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    Regeneration of water treatment substrates
    11.
    发明授权
    Regeneration of water treatment substrates 有权
    水处理底物的再生

    公开(公告)号：US07887707B2

    公开(公告)日：2011-02-15

    申请号：US11886642

    申请日：2006-03-17

    Applicant: Peter James Mawle ,  Michael John Waite

    Inventor： Peter James Mawle ,  Michael John Waite

    IPC: B01J49/00

    CPC classification number: C02F1/42 ,  B01J49/08 ,  B01J49/16 ,  B01J49/53 ,  B01J49/57

    Abstract: 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.

    Abstract translation: 在用于操作和再生离子交换材料的方法和装置中，制备用于冲洗离子交换材料（1）的洗涤液或洗脱溶液，作为所述制剂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）经受洗涤步骤，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）合并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。

    Process for regenerating resins of deionization system
    14.
    发明授权
    Process for regenerating resins of deionization system 失效
    用于再生污染系统树脂的方法

    公开(公告)号：US3691109A

    公开(公告)日：1972-09-12

    申请号：US3691109D

    申请日：1970-05-25

    Applicant: MARATHON OIL CO

    Inventor： LARSEN ARTHUR L

    IPC: B01D15/04 ,  B01J49/00 ,  B01D15/06 ,  C02B1/76

    CPC classification number: B01J49/08

    Abstract: A weak acid resin which is exhausted by contact with bases is regenerated by contact with carbonic acid formed by introducing carbon dioxide into water under a pressure of from 100 to 300 psi. The carbonic acid is capable of regenerating the sodium form of the weak acid resin. The sodium bicarbonate from the regeneration of the weak acid resin is then degassed to eliminate the carbonic acid or CO2 and the remaining sodium bicarbonate is used to regenerate a weak base anion resin. The ion exchange beds are then run in reverse, that is, the anions are exchanged before the cations.

    Abstract translation: 通过与碱接触而排出的弱酸性树脂通过与在碳酸中接触，通过在100-300psi的压力下将二氧化碳引入水中而形成。 碳酸能够再生钠形式的弱酸性树脂。 然后将来自弱酸性树脂的再生的碳酸氢钠脱气以除去碳酸或CO 2，并且使用剩余的碳酸氢钠来再生弱碱性阴离子树脂。 然后离子交换床反向运行，即在阳离子之前交换阴离子。

    Metal ion recovery system
    15.
    发明授权
    Metal ion recovery system 失效
    金属离子回收系统

    公开(公告)号：US3658470A

    公开(公告)日：1972-04-25

    申请号：US3658470D

    申请日：1969-06-16

    Applicant: INDUSTRIAL FILTER PUMP MFG CO

    Inventor： ZIEVERS JAMES F ,  RILEY CLAY W ,  CRAIN RICHARD W

    IPC: B01J49/00 ,  C01G37/00 ,  B01K3/00 ,  C01G37/02 ,  C23B5/06

    CPC classification number: C01G37/003 ,  B01J49/08 ,  Y10S204/13

    Abstract: A metal ion recovery system first removes most of the plating solution from recently plated articles in a relatively concentrated form and removes the remainder of the solution in much less concentrated form. These solutions are treated separately with only the lower concentrated solution being completely deionized to remove said metal ions therefrom.

    Abstract translation: 金属离子回收系统首先以相对浓缩的形式除去最近镀敷的制品中的大部分电镀溶液，并以少得多的浓缩形式除去剩余的溶液。 分开处理这些溶液，只有较低浓度的溶液完全去离子以从中除去所述金属离子。

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