The present invention relates to the extraction of lithium from liquid resources such as natural and synthetic brines, leachate solutions from clays and minerals, and recycled products.

Processes for purifying polyether polyols via treatment with ion exchange resins. A mixture that includes the polyether polyol and alkali metal ions is passed through a first bed that includes a cation exchange resin comprising carboxylic acid and/or phosphonic acid groups to remove alkali metal ions from the mixture. Thereafter, the product is passed through a second bed comprising an anion exchange resin comprising quaternary ammonium groups and a cation exchange resin comprising carboxylic acid and/or phosphonic acid groups to thereby produce a purified polyether polyol.

Processes for purifying polyether polyols via treatment with ion exchange resins. A mixture that includes the polyether polyol and alkali metal ions is passed through a first bed that includes a cation exchange resin comprising carboxylic acid and/or phosphonic acid groups to remove alkali metal ions from the mixture. Thereafter, the product is passed through a second bed comprising an anion exchange resin comprising quaternary ammonium groups and a cation exchange resin comprising carboxylic acid and/or phosphonic acid groups to thereby produce a purified polyether polyol.

The invention relates to a method of recycling lithium iron phosphate batteries with the aim of enabling the isolated recovery of elements from black mass. Black mass comprising at least cathodic and anodic components is immersed in a pH 13-14 solution to obtain a first leachate and first solid residue. The first leachate is immersed in a 4-6M acid solution to obtain a second leachate. The second leachate is passed through a first ion-exchange column where fluoride ions are retained and a second ion-exchange column where copper ions are to obtain a second eluate. The pH of the second eluate is adjusted to about 2.5-5 and a quantity of phosphoric acid that is sufficient to achieve an equivalent stoichiometric ratio of ferric iron and phosphate anions is added to obtain a first solution and an iron (III) phosphate precipitate. The first solution is combined with the first leachate to obtain a second solution. The pH of the second solution is adjusted to about 6.5 to a residual precipitate and a lithium solution.

The present invention relates to the extraction of lithium from liquid resources such as natural and synthetic brines, leachate solutions from clays and minerals, and recycled products.

The present invention relates to the extraction of lithium from liquid resources such as natural and synthetic brines, leachate solutions from clays and minerals, and recycled products.

The present disclosure relates processes and systems for producing and/or purifying .sup.68Ga from an irradiated substrate of .sup.68Zn. In some embodiments, the process rely on the use two cation-exchange chromatography columns to separate .sup.68Ga from .sup.68Zn and other radionuclides and metallic impurities. The process achieves a high overall yield of .sup.68Ga and a high effective molar activity while being implementable in a time compatible with the short half-life of .sup.68Ga. In additional embodiments, the process is implemented by an automated system.

The present disclosure relates processes and systems for producing and/or purifying .sup.68Ga from an irradiated substrate of .sup.68Zn. In some embodiments, the process rely on the use two cation-exchange chromatography columns to separate .sup.68Ga from .sup.68Zn and other radionuclides and metallic impurities. The process achieves a high overall yield of .sup.68Ga and a high effective molar activity while being implementable in a time compatible with the short half-life of .sup.68Ga. In additional embodiments, the process is implemented by an automated system.

A method and device of removing and recycling metals from a mixing acid solution, includes adsorbing a mixing acid solution with a pH value of ?1 to 4 and a cobalt ion concentration of 100 to 1,000 mg/L by at least two cation resins in series setting to the cobalt ion concentration in the mixing acid solution is less than 10 mg/L, and then adjusting the pH value of the mixing acid solution after adsorption to meet a discharge standard, wherein the particle size of the at least two cation resins in series setting is 150?1,200 ?m. After the cation resins are saturated by adsorption, regenerating the cation resins by sulfuric acid to form a cobalt sulfate solution, and then electrolytically treating the cobalt sulfate solution to obtain electrolytic cobalt and sulfuric acid electrolyte. The operation process is simple without complicated equipment, and it can effectively recycle metals from mixing acid solutions. The cationic resin and sulfuric acid solution can also be reused, so the method of the present invention has environmental and economic benefits.

An ion exchange system includes a first ion exchange column containing a first resin having an affinity for sulfate ions and nitrate ions that is greater than the first resin's affinity for chloride ions. The first ion exchange column is configured to pass a predetermined mass flow rate of drainage water therethrough. A second ion exchange column is connected in series with the first ion exchange column. The second ion exchange column contains a second resin having an affinity for chloride ions and is configured to pass the same predetermined mass flow rate of the same drainage water therethrough. As the drainage water passes through the first ion exchange column, primarily sulfate ions and/or nitrate ions are removed from the drainage water. As the drainage water passes through the second ion exchange column, primarily chloride ions are removed from the drainage water.