Regeneration method for dual beds of ion exchange resins
    1.
    发明授权
    Regeneration method for dual beds of ion exchange resins 失效
    离子交换树脂双重再生方法

    公开(公告)号:US3711401A

    公开(公告)日:1973-01-16

    申请号:US3711401D

    申请日:1971-03-08

    Applicant: SYBRON CORP

    CPC classification number: B01J49/05 B01J39/05 B01J41/05 B01J39/07

    Abstract: Ion exchange columns containing a layer of weak resin and a layer of strong resin are regenerated by passing partially spent regenerant through the column to regenerate the weak resin and then passing fresh regenerant through the column to regenerate the strong resin. Efficient regeneration is achieved in a downflow regeneration process and silica and calcium sulphate precipitation problems are reduced. In some cases, it is desirable to soak the strong resin in regenerant after the weak regenerant as been passed through the column in order to improve separation of the resins, shorten the total regeneration time and remove additional silica ions. The processes are preferably practiced on systems of three or more columns in which the columns are sequentially exhausted and regenerated, with at least two columns being regenerated in series.

    Abstract translation: 含有弱树脂层和强树脂的离子交换柱通过部分废旧再生剂通过柱再生,再生弱树脂,然后通过新鲜再生剂通过柱再生强树脂。 在下流再生过程中实现有效再生,二氧化硅和硫酸钙沉淀问题减少。 在一些情况下,为了改善树脂的分离,缩短总再生时间,除去附加的二氧化硅离子,希望在弱再生剂通过柱后,将强树脂浸渍在再生剂中。 这些方法优选在三个或更多个柱的系统上实施,其中柱依次耗尽和再生,其中至少两个柱被串联再生。

    Method and apparatus for separating suspended material from a fluid stream
    2.
    发明授权
    Method and apparatus for separating suspended material from a fluid stream 失效
    从流体流中分离悬浮材料的方法和装置

    公开(公告)号:US3768648A

    公开(公告)日:1973-10-30

    申请号:US3768648D

    申请日:1972-07-21

    Applicant: SYBRON CORP

    Inventor: ANDERSON J BEACH W

    Abstract: An improved settler assembly comprising a plurality of inclined passages of chevron cross-sectional configuration. The chevron configuration provides a higher critical flow rate than for passages of equal area and length but of conventional crosssectional configuration such as square, circular, hexagonal and the like. A method of separating suspended material from a liquid is disclosed.

    Abstract translation: 一种改进的沉降器组件,包括多个人字形横截面构造的倾斜通道。 人字纹配置提供比相同面积和长度的通道更高的临界流速,但是具有常规横截面构造,例如正方形,圆形,六边形等。 公开了一种从液体中分离悬浮物质的方法。

    Method for precipitation of heavy metal sulfides
    3.
    发明授权
    Method for precipitation of heavy metal sulfides 失效
    降低重金属硫化物的方法

    公开(公告)号:US3740331A

    公开(公告)日:1973-06-19

    申请号:US3740331D

    申请日:1971-06-23

    Applicant: SYBRON CORP

    Inventor: ANDERSON J WEISS C

    CPC classification number: C01G1/12 C02F1/5236 Y10S210/912

    Abstract: HEAVY METAL POLLUTANT IONS ARE REMOVED FROM AN AQUEOUS SOLUTION IN ASULFIDE PRECIPITATION PROCESS THAT AVOIDS GENERATION OF NOXIOUS AMOUNTS OF HYDROGEN SULFIDE AND THE FORATION OF SOLUBLE COMPLEXES OF SULFIDE IONS. SULFIDE ION AND A HEAVY METAL ION THAT FORMS A SULFIDE HAVING A HIGHER EQUILIBRIUM SULFIDE ION CONCENTRATION THAN THE SULFIELD OF THE HEAVY METAL POLLUTANT ARE ADDED TO THE SOLUTION. THE ADDED HEAVY METAL ACTS AS A SCAVENGER FOR EXCESS SULFIDE. IN SOME CASES THE ADDED HEAVY METAL AND THE HEAVY METAL POLLUTANT FORM CO-PRECIPITATES WHICH RESULT IN MORE COMPLETE REMOVAL OF THE POLLUTANT ION THAN COULD BE ACHIEVED BY SULFIDE PRECIPITATION OF THE POLLUTANT ALONE.

    4.
    发明专利
    未知

    公开(公告)号:BR7201177D0

    公开(公告)日:1973-12-18

    申请号:BR117772

    申请日:1972-02-29

    Applicant: SYBRON CORP

    Abstract: Ion exchange columns containing a layer of weak resin and a layer of strong resin are regenerated by passing partially spent regenerant through the column to regenerate the weak resin and then passing fresh regenerant through the column to regenerate the strong resin. Efficient regeneration is achieved in a downflow regeneration process and silica and calcium sulphate precipitation problems are reduced. In some cases, it is desirable to soak the strong resin in regenerant after the weak regenerant as been passed through the column in order to improve separation of the resins, shorten the total regeneration time and remove additional silica ions. The processes are preferably practiced on systems of three or more columns in which the columns are sequentially exhausted and regenerated, with at least two columns being regenerated in series.

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