# US 10,246,759 B2 · Method of recovering 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 10,246,759 B2 - Document ID: US10246759B2 - Status: Granted - Kind: B2 - Application number: 14/636,722 - Filed: 2015-03-03 - Published: 2016-09-01 - Granted: 2019-04-02 - Earliest claimed: 2015-02-27 - Assignees: Nippon Light Metal Company, Ltd.; The Jamaica Bauxite Institute Limited - Applicants: Nippon Light Metal Company, Ltd.; The Jamaica Bauxite Institute Limited - Inventors: Kaoru Sugita; Yasushi Kobayashi; Yoshihiro Taguchi; Wilmon Wallen-Bryan; Worrell Lyew You; Parris A Lyew-Ayee - Web page: https://patentgrep.com/patent/US10246759B2 ## CPC - C22B 3/44: by chemical processes (treatment or purification of solutions by liquid-liquid extraction C22B3/26, by ion-exchange extraction C22B3/42) - C22B 3/3846: {Phosphoric acid, e.g. (O)P(OH)3} - C22B 7/007: {by acid leaching} - C22B 59/00: Obtaining rare earth metals - Y02P 10/20: Recycling - C22B: PRODUCTION AND REFINING OF METALS (electrolytic C25); PRETREATMENT OF RAW MATERIALS - Y02P: CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS ## Abstract Provided is a method of recovering rare-earth elements by performing slight pH adjustment of a leachate, which does not require such significant pH adjustment as in conventional methods, reduces cost and effort, and can efficiently recover rare-earth elements in a bauxite residue in a good yield. The method of recovering rare-earth elements is a method of recovering rare-earth elements, the method including: a leaching step of bringing a raw material bauxite residue, which is produced as a by-product in a Bayer process, into contact with a liquid leaching agent to recover a leachate containing rare-earth elements; an extraction step of bringing the leachate into contact with an extraction treatment liquid containing a phosphoric acid ester-based extractant to recover an extract liquid containing the rare-earth elements; and a back extraction step of bringing the extract liquid into contact with a back extraction treatment liquid to recover the rare-earth elements, the leaching step including recovering a leachate having a pH of 0.5 or more and 1.2 or less by using an acidic liquid leaching agent, the extraction step including adjusting the pH of the leachate to 1.0 or more and 1.7 or less and then bringing the leachate into contact with the extraction treatment liquid. ## Claims ### Claim 1 A method of recovering rare-earth elements from a bauxite residue, which is produced as a by-product in a Bayer process and is used as a raw material, the method comprising: a leaching step of bringing the bauxite residue into contact with a liquid leaching agent to recover a leachate containing rare-earth elements; a pretreatment step of bringing the leachate recovered in the leaching step into contact with a pretreatment liquid containing one of a phosphoric acid ester-based extractant and a phosphonic acid ester-based extractant at a concentration of from 0.01 to 0.1 mol/L, followed by filtration treatment, to thereby recover a pretreated leachate containing the rare-earth elements; an extraction step of bringing the pretreated leachate into contact with an extraction treatment liquid containing a phosphoric acid ester-based extractant to recover an extract liquid containing the rare-earth elements; and a back extraction step of bringing the extract liquid into contact with a back extraction treatment liquid to recover the rare-earth elements, the leaching step comprising recovering a leachate having a pH of 0.5 to 1.2 by using an acidic liquid leaching agent, the extraction step comprising adjusting the pH of the pretreated leachate to 1.0 to 1.7 and then bringing the pretreated leachate into contact with the extraction treatment liquid under a condition that the pretreated leachate has an oxidation-reduction potential of 300 mV or less adjusted by a method of performing electrolytic reduction treatment, wherein the back extraction treatment liquid comprises a 40 to 60 mass % sulfuric acid aqueous solution, and wherein the extract liquid and the sulfuric acid aqueous solution are brought into contact with each other at a volume ratio of extract liquid:sulfuric acid aqueous solution of from 5:1 to 10:1, or wherein the back extraction treatment liquid comprises a 4 N to 8 N hydrochloric acid aqueous solution, and wherein the extract liquid and the hydrochloric acid aqueous solution are brought into contact with each other at a volume ratio of extract liquid:hydrochloric acid aqueous solution of from 5:1 to 10:1. ### Claim 2 (depends on 1) A method of recovering rare-earth elements according to claim 1, wherein the extraction treatment liquid in the extraction step contains the phosphoric acid ester-based extractant at a concentration of from 0.2 to 1.5 mol/L. ### Claim 3 (depends on 1) A method of recovering rare-earth elements according to claim 1, wherein the back extraction step comprises: dispersing a back extraction treatment liquid phase by bringing the extract liquid and the back extraction treatment liquid into contact with each other, to thereby form a phase separation structure having an extract liquid phase and the back extraction treatment liquid phase dispersing in the extract liquid phase, the dispersing being performed so that the back extraction treatment liquid phase has an average droplet diameter of from 0.2 to 1.0 mm; and recovering the rare-earth elements. ### Claim 4 (depends on 1) A method of recovering rare-earth elements according to claim 1, wherein the back extraction treatment liquid comprises the 40 to 60 mass % sulfuric acid aqueous solution, and wherein the extract liquid and the sulfuric acid aqueous solution are brought into contact with each other at the volume ratio of the extract liquid:the sulfuric acid aqueous solution of from 5:1 to 10:1. ### Claim 5 (depends on 1) A method of recovering rare-earth elements according to claim 1, wherein the back extraction treatment liquid comprises the 4 N to 8 N hydrochloric acid aqueous solution, and wherein the extract liquid and the hydrochloric acid aqueous solution are brought into contact with each other at the volume ratio of the extract liquid:the hydrochloric acid aqueous solution of from 5:1 to 10:1. ### Claim 6 (depends on 1) A method of recovering rare-earth elements according to claim 1, further comprises: subjecting the extract liquid used in the back extraction step to back extraction in presence of an acid aqueous solution as a back extractant so as to reduce an accumulated Al fraction and obtain an recycled extraction treatment liquid; and reusing the recycled extraction treatment liquid in the extraction step. ### Claim 7 (depends on 1) A method of recovering rare-earth elements according to claim 1, wherein the leaching step is conducted without adjusting the pH of the leachate to 2.5 to 3.5.