Removal of selenium from water by ion-exchange
    61.
    发明授权
    Removal of selenium from water by ion-exchange 失效
    通过离子交换从水中去除硒

    公开(公告)号:US5494582A

    公开(公告)日:1996-02-27

    申请号:US396990

    申请日:1995-03-01

    CPC classification number: C02F1/42 B01J41/043 B01J45/00

    Abstract: Selenium compounds present in aqueous liquids containing sulfate and or chloride anions can be effectively removed by passing the liquid through a thiouronium modified anion ion exchange resin.

    Abstract translation: 存在于含有硫酸盐和/或氯化物阴离子的含水液体中的硒化合物可以通过使液体通过硫脲改性阴离子交换树脂而被有效地除去。

    Ion exchange device for purifying water, process for manufacturing it
and its use for removing nitrates and/or nitrates from water
    62.
    发明授权
    Ion exchange device for purifying water, process for manufacturing it and its use for removing nitrates and/or nitrates from water 失效
    用于净化水的离子交换装置,其制造方法及其从水中去除硝酸盐和/或硝酸盐的用途

    公开(公告)号:US5238576A

    公开(公告)日:1993-08-24

    申请号:US663904

    申请日:1991-10-03

    Applicant: Alvaro Affonso

    Inventor: Alvaro Affonso

    Abstract: The present invention relates to an ion exchange device for purifying water by reducing the nitrite and/or nitrate content, consisting of at least one container with a basic anion exchanger in chloride and/or sulphate form arranged therein and at least one additional basic anion exchanger layer in hydroxyl form or a hydroxyl-group-containing layer, in which the anion exchanger layers are arranged one behind the other directly and/or with the interposition of an intermediate layer and the anion exchange layer(s) in chloride and/or sulphate form is/are arranged not as a mixture but in (a) separate layer(s). The chloride and/or sulphate containing layer is arranged near or beneath the inlet aperture, preferably beneath the filter layer and/or (in the direction of flow of the water) in front of the anion exchange layer in the form of hydroxyl or containing hydroxyl groups. This invention also relates to processes for manufacturing and for using the ion exchange device to remove nitrates and/or nitrates from water.

    Abstract translation: 本发明涉及一种用于通过降低亚硝酸盐和/或硝酸盐含量来净化水的离子交换装置,所述装置由至少一个具有排列在其中的氯化物和/或硫酸盐形式的碱性阴离子交换剂的容器和至少一种另外的碱性阴离子交换剂 羟基形式的层或含羟基的层,其中阴离子交换层被直接布置在另一个之后和/或在中间层和阴离子交换层之间插入氯化物和/或硫酸盐 形式不是作为混合物排列,而是(a)单独的层。 含有氯化物和/或硫酸盐的层被布置在入口孔附近或下方,优选在过滤层下方和/或(在水的流动方向上)位于阴离子交换层前面,呈羟基或含羟基的形式 团体 本发明还涉及用于制造和使用离子交换装置从水中去除硝酸盐和/或硝酸盐的方法。

    Reversible oxygen sorbent compositions
    63.
    发明授权
    Reversible oxygen sorbent compositions 失效
    可逆氧吸附剂组合物

    公开(公告)号:US5208335A

    公开(公告)日:1993-05-04

    申请号:US890065

    申请日:1992-05-27

    Abstract: High Capacity solid state cyanocobaltate complexes represented by the chemical formula:[(A).sub.a (R.sub.4 N).sub.b ].sup.z+.sub.x/z [Co(CN).sub.n ].sup.x- .multidot.pSwhere:A is alkali metal atom, alkaline earth metal atom, Zn, Cd or Hg atom;a is any number from 0 to 2.5each R is independently C.sub.1 -C.sub.1O substituted or unsubstituted alkyl, aryl or aralkyl; or a long chain hydrocarbon polymerb is any number from greater than zero to 3z is 1, 2 or 3;n is any number from 3 to 5;x is n-2;p is any number from greater than zero to 6; andS is a ligand which is capable of coordinating with [(A).sub.a (R.sub.4 N).sub.b 9 .sup.z+, Co or both.are capable of chemically binding oxygen to form novel oxygen adducts, thereby selectively removing oxygen from an oxygen-containing fluid stream. The bound oxygen may be recovered from the complexes by increasing the temperature or by reducing the partial pressure of O.sub.2 above the adduct.

    Abstract translation: 由[化学式为[(A)a(R4N)b] z + x / z [Co(CN)n] x-xpS表示的高容量固态氰钴酸盐络合物,其中:A为碱金属原子,碱土金属原子, Zn,Cd或Hg原子; a为0至2.5的任何数,每个R独立地为C 1 -C 10取代或未取代的烷基,芳基或芳烷基; 或长链烃聚合物b是大于0至3的任何数为1,2或3; n是从3到5的任何数字; x是n-2; p是从大于零到6的任何数字; 并且S是能够与[(A)a(R 4 N)b 9 z +,Co或两者配位的配体。 能够化学结合氧以形成新的氧加合物,从而从含氧流体物流中选择性地除去氧。 可以通过增加温度或通过降低加合物上方的O 2分压来从络合物中回收结合的氧。

    Resins having improved exchange kinetics
    64.
    发明授权
    Resins having improved exchange kinetics 失效
    具有改进的交换动力学的树脂

    公开(公告)号:US5182026A

    公开(公告)日:1993-01-26

    申请号:US856615

    申请日:1992-05-04

    Inventor: William C. Pike

    CPC classification number: B01J45/00 B01J41/043 B01J41/14 Y10S423/14

    Abstract: Disclosed are novel ion-exchange and chelate-exchange resins having improved exchange kinetics for separating chemical species from liquids. The resins are prepared from copolymer beads consisting of a monovinyl aromatic monomer and a cross-linking monomer. The copolymer beads are functionalized such that weak-base exchange moieties are substituted at haloalkylated sites which are most accessible to diffusion into the beads, while hydrophilic, strong-base exchange moieties are substituted at haloalkylated sites which are least accessible to diffusion. The resins have improved exchange kinetics due to shortened diffusion path lengths for the chemical species being separated and improved diffusion into the resin beads due to the hydrophilic, strong-base exchange moieties.

    Abstract translation: 公开了具有改进的用于将化学物质与液体分离的交换动力学的新型离子交换和螯合交换树脂。 树脂由由单乙烯基芳族单体和交联单体组成的共聚物珠制备。 共聚物珠被官能化,使得弱碱交换部分在卤代烷基化位点被取代,其最容易扩散到珠中,而亲水的强碱交换部分在不能扩散的卤代烷基化位点被取代。 由于亲水的强碱交换部分,由于分离的化学物质的扩散路径长度缩短和树脂珠粒的扩散,树脂具有改善的交换动力学。

    Process for removing selenium from wastewater effluent
    68.
    发明授权
    Process for removing selenium from wastewater effluent 失效
    从废水中除去硒的工艺

    公开(公告)号:US4915928A

    公开(公告)日:1990-04-10

    申请号:US331360

    申请日:1989-03-31

    CPC classification number: B01J49/0013 B01J41/043 Y10S423/14

    Abstract: Disclosed is a process for removing selenium from wastewater effluent. The processd includes the steps of;(i) contacting a selenide containing wastewater and a strong-base anion exchange resin to absorb selenide on the resin;(ii) eluting the ion exchange resin with an eluant which is effective for stripping selenide therefrom; and(iii) recovering elemental selenium from the selenide containing eluate resulting from step (ii). Also disclosed is a process for regenerating the ion exchange resin by treatment of the resin with an acidic chlorate solution.

    Abstract translation: 公开了从废水流出物中除去硒的方法。 流程包括以下步骤: (i)使含有硒化物的废水和强碱阴离子交换树脂接触以在树脂上吸收硒化物; (ii)用洗脱液洗脱离子交换树脂,该洗脱剂有效地从其中提取硒化物; 和(iii)从由步骤(ii)得到的含有硒化物的洗脱液中回收元素硒。 还公开了通过用酸性氯酸盐溶液处理树脂来再生离子交换树脂的方法。

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