System and methods for regeneration of mixed bed demineralizers
    51.
    发明申请
    System and methods for regeneration of mixed bed demineralizers 审中-公开
    混床脱盐机再生系统及方法

    公开(公告)号:US20020104802A1

    公开(公告)日:2002-08-08

    申请号:US09962810

    申请日:2001-09-25

    CPC classification number: B01J49/09

    Abstract: Systems and methods for regenerating mixed bed demineralizers are disclosed in this invention. Ion exchange resins are separated in a separation vessel and are separately regenerated in a regeneration vessel. No inert resins are required for separation. Fluid purification and resin regeneration may occur simultaneously, without the use of additional storage tanks or vessels.

    Abstract translation: 在本发明中公开了用于再生混合床软化器的系统和方法。 离子交换树脂在分离容器中分离,并在再生容器中单独再生。 不需要惰性树脂进行分离。 流体净化和树脂再生可能同时发生,而不需要使用额外的储罐或容器。

    Water-demineralizing apparatus with a central regenerant collecting and distributing device

    公开(公告)号:US3595394A

    公开(公告)日:1971-07-27

    申请号:US3595394D

    申请日:1969-02-28

    CPC classification number: B01J49/09

    Abstract: In the regeneration of a mixed bed of cation and anion resins which are separated into layers, these being individually regenerated, the effluent regenerant of the anion layer is collected at points above the interface between the layers and the regenerant of the cation layer is introduced at points below the interface. A central device for collecting and distributing regenerant has inlets on the upper side and outlets on the under side, and all the inlets and outlets are controlled by nonreturn valves.

    Method for separating and isolating ion exchange resins
    53.
    发明授权
    Method for separating and isolating ion exchange resins 失效
    分离和分离离子交换树脂的方法

    公开(公告)号:US3582504A

    公开(公告)日:1971-06-01

    申请号:US3582504D

    申请日:1970-04-20

    Applicant: ECODYNE CORP

    CPC classification number: B01J49/09

    Abstract: IN THE REGENERATION OF MIXED-BED ION EXCHANGE RESINS, THE RESINS ARE FIRST SEPARATED IN THE CONVENTIONAL MANNER BY AN UPFLOW OF LIQUID. THE RESINS ARE THEN ISOLATED FROM ONE ANOTHER, AND CONTAMINANT CATION EXCHANGE RESIN IS SEPARATED FROM THE ANION EXHANGE RESIN BY FLOATING THE ANION EXCHANGE RESIN IN AN INTERMEDIATE-DENSITY LIQUID HAVING A DENSITY INTERMEDIATE BETWEEN THE CATION AND ANION EXCHANGE RESINS. THE CONTAMINANT CATION EXCHANGE RESIN SINKS TO THE BOTTOM OF THE VESSEL, PERMITTING THE ANION EXCHANGE RESIN TO BE READILY ISOLATED.

    Abstract translation: 1310067离子交换ECODYNE CORP 1971年4月19日[1970年4月20日] 26263/71标题B1J通过将树脂分离成一层阳离子交换树脂和一层阴离子交换树脂与一些阴离子交换树脂再生,排出的阴离子和阳离子交换树脂的混合床 作为污染物存在的阳离子交换树脂,将阴离子交换树脂和污染物树脂转移到污染物分离区,其中使用两种树脂之间密度的氢氧化钠水溶液再生阴离子交换树脂并引起 漂浮和污染树脂下沉。 阳离子交换树脂被再生并转移到具有分离和再生的阴离子交换树脂的保持区,在那里它们在进入服务区之前混合。

Patent Agency Ranking