The present disclosure provides a thiodiglycolamic acid extractant, and a preparation method and use thereof, belonging to the technical fields of extractant synthesis and extraction separation in the field of hydrometallurgy. In the present disclosure, the preparation method includes: mixing thiodiglycolic anhydride, an alkyl-substituted secondary amine, and an organic reagent in proportion; subjecting a resulting mixed reactant to a reaction I by stirring in an ice-water bath for 10 min to 60 min, and then to a reaction II by stirring at 20 C. to 50 C. for 6 h to 24 h; after the reaction II is completed, conducting extraction on an obtained product, and subjecting an obtained organic phase to washing, drying, suction filtration, and rotary evaporation to obtain the extractant.

The present disclosure provides a thiodiglycolamic acid extractant, and a preparation method and use thereof, belonging to the technical fields of extractant synthesis and extraction separation in the field of hydrometallurgy. In the present disclosure, the preparation method includes: mixing thiodiglycolic anhydride, an alkyl-substituted secondary amine, and an organic reagent in proportion; subjecting a resulting mixed reactant to a reaction I by stirring in an ice-water bath for 10 min to 60 min, and then to a reaction II by stirring at 20 C. to 50 C. for 6 h to 24 h; after the reaction II is completed, conducting extraction on an obtained product, and subjecting an obtained organic phase to washing, drying, suction filtration, and rotary evaporation to obtain the extractant.

The proposed invention relates to processes of extraction and concentration of radio nuclides and can be used in radiochemical technologies when processing liquid radioactive wastes.

A method for extraction of americium from liquid radioactive wastes and its separation from rare-earth elements comprises simultaneous extraction of americium and rare-earth elements from radioactive nitrate solution with neutral solution of organic extracting agent in polar fluorinated organic solvent, washing of saturated with metals organic phase, selective re-extraction of americium. N,N,N,N-tetraalkyl-amide of diglycolic acid is used as an extracting agent and solution containing 5-20 g/L of complexon, 5-60 g/L of nitrogen-containing organic acid and 60-240 g/L of salting-out agent is used as a solution for re-extraction of americium.

Technical effect is the extraction of americium from acidic liquid radioactive solutions and its separation from all rare-earth elements in a single extraction cycle.

Provided is a system for efficiently recovering trace metal from a large amount of a raw material, such as when trace metal is recovered from nickel oxide ore. This ion exchange resin has, on a carrier, an amide derivative represented by the following general formula. In the formula, R1 and R2 represent the same or different alkyl groups, R3 represents a hydrogen atom or an alkyl group, and R4 represents a hydrogen atom or an arbitrary group, other than an amino group, bonded to carbon as an amino acid. The amide derivative is preferably a glycinamide derivative. The carrier preferably includes a primary amine and/or a secondary amine.

The present invention provides methods for recovering metals, including rare earth metals, from mixed metals. An example is the recovery of metals from electronic waste. The method of separation is based on the inversion and/or lowering of the thermodynamic energy barrier by using one or more stressors applied at appropriate ratios to create lower energy points in the thermodynamic energy landscape of the mixed metals. Example stressors include a) a chemical stress, b) a mechanical stress, c) a thermal stress, d) and electromagnetic radiation and/or light stress, an interfacial stress, and/or a magnetic flux gradient stress.

The present invention provides methods for recovering metals, including rare earth metals, from mixed metals. An example is the recovery of metals from electronic waste. The method of separation is based on the inversion and/or lowering of the thermodynamic energy barrier by using one or more stressors applied at appropriate ratios to create lower energy points in the thermodynamic energy landscape of the mixed metals. Example stressors include a) a chemical stress, b) a mechanical stress, c) a thermal stress, d) and electromagnetic radiation and/or light stress, an interfacial stress, and/or a magnetic flux gradient stress.

Uses of cyclic amine monoamides for extracting uranium(VI) and/or plutonium(IV) from an acidic aqueous solution, as well as for totally or partially separating uranium(VI) from plutonium(IV) from an acidic aqueous solution. A method for treating an aqueous solution resulting from the dissolution of spent nuclear fuel in nitric acid to extract, separate and decontaminate uranium(VI) and plutonium(IV) in a single cycle and without resorting to any operation of reducing plutonium(IV), and wherein a cyclic amine monoamide or a mixture of cyclic amine monoamides is used as extractant. The cyclic amine monoamides have formula (I):

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The manufacture method disclosed herein includes: a preparation step of preparing a recovery object containing lithium and a first metal element; a chlorination heating step of heating the recovery object together with a metal chloride to produce LiCl; and a water dissolution step of immersing the recovery object after the chlorination heating step in water to dissolve LiCl in water to obtain a Li solution. In the manufacture method disclosed herein, a heating temperature in the chlorination heating step is 1000 C. or lower, and the metal chloride contains a second metal element that is more easily chlorinated than the first metal element in the recovered object and more hardly chlorinated than lithium in the chlorination heating step. Thereby, Li can be easily recovered from the recovery object at a low temperature of 1000 C. or lower.

Provided is a system for efficiently recovering trace metal from a large amount of a raw material, such as when trace metal is recovered from nickel oxide ore. This ion exchange resin has, on a carrier, an amide derivative represented by the following general formula. In the formula, R1 and R2 represent the same or different alkyl groups, R3 represents a hydrogen atom or an alkyl group, and R4 represents a hydrogen atom or an arbitrary group, other than an amino group, bonded to carbon as an amino acid. The amide derivative is preferably a glycineamide derivative. The carrier preferably includes a primary amine and/or a secondary amine.

A method for recovering hafnium and impurity metals from a hafnium-containing waste residue, comprises dissolving the waste residue in sulfuric acid and ammonium sulfate to obtain an acidic solution, adjusting acidity of the acidic solution, and adding a complexing agent to obtain a material solution; conducting extraction to obtain a hafnium-loaded organic phase and an impurity metal ions-containing aqueous phase; subjecting the hafnium-loaded organic phase to purification, stripping, precipitation, and filtration, and washing and burning to obtain hafnium oxide; precipitating the impurity metal ions-containing aqueous phase, washing a resulting precipitate to remove the complexing agent; dissolving a resulting precipitates of the impurity metal ions in sulfuric acid, and adjusting acidity of a resulting solution to obtain a solution of the impurity metal ions; extracting the solution of the impurity metal ions to obtain an impurity metal ions-loaded organic phase, purifying and stripping to obtain oxides of the impurity metals.