Method for separating zinc, iron, calcium, copper and manganese from the aqueous solutions of cobalt and/or nickel
    2.
    发明授权
    Method for separating zinc, iron, calcium, copper and manganese from the aqueous solutions of cobalt and/or nickel 有权
    从钴和/或镍的水溶液中分离锌,铁,钙,铜和锰的方法

    公开(公告)号:US08357226B2

    公开(公告)日:2013-01-22

    申请号:US12918119

    申请日:2009-02-18

    IPC分类号: C22B3/26 C22B3/42

    摘要: A method is provided for separating the impurities zinc, iron, calcium, copper and/or manganese from an aqueous solution that contains cobalt and nickel. The solution is brought into a mixing contact with an extraction solution, which is pre-loaded with cobalt and nickel ions, whereby the cobalt and nickel in the extraction solution are replaced with the impurity metals, and the aqueous solution is cleaned from impurities after this phase. This purified aqueous solution, raffinate, can be used to pre-charge the extraction solution so that a minor part of the raffinate is contacted with a pre-neutralized extraction solution, whereby the cobalt and nickel replace the alkali metal, alkali earth metal or ammonium ion that is used in the pre-neutralization.

    摘要翻译: 提供了从含有钴和镍的水溶液中分离杂质锌,铁,钙,铜和/或锰的方法。 将溶液与预先加有钴和镍离子的提取溶液进行混合接触,由此将提取溶液中的钴和镍替换为杂质金属,并在此之后将水溶液从杂质中清除 相。 这种纯化的水溶液,提余液可用于对萃取溶液进行预充电,使得少量的萃余液与预中和的萃取溶液接触,由此钴和镍代替碱金属,碱土金属或铵 用于预中和的离子。

    Separations of actinides, lanthanides and other metals
    3.
    发明授权
    Separations of actinides, lanthanides and other metals 失效
    锕系元素,镧系元素和其他金属的分离

    公开(公告)号:US5409678A

    公开(公告)日:1995-04-25

    申请号:US31053

    申请日:1993-03-11

    摘要: An organic extracting solution comprised of a bis(acylpyrazolone or a substituted bis(acylpyrazolone) and an extraction method useful for separating certain elements of the actinide series of the periodic table having a valence of four from one other, and also from one or more of the substances in a group consisting of hexavalent actinides, trivalent actinides, trivalent lanthanides, trivalent iron, trivalent aluminum, divalent metals, and monovalent metals and also from one or more of the substances in a group consisting of hexavalent actinides, trivalent actinides, trivalent lanthanides, trivalent iron, trivalent aluminum, divalent metals, and monovalent metals and also useful for separating hexavalent actinides from one or more of the substances in a group consisting of trivalent actinides, trivalent lanthanides, trivalent iron, trivalent aluminum, divalent metals, and monovalent metals.

    摘要翻译: 一种由双(酰基吡唑啉酮或取代的二(酰基吡唑啉酮)组成的有机萃取溶液和一种萃取方法,该萃取方法可用于从周期表中分离出四价四价锕系元素的某些元素, 由六价锕系元素,三价锕系元素,三价镧系元素,三价铁,三价铝,二价金属和一价金属组成的组中的物质,以及由六价锕系元素,三价锕系元素,三价镧系元素组成的组中的一种或多种物质 ,三价铁,三价铝,二价金属和一价金属,也可用于从三价锕系元素,三价镧系元素,三价铁,三价铝,二价金属和一价金属中的一种或多种物质中分离六价锕系元素 。

    Amino methylphenyl silicon compounds
    4.
    发明授权
    Amino methylphenyl silicon compounds 失效
    氨基甲基苯基硅化合物

    公开(公告)号:US3171851A

    公开(公告)日:1965-03-02

    申请号:US15759061

    申请日:1961-12-06

    发明人: PEPE ENRICO J

    摘要: Lubricating oils consist of (i) silanes of the general formula wherein Z is hydrogen or a saturated or unsaturated monovalent hydrocarbon radical preferably having 1 to 18 carbon atoms, R is a monovalent hydrocarbon radical free from aliphatic unsaturation, n is 1 to 20, a is 1 or 2; b is 0, 1 or 2 and (a+b) is 1, 2 or 3; and (ii) siloxanes containing at least one group represented by the formula wherein Z, n, a, b, and (a+b) have the above meaning and R1 is R or a group OR.ALSO:The invention comprises (1) silanes of formula wherein Z is hydrogen or a saturated or unsaturated monovalent hydrocarbon radical preferably containing 1 to 18 carbon atoms, R is a monovalent hydrocarbon radical free from aliphatic unsaturation, a is 1 or 2, b is 0, 1 or 2 and (a+b) is 1, 2 or 3, and (2) siloxanes containing at least one unit represented by the formula wherein n, Z, a, b and (a+b) have the above meanings and R1 is equal to R or is a hydrocarbonoxy radical OR. The siloxanes can have linear, cyclic or branched structures and may form copolymers with at least one group wherein R1 is as above and c may be 0, 1, 2 or 3. They are prepared by hydrogenating the corresponding cyanophenylalkyl silicon compound and the primary amine formed may be converted to secondary or tertiary amines using alkyl halides or dialkyl sulphates. The hydrogenation is preferably conducted under a hydrogen pressure of 100 to 133 atmos. and at temperatures of 80 DEG to 140 DEG C. Catalysts may be used, e.g. platinum and palladium which may be supported on the gamma-allotrope of alumina or charcoal and other catalysts used include nickel cobalt and cyclopentadienyl metal compounds. Suitable solvents include alcohols and hydrocarbons. The siloxanes may also be prepared by hydrolysis of the corresponding silane which may also be cohydrolysed with groups. The examples describe the preparation of beta-(p-aminomethylphenyl)-ethyltriethoxysilane from the corresponding cyanophenylsilane and its subsequent hydrolysis and condensation to form a resin composed of the groups Uses: Corrosion inhibitors, lubricating oils, sequestering agents and coatings for metals. The starting materials are prepared by reacting an alkali metal cyanide with bromophenylalkylhydrocarbonoxysilane in a highly polar organic liquid, e.g. diethylformamide, in presence of cuprous cyanide and copper at 25-250 DEG C. Hydrolysis produces the corresponding siloxane starting materials.

    Extractants
    5.
    发明授权
    Extractants 失效
    萃取剂

    公开(公告)号:US4370237A

    公开(公告)日:1983-01-25

    申请号:US193280

    申请日:1980-05-21

    IPC分类号: B01D11/04 C22B3/26 C22B3/38

    摘要: An extraction process for extracting ionic values from an aqueous solution containing same which comprises contacting the aqueous solution with an organic hydrophobic liquid extractant phase comprising an extractant for ions, the molecules of which extractant contain at least one hydrophobic group selected from cyclic phosphazene radicals, linear siloxane radicals, cyclic siloxane radicals, and three-dimensional siloxane radicals, and stripping resulting loaded extractant phase with an aqueous stripping liquid phase.

    摘要翻译: PCT No.PCT / GB79 / 00171 Sec。 371日期1980年5月21日 102(e)日期1980年5月21日PCT提交1979年10月25日PCT公布。 出版物WO80 / 00796 日期:1980年5月1日。一种用于从含有该溶液的水溶液中提取离子值的提取方法,其包括使该水溶液与包含用于离子的萃取剂的有机疏水性液体萃取剂相接触,所述萃取剂的分子含有至少一个选自 从环状磷腈基团,直链硅氧烷基团,环状硅氧烷基团和三维硅氧烷基团,并用水性剥离液相汽提得到的负载萃取剂相。

    METHOD FOR SEPARATING ZINC, IRON, CALCIUM, COPPER AND MANGANESE FROM THE AQUEOUS SOLUTIONS OF COBALT AND/OR NICKEL
    8.
    发明申请
    METHOD FOR SEPARATING ZINC, IRON, CALCIUM, COPPER AND MANGANESE FROM THE AQUEOUS SOLUTIONS OF COBALT AND/OR NICKEL 有权
    从钴和/或镍的水溶液中分离锌,铁,钙,铜和锰的方法

    公开(公告)号:US20110072937A1

    公开(公告)日:2011-03-31

    申请号:US12918119

    申请日:2009-02-18

    IPC分类号: C22B23/00

    摘要: The invention relates to a method for separating the impurities zinc, iron, calcium, copper and/or manganese from aqueous solutions that contain cobalt and/or nickel. An aqueous solution (1) containing metallic salts is brought into a mixing contact with an extraction solution (2), which is pre-loaded with cobalt and/or nickel ions, whereby the cobalt and/or nickel in the extraction solution are replaced with the impurity metals, and the aqueous solution is cleaned from impurities after this phase. This purified aqueous solution, raffinate (3), can be used to pre-charge the extraction solution with cobalt and/or nickel ions, so that a minor part (5) of the raffinate is contacted with a pre-neutralized extraction solution (6), whereby the cobalt and/or nickel replace the alkali metal, alkali earth metal or ammonium ion that is used in the pre-neutralization. After this pre-charging stage, the aqueous solution that contains said alkali metal, alkali earth metal and/or ammonium ion, but no cobalt and/or nickel, is conveyed as reject (7) out of the process. After the extraction stage, the extraction solution (8) can be washed at a separate washing stage with washing water (9) that contains impurity metal chlorides. In that case, the cobalt and/or nickel ions remaining in the extraction solution are replaced with the impurity ions and they transfer to the chloride-containing aqueous solution. This washing water (11) can be conveyed to the pre-charging stage mentioned above, whereby the chloride ions that come along are removed to the reject. After the washing stage, the impurities can be back-extracted into the aqueous solution by the aqueous solution (13) of hydrochloric acid.

    摘要翻译: 本发明涉及从含有钴和/或镍的水溶液中分离杂质锌,铁,钙,铜和/或锰的方法。 将含有金属盐的水溶液(1)与预先加有钴和/或镍离子的提取溶液(2)进行混合接触,由此将萃取溶液中的钴和/或镍置换为 杂质金属和水溶液在该相之后被清除杂质。 该纯化水溶液(3)可用于用钴和/或镍离子对萃取溶液预充电,使得少量(5)的萃余液与预中和的萃取溶液(6)接触 ),由此钴和/或镍取代用于预中和的碱金属,碱土金属或铵离子。 在该预充电阶段之后,含有所述碱金属,碱土金属和/或铵离子但不含钴和/或镍的水溶液作为废料(7)输送出该方法。 萃取阶段后,萃取液(8)可以在洗涤阶段用洗涤水(9)洗涤,洗涤水(9)含有杂质金属氯化物。 在这种情况下,残留在萃取溶液中的钴离子和/或镍离子被杂质离子代替,并转移到含氯化物的水溶液中。 该洗涤水(11)可以被输送到上述预充电阶段,由此将来来的氯离子除去到废料。 在洗涤阶段之后,杂质可以通过盐酸水溶液(13)反萃取到水溶液中。