Salt hydrate compositions for thermal energy storage systems
US-2025066658-A1 · Feb 27, 2025 · US
US2018134577A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018134577-A1 |
| Application number | US-201615577521-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 20, 2016 |
| Priority date | May 29, 2015 |
| Publication date | May 17, 2018 |
| Grant date | — |
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The present invention provides an aqueous cobalt chloride solution refinement method, in which impurities can be efficiently removed from a cobalt salt solution. Disclosed is a method for bringing metallic nickel into contact with an aqueous solution containing cobalt chloride to remove an impurity by a cementation reaction, in which the metallic nickel is washed with an acidic liquid having a pH of not more than 2.5 before the metallic nickel is brought into contact with the aqueous solution containing cobalt chloride. Since the metallic nickel is washed with the acidic liquid having a pH of not more than 2.5, a passive film on a surface of the metallic nickel is removed. The passive film is removed from the metallic nickel, and therefore, when the metallic nickel comes in contact with the aqueous solution containing cobalt chloride, an impurity more noble than the metallic nickel can be precipitated by the cementation reaction. In addition, since the metallic nickel is only washed with acid to be brought into contact with the aqueous solution containing cobalt chloride, the impurity can be easily removed from the aqueous solution containing cobalt chloride.
Opening claim text (preview).
1 . An aqueous cobalt chloride solution refinement method for bringing metallic nickel into contact with an aqueous solution containing cobalt chloride to remove an impurity by a cementation reaction, wherein the aqueous solution containing cobalt chloride has a pH of not less than 1.5 and not more than 2.5, and acidic liquid having a pH the metallic nickel is washed with an acidic liquid having a pH of not more than 2.5 before the metallic nickel is brought into contact with the aqueous solution containing cobalt chloride. 2 . The aqueous cobalt chloride solution refinement method according to claim 1 , wherein the aqueous solution containing cobalt chloride at room temperature is brought into contact with the metallic nickel. 3 . The aqueous cobalt chloride solution refinement method according to claim 1 , wherein the impurity is copper. 4 . The aqueous cobalt chloride solution refinement method according to claim 1 , wherein the aqueous solution containing cobalt chloride from which the impurity has been removed is used as a raw material of a positive electrode material containing in the composition of the positive electrode material nickel and cobalt in a nonaqueous electrolyte secondary battery. 5 . The aqueous cobalt chloride solution refinement method according to claim 4 , wherein the aqueous solution containing cobalt chloride is a process liquid in a nickel smelting process, and the aqueous solution containing cobalt chloride from which the impurity has been removed is used in a liquid state as a raw material of the positive electrode material. 6 . The aqueous cobalt chloride solution refinement method according to claim 1 , wherein the aqueous solution containing cobalt chloride at a liquid temperature of 10 to 40° C. is brought into contact with the metallic nickel.
Halides; Oxyhalides · CPC title
Chlorides; Oxychlorides · CPC title
Refining · CPC title
by chemical substitution, e.g. by cementation · CPC title
by substitution, e.g. by cementation · CPC title
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