# US 5,708,958 A · Method of separating trivalent actinides and rare earth elements > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 5,708,958 A - Document ID: US5708958A - Status: Granted - Kind: A - Application number: 08/695,570 - Filed: 1996-08-12 - Granted: 1998-01-13 - Earliest claimed: 1995-09-12 - Assignees: Doryokuro Kakunenryo Kaihatsu Jigyodan - Inventors: Yoshikazu Koma; Masayuki Watanabe; Shinichi Nemoto - Web page: https://patentgrep.com/patent/US5708958A ## CPC - C22B 3/408: {using a mixture of phosphorus-based acid derivatives of different types} - C22B 59/00: Obtaining rare earth metals - C22B 60/0295: {obtaining other actinides except plutonium} - G21C 19/48: Non-aqueous processes - Y02E 30/30: Nuclear fission reactors - Y02P 10/20: Recycling - Y02W 30/50: Reuse, recycling or recovery technologies - C22B: PRODUCTION AND REFINING OF METALS (electrolytic C25); PRETREATMENT OF RAW MATERIALS - G21C: NUCLEAR REACTORS (fusion reactors, hybrid fission-fusion reactors G21B; nuclear explosives G21J) - Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION - Y02P: CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS - Y02W: CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT ## Abstract A method is provided for separating trivalent actinides and rare earth elements in the TRUEX method using a CMPO-TBP mixed solvent. The method of separating trivalent actinides and rare earth elements comprises a trivalent actinide/rare earth extraction step wherein trivalent actinides and rare earth elements are extracted by a solvent from highly acid waste generated by reprocessing of spent nuclear fuel, a nitric acid removal step wherein the nitric acid concentration of the solvent used to extract the trivalent actinides and rare earth elements is reduced, and a separation step wherein the trivalent actinides and rare earth elements contained in the solvent of low nitric acid concentration, are separated from each other. ## Claims ### Claim 1 A method of separating trivalent actinides and rare earth elements comprising the following steps: extracting trivalent actinides and rare earth elements from a highly acidic waste generated by reprocessing of spent nuclear fuel, by a solvent, reducing the nitric acid concentration in said solvent used to extract said trivalent actinides and said rare earth elements, and separating said trivalent actinides and said rare earth elements contained in said solvent having a low nitric acid concentration from each other. ### Claim 2 (depends on 1) A method of separating trivalent actinides and rare earth elements as defined in claim 1 wherein, in said trivalent actinide/rare earth extraction step, said trivalent actinides and rare earth elements are extracted using a solvent comprising a mixture of octyl (phenyl)-N,N-di-isobutylcarbamoylmethyl phosphine oxide of 0.2M concentration, tributylphosphoric acid (TBP) of 1.0-1.4M concentration, and a hydrocarbon diluent. ### Claim 3 (depends on 1) A method of separating trivalent actinides and rare earth elements as defined in claim 1 wherein, in said nitric acid removal step, a predetermined amount of nitric acid is removed from said solvent while maintaining said trivalent actinides and said rare earth elements in said solvent by bringing said solvent used to extract said trivalent actinides and rare earth elements in contact with an aqueous solution of nitric acid having a concentration of 0.1M or less and containing 0.2-1.0M of a nitrate, in order to reduce the nitric acid concentration of said solvent to 0.01M or less. ### Claim 4 (depends on 3) A method of separating trivalent actinides and rare earth elements as defined in claim 3, wherein, in said rare earth element/trivalent actinide separation step, an aqueous solution comprising nitrates having a concentration of 1-5M and a complexing agent having a concentration of 0.01-0.1M, is brought in contact with said solvent containing said trivalent actinides and said rare earth elements, the nitric acid concentration of said solvent having been reduced to 0.01M or less. ### Claim 5 (depends on 1) A method of separating trivalent actinides and rare earth elements as defined in claim 1 wherein the pH of the treated solvent in said rare earth element/trivalent actinide separation step lies in the range of 1.5-3. ### Claim 6 (depends on 4) A method of separating trivalent actinides and rare earth elements as defined in claim 4 wherein said nitrates used in said nitric acid removal step and said rare earth element/trivalent actinide separation step comprise one or more metal nitrates chosen from a group comprising alkali metal nitrates and alkaline earth metal nitrates, or hydroxylammonium nitrate. ### Claim 7 (depends on 1) A method of separating trivalent actinides and rare earth elements as defined in claim 1, wherein the pH of the treated solvent in said rare earth element/trivalent actinide separation step lies in the range of 1.8-2.2. ### Claim 8 (depends on 4) A method of separating trivalent actinides and rare earth elements as defined in claim 4, wherein said complexing agent used in said rare earth element/trivalent actinide separation step is an aminopolyacetic acid. ### Claim 9 (depends on 4) A method of separating trivalent actinides and rare earth elements as defined in claim 4, wherein said complexing agent used in said rare earth element/trivalent actinide separation step is at least one substance selected from the group consisting of diethylenetriamine pentacetic acid, ethylenediamine tetracetic acid and nitrilotriacetic acid. ### Claim 10 (depends on 4) A method of separating trivalent actinides and rare earth elements as defined in claim 4, wherein the process temperature in said rare earth element/trivalent actinide separation step lies within a range from 25.degree. C. to 40.degree. C. ### Claim 11 (depends on 1) A method of separating trivalent actinides and rare earth elements as defined in claim 1, further comprising stripping rare earth elements alone using dilute nitric acid from the solvent containing said rare earth elements which have been separated from said trivalent actinides.