  B01J8/20 ,  B01J47/10

    Abstract: A single column contains a moving ion-exchange bed in which the treatments of regeneration, washing and exhaustion are effected simultaneously in three different vertical sections of the column. The successive batches of exchange resins are fed into the bottom of the column so as to bring about the intermittent progression of the bed, and each successive batch of resins is recovered at the top of the column. The rates of flow of the purified liquid, the regenerant flow and the discharged effluent are controlled so that the raw liquid inflow rate automatically adjusts itself to assure that an adequate flow distribution will be maintained in the different sections of the column.

    Ion exchange apparatus for treating liquids
    76.
    发明授权
    Ion exchange apparatus for treating liquids 失效
    离子交换装置用于处理液体

    公开(公告)号：US3554376A

    公开(公告)日：1971-01-12

    申请号：US3554376D

    申请日：1968-02-16

    Applicant: GHH M A N TECHNIK GES FUR ANLA

    Inventor： KUNZ GERHARD

    IPC: C02F1/42 ,  B01D15/04 ,  B01J47/10 ,  B01J1/06 ,  C02B1/72

    CPC classification number: B01J47/10

    Abstract: In an ion exchange apparatus such as for the softening or desalting of water, the active column and the combined regenerating and washing columns are interconnected by pipe systems including counterpressure chambers so that spent ion exchange material is recycled from the active column through the regenerating and washing columns and back to the active column with a balanced rate of flow.

    Countercurrent solid-liquid contacting system
    78.
    发明授权
    Countercurrent solid-liquid contacting system 失效

    公开(公告)号：US3512641A

    公开(公告)日：1970-05-19

    申请号：US3512641D

    申请日：1967-10-18

    Applicant: AMERICAN STANDARD INC

    Inventor： KUGELMAN IRWIN J

    IPC: B01D11/02 ,  B01D15/02 ,  B01D24/16 ,  B01D24/30 ,  B01J47/10 ,  B01D33/20

    CPC classification number: B01J47/10 ,  B01D11/0223 ,  B01D15/02 ,  B01D24/16 ,  B01D24/30 ,  B01D24/386 ,  B01D24/40 ,  B01D24/42 ,  B01D24/44 ,  B01D2215/021

    Abstract: 1,219,485. Sewage treatment; solid/liquid contact apparatus; ion-exchange. AMERICAN STANDARD Inc. 16 Oct., 1968 [18 Oct., 1967], No. 49155/68. Headings B1D, B1F and B1J. In solid-liquid contacting apparatus, sewage is purified by filtration and/or absorption as it passes upwards through zone 40 of a bed 10 of powdered coal or sand, from inlet pipe 15 to outlet pipe 16, and a fraction of purified sewage is recycled by pump 32 to flow downwards through upper zone 38, to pipe 16, thereby exerting sufficient downward force on the bed to keep zone 40 compacted against the pressure gradient between pipes 15 and 16. A net flow of purified sewage leaves outlet tank 20 over weir 22. The downwardly flowing sewage in zone 38 may be further purified therein. The granular filter medium is progressively replaced, spent medium being withdrawn through rotary valve 44 and fresh medium added to the recycled sewage where it flows through venturi 31. Or the fresh medium may be delivered directly to cylindrical filter housing 12 (Fig. 2, not shown). Inlet and outlet pipes 15, 16 may be replaced by apertures in the housing wall.

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