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    • 1. 发明授权
    • Process for recovery of reusable chromic acid from the waste chromic
acid solution containing impurities
    • 从含有杂质的废铬酸溶液中回收可重复使用的铬酸的方法
    • US4349514A
    • 1982-09-14
    • US66167
    • 1979-08-13
    • Morio WatanabeSanji Nishimura
    • Morio WatanabeSanji Nishimura
    • B01D11/04C01G37/00C01G37/033C01G37/14C02F1/469C23C22/86C25B1/00C25D21/16C25F7/02B01D11/00
    • B01D61/44C01G37/003C25B1/00B01D2311/04C02F1/469C02F2101/22Y10S204/13Y10S210/913
    • A process for recovery of reusable chromic acid from waste chromic acid solution containing impurities, which process comprises a first step in which the solution containing chromic acid is introduced into the cathode compartment in an electro-dialysis process and free chromic acid or chromate ions in the above solution are transferred to the anode compartment, a second step in which H.sub.2 SO.sub.4 is added in at least equivalent amounts to the heavy metallic ion contained in the outlet solution, in which chromic acid ion concentration is reduced, in order to convert chemical species of the contained metallic ion and increase the H.sup.+ ion concentration and then chromate ions in the resultant solution are extracted into an organic phase with contact of an organic solvent (A), and a third step in which residual amounts of chromic acid ion remaining in the aqueous raffinate from the second step are extracted into an organic phase with contact of an organic solvent (B). Organic solvents A and B are regenerated by stripping the organic phase with a suitable strip reagent.
    • 从含有杂质的废铬酸溶液中回收可再利用的铬酸的方法,该方法包括第一步骤,其中将含有铬酸的溶液在电渗析过程中引入阴极室,并且将游离的铬酸或铬酸根离子 将上述溶液转移到阳极室,第二步骤,其中以至少等量的量加入H 2 SO 4,其中所述重金属离子包含在出口溶液中,其中铬酸离子​​浓度降低,以便将化学物质转化为 含有金属离子并增加H +离子浓度,然后将所得溶液中的铬酸根离子与有机溶剂(A)接触而萃取到有机相中,并且残留在残液中的残余量的铬酸离子的第三步骤 从有机溶剂(B)与第二步骤萃取到有机相中。 有机溶剂A和B通过用合适的剥离试剂汽提有机相来再生。
    • 7. 发明授权
    • Process for electrolytically producing metals of Ni, Co, Zn, Cu, Mn, and
Cr from a solution thereof
    • 从其溶液中电解生产Ni,Co,Zn,Cu,Mn和Cr的金属的方法
    • US4789444A
    • 1988-12-06
    • US14260
    • 1987-02-12
    • Morio WatanabeSanji NishimuraNobuatsu Watanabe
    • Morio WatanabeSanji NishimuraNobuatsu Watanabe
    • C25C1/08C25C1/00C25C1/10C25C1/12C25C1/16
    • C25C1/00
    • Process for electrolytically producing metals of Ni, Co, Zn, Cu, Mn, and Cr, comprising, electrolyzing an aqueous solution containing ions of a metal as main component selected from Ni, Co, Zn, Cu, Mn, and Cr in a cathode compartment to deposit the metal electrolytically on a cathode, the cathode compartment being separated by one or more diaphragms from the remainder of the solution where iron or a metal containing iron is used for material of corrosible anode, and maintaining the concentration of iron ion in the solution circulating in the anode compartment at a low level by bringing the whole or a part of the circulating solution into contact with an organic solvent which is prepared by adding petroleum hydrocarbon for dilution of one or more extracting agents selected from the group consisting of carboxylic acids, alkylaryl phosphoric acids, hydroxyoximes, alkyl phosphoric acids, alkylamines, ketones, alkylamides, and neutral phosphoric acid esters, to extract and remove the iron or the chloro-complex ions.
    • 电解生产Ni,Co,Zn,Cu,Mn和Cr的金属的方法,包括:在阴极中电解含有作为主要成分的金属的离子的水溶液,其中Ni,Co,Zn,Cu,Mn和Cr 隔室将金属电解沉积在阴极上,阴极室由溶液的其余部分分隔开一个或多个隔膜,其中铁或含铁的金属用于可腐蚀阳极的材料,并将铁离子的浓度保持在 通过使全部或一部分循环溶液与通过添加石油烃制备的有机溶剂接触而在阳极室中循环的溶液处于低水平,所述有机溶剂用于稀释选自羧酸的一种或多种萃取剂 ,烷基芳基磷酸,羟基肟,烷基磷酸,烷基胺,酮,烷基酰胺和中性磷酸酯,以提取和除去铁 氯离子。
    • 8. 发明授权
    • Recovery process of uranium
    • 铀的回收过程
    • US4478804A
    • 1984-10-23
    • US411353
    • 1982-08-25
    • Morio WatanabeSanji Nishimura
    • Morio WatanabeSanji Nishimura
    • C01G43/00C22B60/02
    • C22B60/026
    • A recovery process of uranium comprising:(1) extracting uranium ions with an organic solvent containing one or more compounds selected from the group consisting of alkyl phosphoric acid, alkyl-aryl phosphoric acid, alkyl dithio phosphoric acid, aryl dithio phosphoric acid, neutral phosphoric acid ester and alkyl amine together with a petroleum hydrocarbon as a diluent; and(2) stripping the uranium ions in the resultant organic solvent from the step (1) to an aqueous phase with contact of an aqueous solution containing one or more compounds selected from the groups of NH.sub.4 F, NH.sub.4 HF.sub.2, KF or KHF.sub.2.
    • 铀的回收方法包括:(1)用含有一种或多种选自烷基磷酸,烷基 - 芳基磷酸,烷基二硫代磷酸,芳基二硫代磷酸,中性磷酸的一种或多种化合物的有机溶剂萃取铀离子 酸酯和烷基胺与石油烃一起作为稀释剂; 和(2)将所得有机溶剂中的铀离子从步骤(1)中除去含有一种或多种选自NH 4 F,NH 4 HF 2,KF或KHF 2的化合物的水溶液与水相接触。