Method for recovery of Nd.SUB.2.Fe.SUB.14.B grains from bulk sintered Nd—Fe—B magnets and/or magnet scraps by electrochemical etching
11232902 · 2022-01-25
Assignee
Inventors
Cpc classification
Y02P10/20
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
International classification
Abstract
The invention relates to a method for recovery of Nd.sub.2Fe.sub.14B grains from bulk sintered Nd—Fe—B magnets and/or magnet scraps. In this method the Nd—Fe—B magnets (1) and/or magnet scraps are anodically oxidized using a non-aqueous liquid electrolyte (5), said anodic oxidation releasing the Nd.sub.2Fe.sub.14B grains (6) in said Nd—Fe—B magnets (1) and/or magnet scraps. The released Nd.sub.2Fe.sub.14B grains (6) are collected during and/or after said anodic oxidation. The proposed method allows a more environmental friendly and cost-effective way for recycling EOL Nd—Fe—B magnets/Nd—Fe—B magnet scraps.
Claims
1. A method for recovery of Nd.sub.2Fe.sub.14B grains from bulk sintered Nd—Fe—B magnets and/or magnet scraps, in which method the Nd—Fe—B magnets and/or magnet scraps are anodically oxidized using a non-aqueous liquid electrolyte, said anodic oxidation releasing the Nd.sub.2Fe.sub.14B grains in said Nd—Fe—B magnets and/or magnet scraps, wherein the released Nd.sub.2Fe.sub.14B grains are collected magnetically during and/or after said anodic oxidation.
2. The method according to claim 1, characterized in that said anodic oxidation is performed in an electrochemical cell having an anode at least in part formed of said Nd—Fe—B magnets and/or magnet scraps.
3. The method according to claim 2, characterized in that a cathode of the electrochemical cell is formed of Cu.
4. The method according to claim 1, characterized in that said anodic oxidation is performed in a three-electrode electrochemical cell having an anode at least in part formed of said Nd—Fe—B magnets and/or magnet scraps, a cathode and a reference electrode.
5. The method according to claim 4, characterized in that the cathode is formed of Cu and the reference electrode is formed of a Pt material.
6. The method according to claim 1, characterized in that a non-aqueous solvent in which etched Nd-rich phases of the Nd—Fe—B magnets and/or magnet scraps dissolve is used as said liquid electrolyte.
7. The method according to claim 6, characterized in that the Nd-rich phases dissolved in the liquid electrolyte are also recovered by separating said Nd-rich phases from the electrolyte.
8. The method according to claim 1, characterized in that dimethylformamide is used as said liquid electrolyte.
9. The method according to claim 1, characterized in that an additive compound is added to said liquid electrolyte in order to enhance electrical conductivity of the electrolyte.
10. The method according to claim 9, characterized in that 0.05-0.3 mol L.sup.−1 FeCl.sub.2 is added as said additive compound.
11. The method according to claim 1, characterized in that the anodic oxidation is carried out at a temperature in a range between 0° C. and about 90° C.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) The proposed method will be described in the following by way of example in connection with the accompanying figures showing:
(2)
(3)
(4)
(5)
EXAMPLE FOR CARRYING OUT THE INVENTION
(6) In the following example of the proposed method Nd.sub.2Fe.sub.14B grains are recovered from an EOF Nd—Fe—B magnet using dimethylformamide as the liquid electrolyte.
(7) Regents
(8) Dimethylformamide (DMF, >99%) was purchased from Sigma-Aldrich, Germany. Prior to using, molecular sieves (4A, Sigma-Aldrich, China) which were dried under vacuum at 160° C. for more than 24 hours was added into DMF to remove the water. FeCl.sub.2.4H.sub.2O (>99.99%, Sigma-Aldrich) were dehydrated under vacuum at 140° C. for 24 hours. All dried chemicals were stored inside a closed bottle in an argon filled glove box with water and oxygen content below 1 ppm. The water concentration which was determined by Karl Fischer titration (C20S, Mettler-Toledo, Switzerland) in the electrolyte was less than 50 ppm. The sintered bulk Nd—Fe—B magnet waste (chemical composition: 66.34 wt. % Fe, 22.10 wt. % Nd, 5.78 wt. % Dy, 5.78 wt. % other elements) used in this example was supplied by Magneti Ljubljana d.d (Ljubljana, Slovenia). Prior to experiment, these bulk magnets were thermally demagnetized and mechanically polished to remove the coating.
(9) Instrumentation
(10) With reference to the schematic illustration in
EXAMPLE
(11) The proposed method is performed in this example using the three-electrode cell of
(12) The initial sintered bulk Nd—Fe—B magnet (
(13) After etching at 2 mA.Math.cm.sup.−2 for 360 min, powders were collected. The magnetic fraction of the etched powder that was collected and separated via external permanent magnet is shown in
(14) An XRD pattern of the magnetic powders mainly shows reflections characteristic of Nd.sub.2Fe.sub.14B phase (Reference PDF: 04-005-2711) (
(15) The etched Nd-rich phase which was dissolved in DMF after filtration was measured by ICP-MS (Inductively Coupled Plasma—Mass Spectrometry) (see
REFERENCES
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