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WO2000039514A1 - Method and device for melting rare earth magnet scrap and primary molten alloy of rare earth magnet - Google Patents

Method and device for melting rare earth magnet scrap and primary molten alloy of rare earth magnet Download PDF

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Publication number
WO2000039514A1
WO2000039514A1 PCT/JP1999/007264 JP9907264W WO0039514A1 WO 2000039514 A1 WO2000039514 A1 WO 2000039514A1 JP 9907264 W JP9907264 W JP 9907264W WO 0039514 A1 WO0039514 A1 WO 0039514A1
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WO
WIPO (PCT)
Prior art keywords
earth magnet
rare earth
scrap
crucible
melting
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP1999/007264
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French (fr)
Japanese (ja)
Other versions
WO2000039514A9 (en
Inventor
Yoichi Hirose
Tatsuo Go
Miki Renda
Nobuhiko Kawamura
Atsushi Otaki
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Resonac Holdings Corp
Original Assignee
Showa Denko KK
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Filing date
Publication date
Application filed by Showa Denko KK filed Critical Showa Denko KK
Priority to JP2000591371A priority Critical patent/JP4263366B2/en
Publication of WO2000039514A1 publication Critical patent/WO2000039514A1/en
Anticipated expiration legal-status Critical
Publication of WO2000039514A9 publication Critical patent/WO2000039514A9/en
Ceased legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B59/00Obtaining rare earth metals
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • C22B7/001Dry processes
    • C22B7/003Dry processes only remelting, e.g. of chips, borings, turnings; apparatus used therefor
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B9/00General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
    • C22B9/16Remelting metals
    • C22B9/22Remelting metals with heating by wave energy or particle radiation
    • C22B9/226Remelting metals with heating by wave energy or particle radiation by electric discharge, e.g. plasma
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B3/00Hearth-type furnaces, e.g. of reverberatory type; Electric arc furnaces ; Tank furnaces
    • F27B3/08Hearth-type furnaces, e.g. of reverberatory type; Electric arc furnaces ; Tank furnaces heated electrically, with or without any other source of heat
    • F27B3/085Arc furnaces
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B3/00Hearth-type furnaces, e.g. of reverberatory type; Electric arc furnaces ; Tank furnaces
    • F27B3/10Details, accessories or equipment, e.g. dust-collectors, specially adapted for hearth-type furnaces
    • F27B3/24Cooling arrangements
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Definitions

  • the present invention relates to a method of reusing an alloy having a high oxygen concentration such as scrap generated in a process of manufacturing a rare-earth magnet by a melting technique, a melting apparatus used in a recycling method, and a secondary melting method.
  • Rare-earth magnet primary molten alloy prepared in such a way that it can be used to produce magnetic alloy materials hereinafter referred to as “magnet alloys”. Background art
  • powdery scrap is generated during the process of cutting and polishing the sintered body. This is a state in which water used for cutting and powder of abrasives are mixed, and as a general method, a method of dissolving and extracting with an acid is used to recover useful metals such as rare earth elements. Already done.
  • a rare-earth metal that is extremely active in high-frequency melting, arc melting, and plasma melting is slag. Since it is difficult to separate rare earth metals from slag, a method has been proposed in which the amount of scrap added to virgin raw materials is limited and redissolved.
  • the problem with the melting method is that the surface of the molten metal is covered with the slag due to the large amount of slag generated, making it difficult to observe the state of the molten metal and measure the temperature; this slag adheres firmly to the inner wall of the crucible and grows As a result, the internal volume of the crucible is reduced, which causes a fence of the input material to be hung; the work of periodically removing the slag from the inner wall of the crucible becomes difficult, and the life of the crucible is shortened. And so on.
  • the present inventors have analyzed the cause of the low yield when the rare-earth magnet scrap is melted using a normal high-frequency induction melting furnace, and as a result, the rare-earth metal originally contained in the scrap was analyzed.
  • the oxide is separated from the scrap melt, the molten metal is also entrapped in the slag, causing the metal to be suspended in the oxide and the yield to deteriorate.
  • high oxygen concentration Slag was present in the form of slag, and the apparent amount of slag increased, resulting in a decrease in yield.
  • the method described in the above-mentioned Japanese Patent Application Laid-Open No. 8-31616 is a method in which a metal (alloy) containing a rare earth magnet constituent element as a main component, a so-called virgin raw material, is first dissolved to prepare a seed water, and then the scrap is produced.
  • This method belongs to the re-melting method rather than the scouring method in which oxides are positively removed by melting.
  • a method has been proposed in which a plasma arc is generated by separately providing a cathode torch and an anode torch (Japanese Patent Application Laid-Open Nos. 1991-1990, 3-8). 736, JP-A-7-126019, and JP-A-8-5247).
  • the plasma generated by this method is called twin-plasma.
  • the method of Japanese Patent Application Laid-Open No. Hei 7-126109 proposes a method of melting quartz glass in which impurities are not mixed from a container, and that the plasma has a high energy density and a granular silica is added to the container prior to melting. He states that laying down mosquitoes is important in achieving the desired effect.
  • Japanese Patent Application Laid-Open No. 3-25247 states that the twin torch plasma method is excellent in that it is easy to restart when melting waste such as incineration ash. As described above, it has been known that the conventional twin torch plasma dissolution method provides excellent results in dissolving oxide materials and wastes. Disclosure of the invention
  • the present invention relates to a method of separating oxides from any rare-earth magnet scrap, such as scrap generated in the process of manufacturing the rare-earth magnet and residues in the crucible generated when melting the raw material of the rare-earth magnet. Aggregation / dissolution that actively promotes separation By providing a melting and refining method, oxides can be partially separated and removed, and a very good yield can be achieved when the raw material for rare earth magnets is secondarily melted using the next vacuum high-frequency induction melting furnace. The purpose is to do so.
  • the method according to the first aspect of the present invention is the method for obtaining a raw material for producing a rare earth magnet by first melting a scrap of a rare earth magnet, wherein a water-cooled crucible or a refractory crucible in which a part or all of a molten metal holding part is insulated.
  • a scrap of rare earth magnet is charged into the crucible, and the scrap of rare earth magnet is melted by a plasma torch comprising at least one pair of an anode and a cathode provided so as to be located above the crucible.
  • the present invention relates to a method for melting scraps of rare earth magnets.
  • the apparatus for melting the rare earth scrap for carrying out the first method of the present invention is a method for holding a molten metal in a plasma arc melting furnace having a plasma torch comprising at least one pair of anode and cathode. It is characterized in that a water-cooled crucible or a refractory crucible in which part or all of the part is insulated is arranged.
  • a method according to a second aspect of the present invention is the method for obtaining a raw material for producing a rare earth magnet by first melting a scrap of the rare earth magnet, wherein the molten metal holding part has a heat insulating part and a water cooling part in a crucible.
  • the present invention relates to a method for dissolving scrap of rare earth magnets, which comprises inserting a lap and dissolving the scrap of rare earth magnets by a tundass arc or a transition type plasma arc.
  • a crucible in which a molten metal holding section includes a heat insulating part and a water cooling part is disposed in a tungsten arc or transition type plasma arc furnace. It is characterized by what has been done.
  • the method according to a third aspect of the present invention is the method for obtaining a raw material for producing a rare-earth magnet by first melting a scrap of the rare-earth magnet, wherein the molten-metal holding part is placed in a crucible having a heat insulating structure. And a tungsten arc or a transition type plasma arc is generated between a first electrode which locally covers the heat insulating surface of the crucible and a second electrode disposed above the crucible. And
  • the present invention relates to a rare earth magnet scrap melting method characterized by melting a rare earth magnet scrap.
  • the apparatus for melting the rare earth scrap for carrying out the third method of the present invention is a crucible having a heat retaining structure of a molten metal holding part in a tungsten arc or transition type plasma arc furnace, and And a second electrode disposed above the crucible.
  • the first electrode locally covers the heat insulating surface.
  • the alloy obtained by primary melting of the rare earth magnet scrap according to the present invention has a total of 10 to 40 wt% of Sm and Ce and 5 wt% of Nd for the SmCo system.
  • Fe force S 25 wt% or less Cu force 4 to 10 wt%, Zr 1 to 4 wt%, oxygen 0.1 wt% or less, and the balance is mainly Co.
  • the present invention relates to a primary molten alloy of a rare earth magnet scrap characterized by being an unavoidable impurity due to the rare earth magnet manufacturing process excluding oxygen and an invading element due to primary melting excluding Fe. .
  • Nd, Pr and Dy total 20 to 35 wt%, B force 0.9 to 1.2 wt%, and A1 force; 1 to 1 wt%, Co force 5 wt% or less, Cu force S 0.5 wt% or less, Nb force S 1 wt% or less, oxygen 0.1 wt% or less, balance Fe mainly And an inevitable impurity due to the rare earth magnet manufacturing process excluding oxygen, and an intrusion element due to primary dissolution excluding Fe, which is a primary molten alloy of a rare earth magnet scrap.
  • B force 0.9 to 1.2 wt%, and A1 force 1 to 1 wt%, Co force 5 wt% or less, Cu force S 0.5 wt% or less, Nb force S 1 wt% or less, oxygen 0.1 wt% or less, balance Fe mainly And an inevitable impurity due to the rare earth magnet manufacturing process excluding oxygen, and an intrusion element due to primary dissolution excluding Fe, which is a primary molten alloy of
  • the obtained primary molten alloy has advanced agglomeration and separation of oxides, it can be melted using the next vacuum high-frequency induction melting furnace, and the yield when reused can be extremely high.
  • melting by a tungsten arc melting furnace or a transition type plasma arc melting furnace is usually performed by a skull melting method using a copper water-cooled crucible in order to use a melting raw material as a direct counter electrode to an arc torch.
  • a shell (skull) of a solidified layer is formed on the inner surface of the water-cooled crucible by the raw material itself.
  • the NdFeB magnet is melted using a normal arc melting furnace or plasma melting furnace to scrap the SmCo magnet. If so, it becomes difficult to sufficiently raise the temperature of the molten metal above the melting point of the alloy. Therefore, if the melting is performed while keeping the temperature of the molten metal low, the deoxidizing scouring effect becomes insufficient. As a result, the yield of secondary melting of the obtained primary ingot is extremely low at 70% or less.
  • the convection of the molten metal which is essential for the separation and refining of oxides, becomes active when the temperature difference between the melting point and the molten material of the rare earth alloy material is 200 ° C or more.
  • the oxides that existed in the clamp are separated efficiently.
  • the difference in specific gravity between a rare earth magnet alloy and its rare earth oxide is small, and it is difficult to separate the oxide by flotation. That was one of the reasons why the conventional dissolution method did not reduce oxygen.
  • the viscosity difference of the alloy from the melting point is 200 ° C or more and the viscosity of the alloy becomes Very degraded. Therefore, it is considered that the separation of oxides by agglomeration and flotation progresses rapidly together with the stirring effect of plasma heating.
  • insulation generally assumes that a water-cooled crucible is made of a metal that is a good conductor of heat, and indicates the use of a contradictory poor conductor of heat. As a result, there is no skull in this heat insulating part. Specifically, a heat-insulated conductor is fixed to a part of a water-cooled crucible made of copper or the like in the molten metal holding part of the crucible to form an adiabatic part, or the crucible is made of a water-cooled metal part and a heat-insulated conductor part. Or the entire crucible is made of a poor conductor of heat.
  • Examples of poor conductors of heat include refractory materials such as alumina, zirconia, yttria, calcite, magnesia and the like and fired products of composite oxides thereof. Of these, alumina refractories are the most economical and durable. The mixing of aluminum from the refractory into the metal is controlled to a level that is not problematic by controlling the heat input from the plasma arc, etc., so that the temperature of the molten pool does not become too high. can do.
  • the molten metal holding part of the crucible is insulated to such an extent that a phenomenon such as the expansion of the molten pool occurs.
  • the heat insulation region is preferably at least 20%, more preferably at least 30%, and even more preferably at least 50% of the inner area of the crucible.
  • the entire inner area of the crucible may be insulated, or the whole may be a refractory crucible.
  • a refractory crucible it may be lined with a refractory inside a metal container (shell). S The refractories used for this lining may be fixed refractories or irregular refractories.
  • the shell can be jacket-cooled.
  • this method has the advantage of dissolving rare-earth magnet scraps with a high oxygen concentration, so it is not advisable to add virgin metal to the raw material to be dissolved.
  • part of the virgin metal preferably 30% by weight or less, is charged to the molten raw material. May be.
  • the virgin metal industrial pure iron, electrolytic iron, rare earth metals such as neodymium, rare earth mother alloys such as ferro neodymium, and ferroboron can be used.
  • the coagulation separation of oxides proceeds even if the molten metal holding time is prolonged, but its contribution is small compared to the temperature, which is not desirable from the viewpoint of productivity.
  • the skull remains, but the skull is thinner than in the case of a normal water-cooled crucible, and no skull is generated at the bottom or other portion where the refractory layer is arranged. You can do more.
  • the next raw material can be charged into the remaining skull to continue dissolution. At this time, the skull shrinks by the time the next raw material is charged, and a gap may occur between the skull and the crucible.
  • the raw materials are additionally charged as appropriate, and the molten metal is provided at the edge of the crucible and overflows from the tap hole, so that the tilting of the crucible is omitted. It is also possible to continue refining continuously.
  • the power supply is stopped at the time of tapping, the surface of the molten metal is covered with the oxide slag.
  • the slag layer is broken and a current-carrying part is formed by the raw material, so that current can be continuously supplied.
  • the twin torch plasma is composed of at least one pair of anode and cathode electrodes, so that the crucible does not need to be conductive.
  • Each torch is inserted from the top of the melting furnace chamber into the melting crucible with the tip of the torch inserted into the melting crucible so that the melting atmosphere is not impaired, the insertion angle is variable, and the vertical position can be adjusted. Have been.
  • the selection range of the voltage, current and input of the plasma torch needs to be changed according to the melting amount per batch and melting time. Generally, it is necessary to increase the plasma current and output as the melting time increases and the melting time decreases. For example, when dissolving 50 kg of scrap per batch, 150 to 300 kW is appropriate. When dissolving 200 kg of scrap, 400 to 600 kW is appropriate.
  • melting by a tungsten arc melting furnace or a transition type plasma arc melting furnace is usually performed by a skull melting method using a copper water-cooled crucible in order to make a melting raw material directly opposite an arc torch.
  • a shell (skull) of a solidified layer is formed by the raw material itself on the inner surface of the water-cooled crucible. The raw material fed into the side is dissolved. If a part of the water-cooled crucible is insulated with refractory, etc., the molten pool will be wide and deep. For this reason, the molten metal temperature can be easily raised. Therefore, convection in the molten metal of the rare-earth magnet scrap or in the crucible residue having a high oxygen concentration is promoted, and the oxides are easily floated. Can be promoted.
  • This method employs a different crucible structure from the second method.
  • a structure in which the molten metal holding portion of the crucible is covered with a refractory material to form a heat insulating structure, and a structure in which the refractory material is locally covered with a metal electrode (first electrode) is selected.
  • the refractory surface is locally covered with a metal electrode in order to secure the power supply.
  • a plate electrode for this coating.
  • a plate-shaped metal electrode if one or more holes are provided at the bottom of the crucible, the temperature of the molten metal rises, and after sufficient separation of oxygen, the metal electrodes on and around the holes become It is possible to extract the molten metal, that is, to tap the molten metal by utilizing the fact that the molten metal disappears.
  • the timing of tapping can be controlled by controlling the heat input from the tungsten arc or transitional plasma arc during melting, or by selecting the material and thickness of the metal electrode described later. Can also be adjusted.
  • an iron electrode can be used as the material of the metal electrode.
  • an electrode made of industrial pure iron an electrode made of a high melting point metal such as niobium, molybdenum, tantalum, or an alloy thereof can be used.
  • the heat input from the tungsten arc or the transition type plasma arc is controlled so that the temperature of the molten metal pool does not become too high in the same way as preventing the incorporation of aluminum when using an alumina refractory. By doing so, the incorporation of the metal elements constituting these electrodes into the substance to be dissolved can be suppressed to a level that is not problematic.
  • the primary molten alloy according to the present invention will be described. Since this is melted as an ingot of 1 to 50 kg that can be directly charged into the secondary melting furnace, it will be referred to as “primary ingot” below.
  • the primary ingot of the present invention has a significantly lower oxygen concentration than the scrap state, and is significantly lower than the conventional vacuum-melted primary ingot.
  • the composition of this primary ingot is analyzed, combined with the virgin raw material, and the composition is determined so that the desired composition is obtained. Secondary melting and fabrication by the method described in (1) above to obtain a magnet alloy.
  • the amount of oxygen in the metal is reduced by the primary melting, when the secondary melting is performed using a vacuum high-frequency melting furnace, the slag-like metal content due to the unseparated oxide remaining in the metal decreases. It is possible to improve the yield.
  • the amount of primary ingot obtained from the rare earth magnet scrap must be determined in consideration of the following points. This is because scrap has a high carbon concentration due to the lubricant used during magnetic field press forming in the magnet manufacturing process, and decarburization is almost expected during primary melting. Therefore, the carbon content in the primary ingot is typically as high as 0.04% or more. Incidentally, the carbon content of the magnet alloy melted from the virgin material alone is usually less than 0.04%, and typically about 0.02%. If the amount of addition of the primary ingot is too large, the secondary dissolution ingot may be added. The carbon content of the magnet also increases, which adversely affects the properties of the magnet obtained from it.
  • the primary ingot obtained by the present method can be secondary-dissolved as 50% by weight or less, and the remainder can be a virgin raw material ratio.
  • the secondary ingot obtained by mixing and melting the primary ingot and the virgin raw material is used as the alloy for the magnet.
  • the primary ingot alone may be used as a magnet alloy, and the ratio of this alloy may be limited in the pulverization and mixing step in the subsequent magnet production.
  • the composition of the primary ingot of the present invention 15 to 40% of the rare earth element and Fe as the main component of the balance define the component range obtained by dissolving the most common grade of scrap. It was done.
  • Oxygen is mixed in as impurities in the manufacturing process of the rare-earth magnet, particularly in the pulverization process or the sintering process. However, since this reduction is an important achievement of the present invention, it is limited to 0.1% or less.
  • the components of the alloy for the magnet include Sm—Fe, Cu, Zr, and Nd (which may be partially replaced by Pr, Dy) of the Co-based magnet, _Fe—
  • B-based magnets such as B, A1, Co, Cu, and Nb, and these are used as components of magnet alloys regardless of the quantity.
  • Sm—Co magnets Co is 40 to 60%
  • Fe is 10 to 25%
  • Cu is 4 to: L0%
  • Zr is 4% or less.
  • B is 0.9 ⁇ : 1.2%
  • A1 is 0.1 ⁇ 1.5%.
  • a metal such as Fe is mixed from the metal electrode used in the third method, in addition to the trace elements from the various refractories described above, for example, A1 and the like.
  • This Fe is a necessary component of the magnet alloy.
  • a 1 is S m
  • a Co-based magnet is a harmful element for magnetic properties, while a Nd-Fe-B magnet is acceptable as a small alloy element, but too much is harmful to magnetic properties. Therefore, its amount is preferably less than 1%.
  • FIG. 1 is a sectional view showing one embodiment of a water-cooled copper crucible for carrying out the first and second methods of the present invention.
  • FIG. 2 is a sectional view showing one embodiment of a refractory crucible for carrying out the first method of the present invention.
  • FIG. 3 is a diagram showing an embodiment of the first melting apparatus of the present invention using a twin torch plasma arc melting furnace.
  • FIG. 4 is a view showing one embodiment of the melting apparatus according to the second and third aspects of the present invention using a transfer type plasma arc melting furnace.
  • FIG. 5 is a perspective view showing one embodiment of a water-cooled copper crucible provided with a current-carrying part for carrying out the second method of the present invention.
  • FIG. 6 is a drawing showing one embodiment of a refractory crucible for carrying out the third method of the present invention.
  • FIG. 7 is a drawing showing another embodiment of a refractory crucible for carrying out the third method of the present invention.
  • FIG. 8 is a drawing showing still another embodiment of the refractory crucible for carrying out the third method of the present invention. Description of embodiments of the invention
  • FIG. 1 shows a crucible having a water-cooled structure made entirely of copper for carrying out the method of the present invention.
  • 1 is a copper crucible
  • 2 is a refractory plate
  • 3 is a raw material
  • 4 is a cooling water inlet
  • 5 is a cooling water passage
  • 6 is a cooling water outlet.
  • the refractory plate 2 only at the bottom of the crucible 1 and leaving the side wall of the water-cooled copper crucible, the heat input by plasma and the insulation by the refractory plate 2 are balanced. However, the molten pool can be deepened. Also, if only the bottom is insulated, it is possible to reduce the amount of expensive refractory used, the shape of the refractory is simple, the durability is excellent, and the cost is excellent because it is inexpensive. Dissolution method.
  • FIG. 2 shows a refractory crucible for carrying out the method of the present invention.
  • a refractory crucible is placed in a metal container.
  • 7 is an alumina crucible
  • 9 is an iron container.
  • the gap between the crucible and the container is filled with alumina powder 8.
  • FIG. 3 shows an embodiment of a twin torch plasma melting furnace.
  • reference numeral 10 denotes a plasma torch, which generates plasma 11 between the anode torch 10a and the cathode torch 10Ob.
  • Fig. 4 shows the transfer type plasma arc melting furnace.
  • reference numeral 15 denotes a plasma torch, which generates a plasma arc between the torch and the raw material charged in the copper crucible 1.
  • the tungsten arc melting furnace has a structure provided with a tungsten electrode in place of the plasma torch 15 and generates an arc between the electrode and the raw material.
  • 16 is a raw material charging pipe.
  • FIG. 5 shows a crucible provided with a current-carrying part 17.
  • the current-carrying part 17 is formed by bending an iron plate or the like in accordance with the inner shape of the crucible so as to be in contact with the inner wall of the water-cooled copper crucible. Melting by this method ⁇ The following rare earth magnet scrap can be charged and melted inside the skull left after tapping.
  • a gap is formed between the crucibles due to the shrinkage of the remaining skull, which causes the conductivity to deteriorate and the crucible to be melted.
  • an energizing section 17 for ensuring conduction between the crucible on one side and the skull.
  • Fig. 5 three plasma transistors are used. 1 shows a crucible used in a plasma arc furnace with three conductors, and three conducting parts are provided so that the conducting parts are arranged between two torches, respectively.
  • the metal electrode 20 is, for example, a plate-like electrode covering the bottom of the crucible, and the crucible is vertically separated into a bottom 21 and a side wall 22.
  • the electrode 20 is sandwiched between the bottom 21 and the side wall 22 so as to ensure that power is supplied from the outer periphery of the electrode 20 to the power supply.
  • a crucible structure after the rare earth magnet scrap is melted, the crucible is tilted and heated.
  • a crucible structure in which a tap hole 25 is provided at the bottom 21 of the crucible may be employed.
  • Example 1 (Example of the first invention)
  • Analytical value of primary ingot Nd + Pr-25. 2 wt%, Dy-2.1 wt%, A1-0.34 wt%, B-1.00 wt%, O — 0.018 wt%, C-0.04 wt%, Fe remaining.
  • the melting amount of each knuckle is 1.5 kg, and the melting point of this alloy is 1200 to 125 ° C, so the melting temperature is more than 300 ° C higher than this.
  • the crucible 1 had an inner diameter of 170 mm and a depth of 70 mm, and an alumina sintered plate 2 having a thickness of 2 Omm was disposed at the bottom.
  • the primary dissolution yield was calculated by dividing the product weight by the charged raw material weight.
  • the melting time in this twin torch plasma arc melting furnace was 13 minutes, and the melting power of the primary ingot was 2.8 kWh Zkg. Since the crucible bottom is insulated, the melting time is short and the melting power is small.
  • the obtained alloy was used as a raw material and melted in an argon gas atmosphere using a vacuum high-frequency induction melting furnace.
  • the primary ingot is usually added to the virgin raw material to make the magnet alloy composition, but in order to investigate the yield, the entire amount was melted with the primary ingot alone.
  • Table 1 shows the dissolution yield of the obtained primary ingot, the dissolution yield of the secondary dissolution, and the average oxygen analysis value of the primary ingot.
  • Example 2 (Example of the second invention)
  • a scrap of the NdFeB magnet used in Example 1 was used as a raw material, and an alumina crucible (FIG. 2) was arranged. It was melted in a chi-plasma arc furnace to obtain a primary ingot.
  • Analytical value of primary ingot N d + P r — 25.0 wt%, D y — 2.2 wt%, A 1-0.38 wt%, B-0.99 wt%, O — 0.019 wt%, C-0. ⁇ 4 wt%, Fe remaining.
  • the dissolution amount of the batch was 1.5 kg, and the melting temperature was 1550 ° C.
  • the aluminum crucible 7 has an inner diameter of 170 mm, a depth of 70 mm, and a thickness of 30 mm.
  • This solution The solution time was 12 minutes and the dissolution power of the primary ingot was 2.6 kWhkg. As in Example 1, the dissolution time was short and the dissolution power was low. Table 1 shows the dissolution yield and average oxygen concentration at this time. These values were also the same as in Example 1, and an ingot with a high yield and a remarkably reduced oxygen concentration could be obtained.
  • Example 1 The NdFeB-based magnet scrap and virgin raw material used in Example 1 were melted using a 15 kW vacuum high-frequency induction melting furnace. The amount of dissolution was 5 kg, and the amount of scrap added to the virgin material was 50%. Table 1 shows the dissolution yield and average oxygen analysis value of the obtained primary ingot. The dissolution yield is assumed to be 95%, which is the average yield when dissolving the virgin raw material using only the virgin raw material, and the dissolving yield of only the scrap is adjusted to match the overall yield. The yield was calculated and the value was given.
  • Example 2 Using the scrap of the NdFeB-based magnet used in Example 1 as a raw material, 5 kg was melted using a 15 kW vacuum high-frequency induction melting furnace to obtain a primary ingot. Analytical value of primary ingot: Nd + Pr-25.0 wt%, Dy-2.3 wt%, A1-0.35 wt%, B-1.01 wt%, O -0.020 wt%, C-0.04 wt%, Fe remaining.
  • Example 1 As in Example 1, this primary ingot was melted again using a vacuum high-frequency induction melting furnace. As in Example 1, the dissolution yield and average oxygen analysis value were determined and are shown in Tables 1 and 2. Comparative Example 3
  • the scrap material of the NdFeB magnet used in Example 1 was used as a raw material in a 50 kW twin torch plasma arc melting furnace using a water-cooled copper crucible without any heat insulation. 5 kg was dissolved to obtain a primary ingot. Analytical value of primary ingot: Nd + Pr—28.0 wt%, Dy-2.4 wt%, A1-0.322 wt%, B-1.02 wt%, O — 0.42 wt%, C-0.04 wt%, Fe remaining.
  • This device can melt scrap with a melting point of 1200 to 125 ° C, but the melting temperature cannot be raised sufficiently because the crucible is not insulated. It stopped at 0 ° C.
  • the skull was also thick, and about half of the charged raw material remained in the crucible as a skull.
  • the melting time in this plasma arc melting furnace was 22 minutes, and the melting power for the primary ingot was 13 kWh / kg.
  • this primary ingot was melted using a vacuum high-frequency induction melting furnace.
  • the dissolution yield and the average oxygen analysis value were determined and are shown in Table 1.
  • the oxygen analysis value in the primary ingot is very high, and the deoxidizing effect is insufficient.
  • the scrap is melted in a plasma arc furnace equipped with a normal water-cooled crucible crucible, it is not insulated, and is not kept at a high temperature even if it is melted. It is clear that the oxygen concentration inside remains high. For this reason, the yield in the secondary melting in the high frequency induction furnace was low, and was about the same as when scrap was melted as it was. Ingot dissolution yield, oxygen analysis
  • the melting amount per batch is 1.5 kg and the melting point of this alloy is 1300 ° C Therefore, the melting temperature was set to 160 ° C., which is higher by 300 ° C. than this.
  • the crucible 1 had an inner volume of 11 O mm in diameter and a depth of 70 mm, and an alumina sintered plate 2 having a thickness of 20 mm was arranged on the bottom thereof.
  • the melting time in this arc melting furnace was 11 minutes, and the melting power of the primary ingot was 1.5 kWh / kg. Because the bottom is insulated, the melting time is short and the melting power is small.
  • the obtained alloy was used as a raw material and melted in an argon gas atmosphere using a vacuum high-frequency induction melting furnace.
  • the primary ingot is usually added to the virgin raw material to make the composition of the magnet alloy, but in order to investigate the yield, the entire amount was melted with the primary ingot alone.
  • Table 2 shows the dissolution yield of the obtained primary ingot, the dissolution yield of the secondary dissolution, and the average oxygen analysis value of the primary ingot.
  • Example 3 a conductive part made of a pure iron plate (thickness 1 mm x width 15 mm, 3 pieces) was provided in contact with the inner wall of the water-cooled copper crucible shown in Fig. 5
  • a primary ingot of the following analysis value was obtained.
  • the analysis value of the primary ingot was Nd + Pr-24.8 wt%, Dy-2.1 wt%, A1-0.35 wt%, B-0.98 wt%, O -0.018 wt%, C-0.04 wt%, Fe remaining.
  • Example 3 a magnetic alloy was melt-formed using this primary ingot.
  • the dissolution yield was determined, and the average oxygen analysis value of the primary ingot was measured.
  • Table 2 also in the plasma arc melting furnace, remarkably reducing the oxygen concentration and a high secondary melting yield were obtained as in Example 3 by melting the scrap at a high temperature.
  • the residue remaining in the crucible (Sm—31.6 wt%, Fe-4.6 wt%, Zr — 2.0 wt%, O—2.8 wt%, Co remaining) and a 30 kW tungsten-arc melting furnace with a water-cooled copper crucible ( Figure 1) insulated with a sintered aluminum plate at the bottom Metals could be recovered by melting in an argon gas atmosphere using a furnace.
  • the dissolution amount is 1.5 kg
  • the dissolution yield of the obtained primary ingot is 75%
  • the composition analysis value is Sm-15.0 wt%, Fe-28.0 wt% , Cu—4.6 wt%, Zr 2.5 wt%, O—0.021 wt%, Co remaining.
  • the high oxygen concentration residue in the high-frequency induction furnace crucible in the production of SmCo-based magnetic alloys is also significantly reduced in oxygen by high-temperature arc melting. Expensive metals such as Sm and Zr could be recovered in high yield as reusable metal.
  • Example 7 Example of the second invention
  • Example 3 To the scrap of the NdFeB magnet used in Example 3, 10% of a virgin material containing Nd metal, which is significantly oxidized, was added, and a primary ingot was obtained in the same manner as in Example 3. Was. The oxygen analysis value of this ingot was sufficiently reduced to no significant difference from Example 1.
  • Example 8 (Example of the first invention)
  • a scrap of 45 kg of the NdFeB magnet used in Example 1 was used as a raw material, the side was insulated with a sintered alumina cylinder 23, and only the bottom was a water-cooled copper plate 24.
  • melting was performed in an argon gas atmosphere to obtain a primary ingot.
  • Analytical value of primary ingot is Nd + Pr-25.8 wt%, Dy-2.3 wt%, A1-0.34 wt%, B-1.00 wt%, O -0.018 wt%, C-0.04 wt%, Fe remaining.
  • the dissolution temperature was set at 160, the same as in Example 3.
  • the crucible 1 was a sintered alumina cylinder 23 having an inner diameter of 32 O mm, a depth of 150 mm and a thickness of 30 mm, and a water-cooled copper plate 24 was disposed at the bottom.
  • Example 3 the magnetic alloy was melt-formed using this primary ingot. As shown in Table 2, in this method, too, by dissolving the scrap at a high temperature, the oxygen concentration was significantly reduced and a high secondary dissolution yield was obtained.
  • Example 6 after the NdFeB-based magnet scrap raw material was melted and discharged, before the molten metal was completely solidified, additional raw materials were added without breaking the argon gas atmosphere. Again, electricity was applied to dissolve. When the molten metal in the crucible became full, a part of the molten metal was poured out by tilting the crucible, and the raw material was added, so that it could be melted continuously. In addition, the metal solidified in the tap at the top of the crucible, and an abnormal arc flew in this part at the beginning of energization, so the solidified metal in this part was cut out slightly to make the tap. The same primary ingot as in Example 8 was obtained by dissolution by such a method.
  • Example 10 (Example of the third invention)
  • Scrap of NdFeB-based magnet used in Example 3 45 kg As a raw material, the sides were insulated with a sintered alumina cylinder, and the bottom was also insulated with a sintered alumina plate.
  • a 300 kW plasma arc melting furnace equipped with a crucible as shown in Fig. 6 in which a circular plate made of pure iron was installed as a current-carrying part melting was performed in an argon gas atmosphere, and the primary ingot was cooled. Obtained.
  • the dissolution temperature was set at 160 ° C., the same as in Example 1.
  • the crucible 1 is a sintered alumina cylinder 10 having an inner diameter of 32 O mm, a depth of 15 O mm and a thickness of 30 mm, and an outer diameter of 32 O mm and a thickness of 3 O mm at the bottom thereof.
  • a sintered alumina circular plate was placed, and a 0.5 mm pure iron circular plate was placed inside.
  • Example 1 1 (Example of the third invention)
  • the side part was insulated with a sintered alumina cylinder 22 and the tap hole 25 was left in the center of the bottom.
  • the crucible shown in FIG. 8 was provided, in which a doughnut-shaped sintered alumina plate 21 was insulated, and a pure iron circular plate 20 was installed as a conducting part inside the pure iron part as a conducting part. Melting was performed in an argon gas atmosphere using a kw plasma arc melting furnace. When melted, the center of the steel plate was broken, and the molten metal flowed to the bottom, and a primary ingot was obtained in the mold installed underneath.
  • the analysis value of the primary ingot was Nd + Pr-25.5 wt%, Dy-2.2 wt%, A1-0.35 wt%, B-1.01 wt%, O — 0.018 wt%, C— 0.04 wt%, Fe remaining.
  • the sintered aluminum plate at the bottom was a doughnut having an inner diameter of 10 O mm, an outer diameter of 320 mm, and a thickness of 30 mm under the same conditions as in Example 10. Dissolved. In this method, slag and some metal remained in the crucible, so that a 40 kg ingot with little slag entrainment was obtained.
  • Example 1 2 Example of the third invention
  • Example 10 After melting and tapping under the same conditions as in Example 10, the slag on the upper part of the solidified metal remaining in the crucible was partially scraped off, the lower metal layer was exposed and the energized part was secured. Was added, and the method of melting by re-energizing was repeated. At this time, there was also a charge with a hole in the center of the remaining solidified metal. In this case, iron foil or an iron plate was placed to close the hole and the raw material was charged. In this method, the same ingot as in Example 10 was obtained. Industrial applicability

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Abstract

A magnet for increasing a yield attained during a process in which, when separating metals from scraps occurring during a rare earth magnet production process, alloy materials for rare earth magnet are melt-refined so as to positively separate oxides and then subjected to a secondary melting by using a vacuum high-frequency induction melting furnace; wherein part or all of the scraps (3) are charged into an insulated (2) water-cooled crucible (1) or a refractory crucible (7, 21, 22) and subjected to twin plasma arc (10A, 10b) melting and tungsten arc or migration arc (15) melting.

Description

明 細 書 希土類磁石のスクラ ップの溶解方法及び溶解装置、 並びに希土類磁石 スクラップの一次溶解合金 技術分野  Description Rare earth magnet scrap melting method and melting apparatus, and rare earth magnet scrap primary melting alloy

本発明は、 希土類磁石の製造工程で発生するスクラ ップ等の酸素濃度 の高い合金を溶融技術によ り再利用する方法、 及び再利用法に使用され る溶解装置、 並びに二次溶解によ り磁石合金素材 (以下 「磁石用合金」 と言う) を溶製できる状態に調製された希土類磁石一次溶解合金に関す る。 背景技術  The present invention relates to a method of reusing an alloy having a high oxygen concentration such as scrap generated in a process of manufacturing a rare-earth magnet by a melting technique, a melting apparatus used in a recycling method, and a secondary melting method. Rare-earth magnet primary molten alloy prepared in such a way that it can be used to produce magnetic alloy materials (hereinafter referred to as “magnet alloys”). Background art

最近、 磁気特性の優れた N d F e B系や S m C o系の希土類焼結磁石 の需要量が増えており、 それに伴い、 磁石の製造工程で発生するスクラ ップの量も増えている。 これらスクラ ップと しては、 焼結工程で発生す る焼結不良品、 切削加工時にチッビング等の原因で発生する形状不良品、 メ ツキ工程でピンホール等の原因で発生するメ ツキ不良品等のスクラ ッ プなどが挙げられる。 さ らに、 希土類磁石用合金を高周波誘導炉で真空 もしく は不活性ガス雰囲気中溶解する際に、 坩堝内に酸素濃度の高い残 留物が耐火内張り に付着して残留する。 これは溶解滓であるが、 広義の スクラップに含まれる。 その他に、 焼結体を切削、 研摩する過程で発生 する粉体状のスクラ ップが発生する。 これは、 切削時に用いる水や研削 材の粉末が混入した状態になっており 、 一般的な方法と して、 酸で溶解 し抽出する方法を用いて、 希土類元素等の有用な金属の回収が既に行わ れている。  Recently, the demand for rare earth sintered magnets based on NdFeB and SmCo, which have excellent magnetic properties, has increased, and the amount of scrap generated in the magnet manufacturing process has also increased. I have. These scraps include defective sintering products that occur during the sintering process, defective products that occur due to chipping or the like during cutting, and defects that occur due to pinholes or the like during the plating process. Scraps of non-defective products are included. In addition, when the alloy for rare earth magnets is melted in a high-frequency induction furnace in a vacuum or inert gas atmosphere, the residue with high oxygen concentration adheres to the refractory lining and remains in the crucible. This is molten slag, but is included in scrap in a broad sense. In addition, powdery scrap is generated during the process of cutting and polishing the sintered body. This is a state in which water used for cutting and powder of abrasives are mixed, and as a general method, a method of dissolving and extracting with an acid is used to recover useful metals such as rare earth elements. Already done.

焼結不良品、 形状不良品、 メ ツキ不良品については、 今まで、 経済的 な回収方法が見出されていないため、 磁石メーカーによっては、 将来再 利用法が出現することを見込んで貯め込んでいたり、 あるいは、 例えば、 S m C o系のスクラ ップのよ う に高価な C o を多く含んでいる合金の場 合は、 電気炉を用いて溶解し、 酸化し易い S mは酸化させてスラグ中に 移行させ、 C oのみメ タルと して回収する といつた溶融精練方法が採用 されている。 この場合 C o と同様に高価な有用金属である S mや Z r は 回収されていなかった。 希土類磁石のスク ラ ップを溶解する技術に関し ては特開平 8 — 3 1 6 2 4号公報があり 、 この説明による と、 高周波溶 解、 アーク溶解、 プラズマ溶解では極めて活性な希土類金属がスラグ化 し、 スラグから希土類金属を分離する こ とが困難であるので、 スク ラ ッ プのバージン原料に対する添加量を限定して、 再溶解する方法が提案さ れている。 Unsatisfactory sintering, defective shape, and defective plating Some recovery methods have not been found, so some magnet manufacturers may store them in anticipation of the emergence of a reuse method, or they may be expensive, for example, SmCo-based scrap. In the case of an alloy containing a large amount of Co, it was melted using an electric furnace, and Sm, which is easily oxidized, was oxidized and transferred to slag, and only Co was collected as metal. Melting scouring method is adopted. In this case, expensive useful metals such as Sm and Zr were not recovered. Japanese Patent Laid-Open No. 8-31624 discloses a technique for melting the scrap of a rare-earth magnet. According to this description, a rare-earth metal that is extremely active in high-frequency melting, arc melting, and plasma melting is slag. Since it is difficult to separate rare earth metals from slag, a method has been proposed in which the amount of scrap added to virgin raw materials is limited and redissolved.

しかし、 S m C o系、 N d F e B系のいずれの場合も、 磁石を製造す る工程で、 極めて活性な希土類元素を多く 含む合金を微粉砕し、 成形焼 結工程を通すため、 スク ラ ップ中には微細な酸化物が多量に存在し、 そ れをそのまま高周波誘導溶解炉で溶解しょ う と しても、 メ タル収率が極 めて低く 、 有効な再利用の技術と しては未確立である。 特に、 溶解法で の問題は、 スラグの発生量が多いため、 溶湯表面がスラグで覆われ、 溶 湯の状況観察や温度測定を困難にする ; このスラグは坩堝内壁に強固に 付着し成長するため、 坩堝の内容積を狭く し、 投入原料の柵吊 り の原因 となる ; さ らに、 定期的に実施する坩堝内壁に付着したスラグの剥ぎ取 り作業を困難にし、 坩堝の寿命を短くする等であった。  However, in both the SmCo-based and NdFeB-based systems, in the process of manufacturing the magnet, an alloy containing a large amount of extremely active rare earth elements is finely pulverized and passed through the forming and sintering process. A large amount of fine oxides are present in the scrap, and even if they are to be melted in a high-frequency induction melting furnace as they are, the metal yield is extremely low. It has not been established yet. In particular, the problem with the melting method is that the surface of the molten metal is covered with the slag due to the large amount of slag generated, making it difficult to observe the state of the molten metal and measure the temperature; this slag adheres firmly to the inner wall of the crucible and grows As a result, the internal volume of the crucible is reduced, which causes a fence of the input material to be hung; the work of periodically removing the slag from the inner wall of the crucible becomes difficult, and the life of the crucible is shortened. And so on.

通常の高周波誘導溶解炉を用いて希土類磁石スク ラ ップを溶解した場 合収率が低い原因を、 本発明者らが解析した結果、 元々 ス ク ラ ップに含 有されていた希土類金属酸化物がスク ラ ップ融体から分離される際、 溶 融状態のメ タル分も一緒にスラグに卷き込まれ、 メ タルが酸化物中に懸 濁した状態となって収率が悪化した り 、 あるいは、 酸素濃度の高いメ タ ル分がスラグ状に存在し、 見掛けのスラグ量が増えるため、 収率を悪化 させるこ とが判明した。 The present inventors have analyzed the cause of the low yield when the rare-earth magnet scrap is melted using a normal high-frequency induction melting furnace, and as a result, the rare-earth metal originally contained in the scrap was analyzed. When the oxide is separated from the scrap melt, the molten metal is also entrapped in the slag, causing the metal to be suspended in the oxide and the yield to deteriorate. Or high oxygen concentration Slag was present in the form of slag, and the apparent amount of slag increased, resulting in a decrease in yield.

前掲特開平 8 — 3 1 6 2 4号の方法は、 希土類磁石構成元素を主成分 とする金属 (合金) 一いわゆるバージン原料一を先ず溶解して種湯をつ く り 、 次にスク ラ ップを溶かし込む方法であるので、 溶融によ り酸化物 を積極的に除く精練法という よ りは再溶解法に属する。  The method described in the above-mentioned Japanese Patent Application Laid-Open No. 8-31616 is a method in which a metal (alloy) containing a rare earth magnet constituent element as a main component, a so-called virgin raw material, is first dissolved to prepare a seed water, and then the scrap is produced. This method belongs to the re-melting method rather than the scouring method in which oxides are positively removed by melting.

と ころで、 プラズマアークには、 トーチの電極を負極と し、 被溶解物 を陽極とする移行型アーク と、 トーチの電極を負極と し、 ノ ズルを陽極 と して、 トーチ自身が两極をもつ非移行型アーク との二種類がある。 最近、 上記方法とは異なり 、 別々に設けられた陰極 トーチと陽極 トー チによ り プラズマアークを発生させる方法が提案された (特開平 2 — 1 9 9 0 2 8号、 特開平 3 — 8 7 3 9号、 特開平 7 — 1 2 6 0 1 9号、 特 開平 8 — 5 2 4 7号参照) 。 この方法で発生されるプラズマをツイ ン ト —チブラズマと称する。  In the plasma arc, a transfer arc using the torch electrode as the negative electrode and the material to be melted as the anode, and the torch itself using the torch electrode as the negative electrode and the nozzle as the anode. There are two types of non-transitional arcs with. Recently, unlike the above method, a method has been proposed in which a plasma arc is generated by separately providing a cathode torch and an anode torch (Japanese Patent Application Laid-Open Nos. 1991-1990, 3-8). 736, JP-A-7-126019, and JP-A-8-5247). The plasma generated by this method is called twin-plasma.

例えば、 前掲特開平 7 — 1 2 6 0 1 9号の方法は、 容器から不純物を 混入させない石英ガラスの溶融方法を提案し、 プラズマのエネルギ密度 が高いこ と と、 溶融に先立ち容器に粒状シリ カを敷き詰めるこ とが所期 の効果を達成する上で重要である と述べている。 また特開平 3 — 5 2 4 7号は廃棄物の焼却灰など溶融するに際しツイ ン トーチプラズマ法は再 起動が容易である点で優れている と述べている。 このよ う に、 従来のッ イ ン トーチプラズマ溶解法は、 酸化物系材料や廃棄物の溶解に優れた結 果をもたらすこ とは知られていた。 発明の開示  For example, the method of Japanese Patent Application Laid-Open No. Hei 7-126109 proposes a method of melting quartz glass in which impurities are not mixed from a container, and that the plasma has a high energy density and a granular silica is added to the container prior to melting. He states that laying down mosquitoes is important in achieving the desired effect. Japanese Patent Application Laid-Open No. 3-25247 states that the twin torch plasma method is excellent in that it is easy to restart when melting waste such as incineration ash. As described above, it has been known that the conventional twin torch plasma dissolution method provides excellent results in dissolving oxide materials and wastes. Disclosure of the invention

本発明は、 希土類磁石の製造工程で発生するス ク ラ ップや希土類磁石 原料を溶解する際生じる坩堝内残留物などのあらゆる希土類磁石スク ラ ップから金属を分離する際に、 酸化物の凝集 · 分離を積極的に進める溶 融精練法を提供するこ とによって、 酸化物を部分的に分離除去して、 次 の真空高周波誘導溶解炉を用いて希土類磁石用原料を二次溶解する時に、 極めて良好な収率を達成することを目的とするものである。 The present invention relates to a method of separating oxides from any rare-earth magnet scrap, such as scrap generated in the process of manufacturing the rare-earth magnet and residues in the crucible generated when melting the raw material of the rare-earth magnet. Aggregation / dissolution that actively promotes separation By providing a melting and refining method, oxides can be partially separated and removed, and a very good yield can be achieved when the raw material for rare earth magnets is secondarily melted using the next vacuum high-frequency induction melting furnace. The purpose is to do so.

本発明の第 1 に係る方法は、 希土類磁石のスク ラ ップを一次溶解して 希土類磁石製造用原料を得る方法において、 溶湯保持部の一部又は全部 を断熱した水冷坩堝あるいは耐火物製坩堝に希土類磁石のスクラップを 装入し、 前記坩堝の上方に位置するよ う に設けられた少なく と も 1対の 陽極と陰極よ り なるプラズマ トーチによ り希土類磁石のスク ラップを溶 解することを特徴とする希土類磁石のスク ラップの溶解方法に関する。  The method according to the first aspect of the present invention is the method for obtaining a raw material for producing a rare earth magnet by first melting a scrap of a rare earth magnet, wherein a water-cooled crucible or a refractory crucible in which a part or all of a molten metal holding part is insulated. A scrap of rare earth magnet is charged into the crucible, and the scrap of rare earth magnet is melted by a plasma torch comprising at least one pair of an anode and a cathode provided so as to be located above the crucible. The present invention relates to a method for melting scraps of rare earth magnets.

また、 本発明の第 1 方法を実施するための希土類スク ラ ップの溶解装 置は、 少なく と も 1対の陽極と陰極よ り なるプラズマ トーチを備えたプ ラズマアーク溶解炉内に、 溶湯保持部の一部又は全部を断熱した水冷坩 堝あるいは耐火物製坩堝を配置したことを特徴とするものである。  Further, the apparatus for melting the rare earth scrap for carrying out the first method of the present invention is a method for holding a molten metal in a plasma arc melting furnace having a plasma torch comprising at least one pair of anode and cathode. It is characterized in that a water-cooled crucible or a refractory crucible in which part or all of the part is insulated is arranged.

本発明の第 2 に係る方法は、 希土類磁石のスクラ ップを一次溶解して 希土類磁石製造用原料を得る方法において、 溶湯保持部が断熱部分と水 冷部分とを有する坩堝に希土類磁石のスク ラ ップを装入し、 タンダステ ンアークまたは移行型プラズマアークにて希土類磁石のスクラ ップを溶 解することを特徴とする希土類磁石のスクラップの溶解方法に関する。  A method according to a second aspect of the present invention is the method for obtaining a raw material for producing a rare earth magnet by first melting a scrap of the rare earth magnet, wherein the molten metal holding part has a heat insulating part and a water cooling part in a crucible. The present invention relates to a method for dissolving scrap of rare earth magnets, which comprises inserting a lap and dissolving the scrap of rare earth magnets by a tundass arc or a transition type plasma arc.

また、 本発明の第 2方法を実施するための希土類スクラ ップの溶解装 置は、 タングステンアークまたは移行型プラズマアーク炉内に、 溶湯保 持部が断熱部分と水冷部分とを含む坩堝を配置したこ とを特徴とするも のである。  Further, in the apparatus for melting a rare earth scrap for performing the second method of the present invention, a crucible in which a molten metal holding section includes a heat insulating part and a water cooling part is disposed in a tungsten arc or transition type plasma arc furnace. It is characterized by what has been done.

本発明の第 3 に係る方法は、 希土類磁石のスク ラ ップを一次溶解して 希土類磁石製造用原料を得る方法において、 溶湯保持部が断熱構造を有 する坩堝に希土類磁石のスク ラ ップを装入し、 該坩堝の断熱面を局部的 に被覆する第 1 の電極と該坩堝上方に配置された第 2 の電極との間でタ ングステンアークまたは移行型プラズマアークを発生させることによ り、 希土類磁石のスク ラ ップを溶解するこ と を特徴とする希土類磁石のス ク ラ ップの溶解方法に関する。 The method according to a third aspect of the present invention is the method for obtaining a raw material for producing a rare-earth magnet by first melting a scrap of the rare-earth magnet, wherein the molten-metal holding part is placed in a crucible having a heat insulating structure. And a tungsten arc or a transition type plasma arc is generated between a first electrode which locally covers the heat insulating surface of the crucible and a second electrode disposed above the crucible. And The present invention relates to a rare earth magnet scrap melting method characterized by melting a rare earth magnet scrap.

また、 本発明の第 3方法を実施するための希土類スク ラ ップの溶解装 置は、 タ ングステンアークまたは移行型プラズマアーク炉内に、 溶湯保 持部が断熱構造を有する坩堝と、 該坩堝の断熱面を局部的に被覆する第 1 の電極と、 該坩堝上方に配置された第 2の電極と含んでなるこ とを特 徴とするものである。  Further, the apparatus for melting the rare earth scrap for carrying out the third method of the present invention is a crucible having a heat retaining structure of a molten metal holding part in a tungsten arc or transition type plasma arc furnace, and And a second electrode disposed above the crucible. The first electrode locally covers the heat insulating surface.

また、 本発明に係る希土類磁石スクラ ップを一次溶解してなる合金は、 S m C o系については、 S mと C e の合計で 1 0〜 4 0 w t %、 N dが 5 w t %以下、 F e力 S 2 5 w t %以下、 C u力 4〜 1 0 w t %、 Z r が 1 〜 4 w t %、 酸素が 0. 1 w t %以下、 残部が主と して C oであり、 さ らに酸素を除く希土類磁石製造工程に起因する不可避的不純物、 及び F e を除く一次溶解に起因した侵入入元素であるこ とを特徴とする希土 類磁石スクラ ップの一次溶解合金に関する。  Further, the alloy obtained by primary melting of the rare earth magnet scrap according to the present invention has a total of 10 to 40 wt% of Sm and Ce and 5 wt% of Nd for the SmCo system. Hereafter, Fe force S 25 wt% or less, Cu force 4 to 10 wt%, Zr 1 to 4 wt%, oxygen 0.1 wt% or less, and the balance is mainly Co. In addition, the present invention relates to a primary molten alloy of a rare earth magnet scrap characterized by being an unavoidable impurity due to the rare earth magnet manufacturing process excluding oxygen and an invading element due to primary melting excluding Fe. .

さ らに、 N d F e B系については、 N d, P r及び D yが合計で 2 0 〜 3 5 w t %、 B力 0. 9〜 1 . 2 w t %、 A 1 力; 0. 1 〜 1 w t %、 C o力 5 w t %以下、 C u力 S 0. 5 w t %以下、 N b力 S 1 w t %以下, 酸素が 0. l w t %以下、 残部が主と して F eであり 、 さ らに酸素を除 く希土類磁石製造工程に起因する不可避的不純物、 及び F e を除く一次 溶解に起因した侵入入元素であるこ と を特徴とする希土類磁石スクラ ッ プの一次溶解合金に関する。  In addition, for the NdFeB system, Nd, Pr and Dy total 20 to 35 wt%, B force 0.9 to 1.2 wt%, and A1 force; 1 to 1 wt%, Co force 5 wt% or less, Cu force S 0.5 wt% or less, Nb force S 1 wt% or less, oxygen 0.1 wt% or less, balance Fe mainly And an inevitable impurity due to the rare earth magnet manufacturing process excluding oxygen, and an intrusion element due to primary dissolution excluding Fe, which is a primary molten alloy of a rare earth magnet scrap. About.

これらの発明が達成した成果を要約して説明する と、 次のとおり であ る。  The following summarizes the results achieved by these inventions.

( 1 ) 得られる一次溶解合金は、 酸化物の凝集分離が進んでいるので、 次の真空高周波誘導溶解炉を用いて溶解し、 再利用する際の収率を極め て高くすることができる。  (1) Since the obtained primary molten alloy has advanced agglomeration and separation of oxides, it can be melted using the next vacuum high-frequency induction melting furnace, and the yield when reused can be extremely high.

( 2 ) 坩堝が一部又は全部が断熱されているため、 酸化物の凝集分離 が進み、 熱効率が向上し、 溶解量が増加する と共に、 溶解時間が短縮さ れる。 このため、 電力原単位は減少しかつ生産性が向上する。 (2) Since the crucible is partly or wholly insulated, coagulation and separation of oxides As the thermal efficiency improves, the amount of dissolution increases, and the dissolution time is shortened. As a result, power consumption decreases and productivity increases.

( 3 ) 一次イ ンゴッ トの組成が均一になるために、 二次イ ンゴッ トの 組成を正確に規定でき、 焼結磁石の品質を良好に維持できる。  (3) Since the composition of the primary ingot is uniform, the composition of the secondary ingot can be accurately specified, and the quality of the sintered magnet can be maintained well.

以下、 上述の成果を達成するために本発明が採用した手段を詳しく説 明する。  Hereinafter, the means adopted by the present invention to achieve the above-described results will be described in detail.

先ず、 本発明の第 1〜第 3方法に共通する事項を説明する。  First, items common to the first to third methods of the present invention will be described.

一般にタングステンアーク溶解炉又は移行型ブラズマアーク溶解炉に よる溶解では、 アーク トーチに対し、 溶解原料を直接対極とするため、 通常、 銅製水冷坩堝を用いたスカル溶解法で行われる。 この方法では、 水冷坩堝の内面に原料自身による凝固層の殻 (スカル) を生じる。 この よ うに、 凝固層が共存した条件下で、 N d F e B系ぁるレ、は S m C o系 磁石のスク ラ ップを通常のアーク溶解炉あるいはプラズマ溶解炉を用い て溶解しょ う とすると、 合金の融点よ り溶湯温度を十分に高める ことが 難しく なる。 そこで溶湯温度を低く保って溶解を行う と、 脱酸精練効果 が不十分となる。 そのために、 得られた 1 次イ ンゴッ トを 2次溶解する ときの歩留が 7 0 %以下と極めて低く なってしま う。  In general, melting by a tungsten arc melting furnace or a transition type plasma arc melting furnace is usually performed by a skull melting method using a copper water-cooled crucible in order to use a melting raw material as a direct counter electrode to an arc torch. In this method, a shell (skull) of a solidified layer is formed on the inner surface of the water-cooled crucible by the raw material itself. As described above, under the condition that the solidified layer coexists, the NdFeB magnet is melted using a normal arc melting furnace or plasma melting furnace to scrap the SmCo magnet. If so, it becomes difficult to sufficiently raise the temperature of the molten metal above the melting point of the alloy. Therefore, if the melting is performed while keeping the temperature of the molten metal low, the deoxidizing scouring effect becomes insufficient. As a result, the yield of secondary melting of the obtained primary ingot is extremely low at 70% or less.

これに対して、 一部もしく は全部を耐火物と した坩堝内に装入された 希土類磁石のスク ラ ップをツイ ン ト一チブラズマ、 タングステンアーク、 移行型プラズマアークで溶解する と、 溶融物を高温にする こ とができ、 その結果スクラ ップ中に存在する希土類酸化物の凝集分離浮上が促進さ れ、 酸素分離精練効果が著しく 高められる こ とを見出した。 この場合、 坩堝の耐火物部分には断熱効果によ り スカルは残らないよ う になり 、 ま た水冷部分のスカルは薄く なり溶湯の温度を融点よ り 2 0 0 °C以上と十 分に高めるこ とが可能になる。 また、 酸化物の分離精練に本質的な溶湯 の対流は、 希土類合金材料では融点と溶融物の温度差が 2 0 0 °C以上で ある と、 活発になることを見出 した。 このよ う に条件を設定する と、 ス クラ ップ中に存在していた酸化物が効率良く分離される。 一般に希土類 磁石合金とその希土類酸化物の比重差は小さ く 、 酸化物の浮上分離は困 難である。 それが、 従来の溶解法では酸素の低減しない理由のひとつで あった。 しかしながら、 断熱構造の坩堝を用い、 かつ、 大容量のェネル ギ一を集中できるプラズマを用いるこ とで高温に保持する と、 融点との 温度差が 2 0 0 °C以上で合金の粘性率は非常に低下する。 このためブラ ズマ加熱による撹拌効果と相俟って、 酸化物の凝集と浮上による分離が 急激に進行するものと考えられる。 On the other hand, when a scrap of a rare-earth magnet placed in a crucible partially or entirely made of refractory is melted by twin-point plasma, tungsten arc, or transfer-type plasma arc, it melts. It has been found that the material can be heated to a high temperature, and as a result, the coagulation separation and floating of the rare earth oxides present in the scrap are promoted, and the oxygen separation scouring effect is significantly enhanced. In this case, the skull does not remain in the refractory part of the crucible due to the heat insulation effect, and the skull in the water-cooled part becomes thin and the temperature of the molten metal becomes more than 200 ° C above the melting point, sufficiently. Can be increased. In addition, it has been found that the convection of the molten metal, which is essential for the separation and refining of oxides, becomes active when the temperature difference between the melting point and the molten material of the rare earth alloy material is 200 ° C or more. By setting conditions in this way, The oxides that existed in the clamp are separated efficiently. In general, the difference in specific gravity between a rare earth magnet alloy and its rare earth oxide is small, and it is difficult to separate the oxide by flotation. That was one of the reasons why the conventional dissolution method did not reduce oxygen. However, if the temperature is kept high by using an insulated crucible and using a plasma that can concentrate a large amount of energy, the viscosity difference of the alloy from the melting point is 200 ° C or more and the viscosity of the alloy becomes Very degraded. Therefore, it is considered that the separation of oxides by agglomeration and flotation progresses rapidly together with the stirring effect of plasma heating.

本発明において、 「断熱」 とは通常水冷坩堝は熱の良導体である金属 から構成されているこ とを前提と し、 これと相反する熱の不良導体を併 用するこ とを指している。 この結果、 この断熱部分にスカルは生じなく なる。 具体的には、 坩堝の溶湯の保持部において全体が銅製等の水冷坩 堝の一部に熱の不良導体を固定して断熱部とするか、 坩堝を水冷金属部 分と熱の不良導体部分とを接合して構成するか、 あるいは坩堝全体を熱 の不良導体で構成する。 熱の不良導体と しては、 耐火物である、 アルミ ナ質、 ジルコニァ質、 イ ッ ト リ ア質、 力ルシア質、 マグネシア質等およ びその複合酸化物の焼成品を挙げることができる。 これらの中でアルミ ナ質耐火物が経済性、 耐久性からも最適である。 なお、 耐火物からメ タ ルへのアルミ ニウムの混入はプラズマアーク等からの入熱を制御し、 溶 融プールの温度が高く なり過ぎないよ うにするこ とで、 問題になる程度 以下に抑制することができる。  In the present invention, “insulation” generally assumes that a water-cooled crucible is made of a metal that is a good conductor of heat, and indicates the use of a contradictory poor conductor of heat. As a result, there is no skull in this heat insulating part. Specifically, a heat-insulated conductor is fixed to a part of a water-cooled crucible made of copper or the like in the molten metal holding part of the crucible to form an adiabatic part, or the crucible is made of a water-cooled metal part and a heat-insulated conductor part. Or the entire crucible is made of a poor conductor of heat. Examples of poor conductors of heat include refractory materials such as alumina, zirconia, yttria, calcite, magnesia and the like and fired products of composite oxides thereof. Of these, alumina refractories are the most economical and durable. The mixing of aluminum from the refractory into the metal is controlled to a level that is not problematic by controlling the heat input from the plasma arc, etc., so that the temperature of the molten pool does not become too high. can do.

また、 水冷坩堝の部分的断熱では、 上記した溶融プールの拡大などの 現象が生じる程度に坩堝の溶湯保持部を断熱する。 断熱領域は坩堝の内 面積に対して 2 0 %以上が好ま しく 、 よ り好ま しく は 3 0 %以上、 一層 好ま しく は 5 0 %以上である。 さ らに、 坩堝の内面積全部を断熱しても よいし、 全体が耐火物性坩堝でもよい。 耐火物性坩堝の場合には、 金属 製容器 (シェル) の内側に耐火物で内張り (ライニング) してもよい。 S このライニングに用いる耐火物は定型耐火物、 不定型耐火物であるかを 問わない。 シェルはジャケ ッ ト水冷しても よレ、。 In the partial heat insulation of the water-cooled crucible, the molten metal holding part of the crucible is insulated to such an extent that a phenomenon such as the expansion of the molten pool occurs. The heat insulation region is preferably at least 20%, more preferably at least 30%, and even more preferably at least 50% of the inner area of the crucible. Further, the entire inner area of the crucible may be insulated, or the whole may be a refractory crucible. In the case of a refractory crucible, it may be lined with a refractory inside a metal container (shell). S The refractories used for this lining may be fixed refractories or irregular refractories. The shell can be jacket-cooled.

上述のよ う に本法は酸素濃度が高い希土類磁石ス ク ラ ップを溶解する と ころに利点があるので、 バ一ジンメ タルを溶解原料に添加することは 得策ではない。 しかし、 磁石製造工場でのスクラ ップ発生量が少なく 、 溶解設備に余力があるよ う な状況では、 バ一ジンメ タルを一部、 好ま し く は 3 0重量%以下、 溶解原料に装入してもよい。 この場合、 バージン メ タルと しては、 工業用純鉄、 電解鉄、 ネオジム等の希土類金属、 ある いはフエロネオジム等の希土類母合金ならびにフエロボロン等を用いる こ とができる。  As described above, this method has the advantage of dissolving rare-earth magnet scraps with a high oxygen concentration, so it is not advisable to add virgin metal to the raw material to be dissolved. However, in a situation where the amount of scrap generated in the magnet manufacturing plant is small and there is room for the melting equipment, part of the virgin metal, preferably 30% by weight or less, is charged to the molten raw material. May be. In this case, as the virgin metal, industrial pure iron, electrolytic iron, rare earth metals such as neodymium, rare earth mother alloys such as ferro neodymium, and ferroboron can be used.

本発明の溶解法において、 溶湯保持時間を長く しても酸化物の凝集分 離は進むが、 温度に比べその寄与は小さ く 、 生産性の観点からは望まし く ないので、 酸化物の凝集分離を促進するためには、 溶湯温度を希土類 磁石スクラ ップの融点の 2 0 0 °C以上、 さ らに望ま しく は 3 0 0 °C以上 の高温に保持することが好ま しい。  In the dissolution method of the present invention, the coagulation separation of oxides proceeds even if the molten metal holding time is prolonged, but its contribution is small compared to the temperature, which is not desirable from the viewpoint of productivity. In order to promote separation, it is preferable to maintain the temperature of the molten metal at a high temperature of 200 ° C. or more, more preferably 300 ° C. or more, which is the melting point of the rare earth magnet scrap.

この方法においても、 坩堝の水冷部分がある場合にはスカルは残るが、 通常の水冷坩堝の場合に比べスカルは薄く 、 底部等の耐火層を配置した 部分にスカルは生じないので、 溶解量を多くするこ とができ る。 出湯後、 残ったスカルの中に次の原料を装入し、 溶解を継続するこ とができる。 このとき、 スカルが次の原料装入までに収縮し、 坩堝との間に間隙を生 じるこ とがある。 スカルと坩堝の導電性が悪いと、 この間でアークを生 じ、 坩堝を局部的に溶損する こ とがあるので、 アノー ド側の坩堝とスカ ルとの導通を確実にするために、 純鉄板等による金属の通電部を具備し た方がよい。  In this method as well, if there is a water-cooled portion of the crucible, the skull remains, but the skull is thinner than in the case of a normal water-cooled crucible, and no skull is generated at the bottom or other portion where the refractory layer is arranged. You can do more. After tapping, the next raw material can be charged into the remaining skull to continue dissolution. At this time, the skull shrinks by the time the next raw material is charged, and a gap may occur between the skull and the crucible. If the conductivity of the skull and the crucible is poor, an arc is generated during this time, and the crucible may be locally melted.Therefore, to ensure conduction between the anode side crucible and the scalp, a pure iron plate It is better to have a metal energizing section made of such as.

溶湯を坩堝からタ ップする場合、 全てを出湯するのでなく 一部のみと し、 溶湯の残部を坩堝内湯に残し、 そこに溶解原料の希土類磁石スクラ ップを追加装入する と、 残湯が追加装入原料塊、 片などの間を満たすの で、 タングステン電極と原料全体の通電を確実なものとするこ とができ る。 それによ り タングステンアークまたは移行型プラズマアークの通電 再スター トが容易となり、 半連続的な溶解を可能と し、 生産性を高める ことができる。 さ らに、 送入物が溶落した後、 原料を適宜追加装入し、 溶湯を坩堝の縁部に設けた、 出湯口 よ りオーバーフローさせるこ とによ り、 坩堝の傾倒を省略して連続的に精鍊を継続するこ と も可能である。 本発明法において、 出湯の際に通電を停止すると、 溶湯表面に酸化物 スラグが覆うので、 この導電性の悪い層のため、 再電通が困難となる。 しかし、 溶湯が完全に固化する前に原料を装入すると、 このスラグ層を 破り原料による通電部ができるため、 引き続き通電ができる。 When tapping the molten metal from the crucible, only the part of the molten metal is removed instead of the whole, leaving the rest of the molten metal in the crucible and adding the rare-earth magnet scrap, which is the raw material to be melted, into the molten metal. Fill the space between the additional charge mass, pieces and so on As a result, it is possible to ensure that the tungsten electrode and the entire raw material are energized. This facilitates the restart of energization of the tungsten arc or the transition type plasma arc, enables semi-continuous melting, and improves productivity. In addition, after the conveyed material has melted down, the raw materials are additionally charged as appropriate, and the molten metal is provided at the edge of the crucible and overflows from the tap hole, so that the tilting of the crucible is omitted. It is also possible to continue refining continuously. In the method of the present invention, when the power supply is stopped at the time of tapping, the surface of the molten metal is covered with the oxide slag. However, if the raw material is charged before the molten metal is completely solidified, the slag layer is broken and a current-carrying part is formed by the raw material, so that current can be continuously supplied.

続いて、 本発明の第 1方法の特長を説明する。  Next, the features of the first method of the present invention will be described.

ツイ ン トーチプラズマは少なく と も陽極と陰極の 1 対の電極よ り構成 されており、 このため坩堝に導電性がある必要はない。 それぞれの トー チは溶解炉チヤンバーの上部から、 トーチ先端が溶解坩堝に向かって挿 入され、 溶解雰囲気を損なう ことはなく 、 挿入角度が可変で、 かつ上下 方向の位置も調整できるよ う に設置されている。 プラズマ トーチの電圧、 電流、 入力は 1バツチ当たり の溶解量と溶解時間に応じて選択範囲を変 える必要がある。 一般的には溶解量が増えるに従い、 溶解時間を短縮す るにつれて、 プラズマ電流、 出力を高める必要がある。 例えば、 1バッ チ当たり 5 0 k g のスク ラ ップを溶解する場合 1 5 0〜 3 0 0 k Wが適 当である。 2 0 0 k gのスク ラ ップを溶解する場合は 4 0 0〜 6 0 0 k Wが適当である。  The twin torch plasma is composed of at least one pair of anode and cathode electrodes, so that the crucible does not need to be conductive. Each torch is inserted from the top of the melting furnace chamber into the melting crucible with the tip of the torch inserted into the melting crucible so that the melting atmosphere is not impaired, the insertion angle is variable, and the vertical position can be adjusted. Have been. The selection range of the voltage, current and input of the plasma torch needs to be changed according to the melting amount per batch and melting time. Generally, it is necessary to increase the plasma current and output as the melting time increases and the melting time decreases. For example, when dissolving 50 kg of scrap per batch, 150 to 300 kW is appropriate. When dissolving 200 kg of scrap, 400 to 600 kW is appropriate.

次に、 本発明の第 2方法の特徴を説明する。  Next, features of the second method of the present invention will be described.

—般にタングステンアーク溶解炉または移行型プラズマアーク溶解炉 による溶解では、 アーク トーチに対し、 溶解原料を直接対極とするため、 通常、 銅製水冷坩堝を用いたスカル溶解法で行われる。 この方法では、 水冷坩堝の内面に原料自身による凝固層の殻 (スカル) を生じ、 その内 側に送入された原料が溶解される。 水冷坩堝の一部を耐火物等で断熱す ると、 溶融プールも広く かつ深く なる。 このために、 容易に溶湯温度を 高くするこ とができる。 よって、 希土類磁石スク ラ ップの溶湯や酸素濃 度の高い坩堝残留物中での対流が促進され、 かつ酸化物が浮上し易く な るので、 酸化物の選択的凝集分離による溶融精練を著しく促進すること ができる。 Generally, melting by a tungsten arc melting furnace or a transition type plasma arc melting furnace is usually performed by a skull melting method using a copper water-cooled crucible in order to make a melting raw material directly opposite an arc torch. In this method, a shell (skull) of a solidified layer is formed by the raw material itself on the inner surface of the water-cooled crucible. The raw material fed into the side is dissolved. If a part of the water-cooled crucible is insulated with refractory, etc., the molten pool will be wide and deep. For this reason, the molten metal temperature can be easily raised. Therefore, convection in the molten metal of the rare-earth magnet scrap or in the crucible residue having a high oxygen concentration is promoted, and the oxides are easily floated. Can be promoted.

引き続いて、 本発明の第 3方法の特長を説明する。  Subsequently, features of the third method of the present invention will be described.

この方法は第 2方法とは別の坩堝構造を採用している。 即ち、 坩堝の 溶湯保持部を耐火物で覆い断熱構造と し、 耐火物を局部的に金属電極 (第 1 の電極) で被覆した構造を選択する。 溶湯保持部の全てを耐火物 で覆う こ とによ り 、 溶湯の温度を上げるこ とがさ らに容易になり 、 溶解 効率、 酸素の分離製鍊効果を高める こ とができる。 この場合、 通電を確 保するため、 金属電極によ り耐火物面を局部的に被覆する。  This method employs a different crucible structure from the second method. In other words, a structure in which the molten metal holding portion of the crucible is covered with a refractory material to form a heat insulating structure, and a structure in which the refractory material is locally covered with a metal electrode (first electrode) is selected. By covering the entire molten metal holding section with the refractory, it is easier to raise the temperature of the molten metal, and the melting efficiency and the effect of separating and producing oxygen can be enhanced. In this case, the refractory surface is locally covered with a metal electrode in order to secure the power supply.

この被覆のためには板状電極を使用するこ とが好ま しい。 板状の金属 性電極を用いる場合、 坩堝底部に一個以上の孔部を設ける と、 溶湯の温 度が上昇し、 酸素の分離が十分進んだ後に、 孔部上およびその周辺の金 属電極が溶解し消失するこ と を利用 して、 溶湯を抜き出す、 すなわち出 湯することが可能となる。 この場合、 出湯のタイ ミ ングは、 溶解時のタ ングステンアークまたは移行型プラズマアークからの入熱を制御するこ とによ り 、 あるいは後述する金属電極の材質、 厚さを選定するこ とによ つても調整するこ とができる。 このよ う に、 底部から溶湯を抜き出す方 式を採用する場合、 所望量の金属溶湯が流出した後、 出湯口をス ト ツバ 一などの塞ぐこ とによ り 、 スラグの金属溶湯中への混入を防止しよ り多 く のスラグが坩堝内に残留するため、 精鍊効果が十分に利いた一次溶解 イ ンゴッ トを得るこ とが可能となる。  It is preferable to use a plate electrode for this coating. When a plate-shaped metal electrode is used, if one or more holes are provided at the bottom of the crucible, the temperature of the molten metal rises, and after sufficient separation of oxygen, the metal electrodes on and around the holes become It is possible to extract the molten metal, that is, to tap the molten metal by utilizing the fact that the molten metal disappears. In this case, the timing of tapping can be controlled by controlling the heat input from the tungsten arc or transitional plasma arc during melting, or by selecting the material and thickness of the metal electrode described later. Can also be adjusted. In this way, when the method of extracting molten metal from the bottom is adopted, after the desired amount of molten metal has flowed out, the outlet of the molten metal is closed with a stud and the like, so that the slag is introduced into the molten metal. Since more slag remains in the crucible than it is prevented from being mixed, it is possible to obtain a primary melting ingot with a sufficient refining effect.

金属電極の材質と しては、 鉄製電極を用いるこ とができる。 特に、 希 土類磁石用原料と して有害な不純物である炭素等の含有量の少ない鉄鋼 材料を用いるこ とによ り 、 これらの元素の汚染を防ぐこ とが可能となる ので、 工業用純鉄製の電極を使用することが望ま しい。 その他、 ニオブ、 モリ ブデン、 タンタル等の高融点金属及びこれらの合金を用いて造られ た電極を用いることができる。 この場合も、 アルミナ製耐火物を用いる 場合のアルミ ニウムの混入を防止するのと同様に、 タ ングステンアーク または移行型プラズマアークからの入熱を制御し、 溶湯プールの温度が 高く なりすぎないよ う にすることで、 これら電極を構成する金属元素の 被溶解物への混入を問題になる程度以下に抑制することができる。 As the material of the metal electrode, an iron electrode can be used. In particular, steel with a low content of carbon, which is a harmful impurity as a raw material for rare earth magnets The use of a material makes it possible to prevent the contamination of these elements, so it is desirable to use an electrode made of industrial pure iron. In addition, an electrode made of a high melting point metal such as niobium, molybdenum, tantalum, or an alloy thereof can be used. In this case as well, the heat input from the tungsten arc or the transition type plasma arc is controlled so that the temperature of the molten metal pool does not become too high in the same way as preventing the incorporation of aluminum when using an alumina refractory. By doing so, the incorporation of the metal elements constituting these electrodes into the substance to be dissolved can be suppressed to a level that is not problematic.

続いて、 本発明に係る一次溶解合金を説明する。 これは、 そのまま二 次溶解炉に装入可能な 1 〜 5 0 k gのイ ンゴッ ト と して溶製されるので、 以下 「一次イ ンゴッ ト」 と称して説明する。 本発明の一次イ ンゴッ トは 酸素濃度がスク ラ ップ状態と比較して著しく低減しており 、 従来の真空 溶解一次イ ンゴッ トよ り も著しく低下している。 この一次イ ンゴッ 卜の 組成を分析し、 バージン原料と合わせ、 目的とする組成となるよ う に配 合を決めて、 通常の真空高周波誘導溶解炉を用いて、 不活性ガス雰囲気 中にて通常の方法で二次溶解し、 铸造し、 磁石用合金とする。  Next, the primary molten alloy according to the present invention will be described. Since this is melted as an ingot of 1 to 50 kg that can be directly charged into the secondary melting furnace, it will be referred to as “primary ingot” below. The primary ingot of the present invention has a significantly lower oxygen concentration than the scrap state, and is significantly lower than the conventional vacuum-melted primary ingot. The composition of this primary ingot is analyzed, combined with the virgin raw material, and the composition is determined so that the desired composition is obtained. Secondary melting and fabrication by the method described in (1) above to obtain a magnet alloy.

一次溶解でメ タル中の酸素量が少なく なっているために、 真空高周波 溶解炉を用いて二次溶解する時には、 メ タル中に残存する未分離酸化物 によるスラグ状のメ タル分が減少し収率の向上に繁げることができる。  Since the amount of oxygen in the metal is reduced by the primary melting, when the secondary melting is performed using a vacuum high-frequency melting furnace, the slag-like metal content due to the unseparated oxide remaining in the metal decreases. It is possible to improve the yield.

この時、 希土類磁石スク ラ ップから得られた一次イ ンゴッ トの添加量 は次の点を考慮して定める必要がある。 これは、 スク ラ ップには、 磁石 の製造工程における磁場中プレス成形時に用いられた潤滑剤に起因して、 炭素濃度も高く なつており 、 また一次溶解中には脱炭はほとんど期待で きないため、 一次イ ンゴッ ト中の炭素量は、 典型的には 0 . 0 4 %以上 と高い。 ちなみに、 バ一ジン原料のみから溶製した磁石用合金の炭素量 は通常 0 . 0 4 %未満であり 、 典型的には 0 . 0 2 %程度である。 この よ うな、 一次イ ンゴッ トの添加量を多く し過ぎる と、 二次溶解イ ンゴッ ト中の炭素量も増加し、 それを原料と して得られる磁石の特性に悪影響 を及ぼす。 この炭素量による制限を考慮する と、 本法で得られた一次ィ ンゴッ トは 5 0重量%以下、 残部はバージン原料の割合と して二次溶解 することができる。 上述のよ うに、 本発明においては、 一次イ ンゴッ ト とバージン原料を 混合して溶解した二次溶解イ ンゴッ トを磁石用合金とする。 一方、 一次 イ ンゴッ トだけで磁石用合金と し、 後の磁石製造時の粉砕混合工程にお いて、 この合金の割合を制限してもよい。 At this time, the amount of primary ingot obtained from the rare earth magnet scrap must be determined in consideration of the following points. This is because scrap has a high carbon concentration due to the lubricant used during magnetic field press forming in the magnet manufacturing process, and decarburization is almost expected during primary melting. Therefore, the carbon content in the primary ingot is typically as high as 0.04% or more. Incidentally, the carbon content of the magnet alloy melted from the virgin material alone is usually less than 0.04%, and typically about 0.02%. If the amount of addition of the primary ingot is too large, the secondary dissolution ingot may be added. The carbon content of the magnet also increases, which adversely affects the properties of the magnet obtained from it. Considering this limitation by the amount of carbon, the primary ingot obtained by the present method can be secondary-dissolved as 50% by weight or less, and the remainder can be a virgin raw material ratio. As described above, in the present invention, the secondary ingot obtained by mixing and melting the primary ingot and the virgin raw material is used as the alloy for the magnet. On the other hand, the primary ingot alone may be used as a magnet alloy, and the ratio of this alloy may be limited in the pulverization and mixing step in the subsequent magnet production.

本発明の一次イ ンゴッ トの組成の内、 1 5〜 4 0 %の希土類元素及び 残部の主成分である F e は、 最も一般的品位のスクラ ップを溶解して得 られる成分範囲を規定したものである。 希土類磁石の製造工程、 特に粉 砕工程あるいは焼結工程で酸素が不純物と して混入するが、 この低減は 上述した本発明の重要な達成成果であるので 0. 1 %以下に限定する。 磁石用合金の成分と しては、 S m— C o系磁石の F e , C u , Z rや、 N d (P r , D yで一部置換されることがある) _ F e — B系磁石の B , A 1 , C o, C u, N bなどがあり、 これらは多寡に拘わらず磁石用合 金の成分と して活用される。 一般には、 S m— C o系磁石では、 C oは 4 0〜 6 0 %、 F eは 1 0〜 2 5 %、 C uは 4〜 : L 0 %, Z r は 4 %以 下であり、 N d— F e — B系磁石では Bは 0. 9〜: I . 2 %、 A 1 は 0. 1〜 1. 5 %である。 さ らに、 焼結磁石の場合は、 磁石用合金粉末成形 工程で炭素が混入するが、 これは上述のよ う に、 ほとんど除去されず不 純物と して一次イ ンゴッ トに残存する。 しかし、 上述のよ う に一次イン ゴッ ト とバージン原料との併用方策を採用すれば、 炭素量は 0. ι %ま で許容できる。  In the composition of the primary ingot of the present invention, 15 to 40% of the rare earth element and Fe as the main component of the balance define the component range obtained by dissolving the most common grade of scrap. It was done. Oxygen is mixed in as impurities in the manufacturing process of the rare-earth magnet, particularly in the pulverization process or the sintering process. However, since this reduction is an important achievement of the present invention, it is limited to 0.1% or less. The components of the alloy for the magnet include Sm—Fe, Cu, Zr, and Nd (which may be partially replaced by Pr, Dy) of the Co-based magnet, _Fe— There are B-based magnets such as B, A1, Co, Cu, and Nb, and these are used as components of magnet alloys regardless of the quantity. In general, for Sm—Co magnets, Co is 40 to 60%, Fe is 10 to 25%, Cu is 4 to: L0%, Zr is 4% or less. Yes, for Nd-Fe-B magnets, B is 0.9 ~: 1.2%, A1 is 0.1 ~ 1.5%. Furthermore, in the case of a sintered magnet, carbon is mixed in the magnet alloy powder forming process, but as described above, this is hardly removed and remains in the primary ingot as an impurity. However, if the combined use of primary ingot and virgin raw material is adopted as described above, the carbon content can be tolerated up to 0.1%.

本発明に係る溶解法では、 上記した各種耐火物からの微量元素、 例え ば A 1 などの他に、 第 3方法において使用する金属電極から F e などの 金属が混入する。 この F e は磁石用合金の必要成分となる。 A 1 は S m 一 C o系磁石では磁気特性に有害な元素であり、 一方 N d — F e 一 B系 磁石では合金元素と して少量は許容されるが、 多すぎると磁気特性に有 害である。 そのためその量は 1 %以下であることが好ましレ、。 図面の簡単な説明 In the melting method according to the present invention, a metal such as Fe is mixed from the metal electrode used in the third method, in addition to the trace elements from the various refractories described above, for example, A1 and the like. This Fe is a necessary component of the magnet alloy. A 1 is S m A Co-based magnet is a harmful element for magnetic properties, while a Nd-Fe-B magnet is acceptable as a small alloy element, but too much is harmful to magnetic properties. Therefore, its amount is preferably less than 1%. BRIEF DESCRIPTION OF THE FIGURES

第 1 図は本発明の第 1 , 第 2方法を実施するための水冷銅坩堝の一実 施例を示す断面図である。  FIG. 1 is a sectional view showing one embodiment of a water-cooled copper crucible for carrying out the first and second methods of the present invention.

第 2図は、 本発明の第 1方法を実施するための耐火物製坩堝の一実施 例を示す断面図である。  FIG. 2 is a sectional view showing one embodiment of a refractory crucible for carrying out the first method of the present invention.

第 3図は、 ツイ ン トーチプラズマアーク溶解炉を使用する本発明の第 1 溶解装置の一実施例を示す図である。 FIG. 3 is a diagram showing an embodiment of the first melting apparatus of the present invention using a twin torch plasma arc melting furnace.

第 4図は、 移行型プラズマアーク溶解炉を使用する本発明の第 2およ び第 3に係る溶解装置の一実施例を示す図である。  FIG. 4 is a view showing one embodiment of the melting apparatus according to the second and third aspects of the present invention using a transfer type plasma arc melting furnace.

第 5図は本発明の第 2方法を実施するための通電部を具備した水冷銅 坩堝の一実施例を示す斜視図である。  FIG. 5 is a perspective view showing one embodiment of a water-cooled copper crucible provided with a current-carrying part for carrying out the second method of the present invention.

第 6図は本発明の第 3方法を実施するための耐火物製坩堝の一実施例 を示す図面である。  FIG. 6 is a drawing showing one embodiment of a refractory crucible for carrying out the third method of the present invention.

第 7図は本発明の第 3方法を実施するための耐火物製坩堝の別の一実 施例を示す図面である。  FIG. 7 is a drawing showing another embodiment of a refractory crucible for carrying out the third method of the present invention.

第 8図は本発明の第 3方法を実施するための耐火物製坩堝のさ らに別 の一実施例を示す図面である。 発明の実施態様の説明  FIG. 8 is a drawing showing still another embodiment of the refractory crucible for carrying out the third method of the present invention. Description of embodiments of the invention

以下、 図面を参照して本発明法を実施する溶解装置の実施態様を説明 する。  Hereinafter, an embodiment of a melting apparatus for carrying out the method of the present invention will be described with reference to the drawings.

第 1 図は本発明法を実施するための全体が銅製の水冷構造を呈する坩 堝を示す。 図において、 1 は銅製坩堝、 2 は耐火物板、 3は原料、 4は冷却水入 口、 5 は冷却水流路、 6 は冷却水出口である。 図示のよ う に、 耐火物板 2 を坩堝 1 の底部にのみ使用 し、 側壁は水冷銅坩堝のまま とすることに よ り、 プラズマによる入熱と耐火物板 2による断熱のバランスをとつて、 溶融プールを深くするこ とができる。 又、 底部のみを断熱する と高価な 耐火物の使用量を少なくするこ とが可能となり、 耐火物の形状が単純で あり 、 耐久性にも優れ、 かつ、 安価なため、 経済性にも優れた溶解方法 となる。 FIG. 1 shows a crucible having a water-cooled structure made entirely of copper for carrying out the method of the present invention. In the figure, 1 is a copper crucible, 2 is a refractory plate, 3 is a raw material, 4 is a cooling water inlet, 5 is a cooling water passage, and 6 is a cooling water outlet. As shown in the figure, by using the refractory plate 2 only at the bottom of the crucible 1 and leaving the side wall of the water-cooled copper crucible, the heat input by plasma and the insulation by the refractory plate 2 are balanced. However, the molten pool can be deepened. Also, if only the bottom is insulated, it is possible to reduce the amount of expensive refractory used, the shape of the refractory is simple, the durability is excellent, and the cost is excellent because it is inexpensive. Dissolution method.

第 2図は本発明法を実施するための耐火物製坩堝を示す。 こ こでは金 属容器に耐火物製坩堝を納めており 、 図中、 7はアルミナ坩堝、 9は鉄 製容器である。 坩堝と容器の間隙にはアルミナ粉末 8 を充填している。 第 3図にはツイ ン トーチプラズマ溶解炉の一実施例を示す。 図中、 1 0はプラズマ トーチであり 、 これによ り陽極 トーチ 1 0 a と陰極 トーチ 1 O b の間にプラズマ 1 1 を発生する。  FIG. 2 shows a refractory crucible for carrying out the method of the present invention. Here, a refractory crucible is placed in a metal container. In the figure, 7 is an alumina crucible, and 9 is an iron container. The gap between the crucible and the container is filled with alumina powder 8. FIG. 3 shows an embodiment of a twin torch plasma melting furnace. In the figure, reference numeral 10 denotes a plasma torch, which generates plasma 11 between the anode torch 10a and the cathode torch 10Ob.

第 4図には移行型プラズマアーク溶解炉を示す。 図中 1 5 はプラズマ トーチであり、 これによ り トーチと銅製坩堝 1 内に装入された原料の間 にプラズマアークを発生させる。 タングステンアーク溶解炉は、 このプ ラズマ トーチ 1 5に替えてタングステン電極を具備した構造であり、 こ の電極と原料間にアークを発生する。 なお 1 6は原料装入管である。  Fig. 4 shows the transfer type plasma arc melting furnace. In the figure, reference numeral 15 denotes a plasma torch, which generates a plasma arc between the torch and the raw material charged in the copper crucible 1. The tungsten arc melting furnace has a structure provided with a tungsten electrode in place of the plasma torch 15 and generates an arc between the electrode and the raw material. 16 is a raw material charging pipe.

第 5図には通電部 1 7 を設けた坩堝を示す。 通電部 1 7は鉄板などを 坩堝内面形状に倣って曲げたものを水冷銅坩堝の内壁に接するよ う に配 置したものである。 本法による溶解 · 出湯後に残ったスカル内側に次の 希土類磁石スクラ ップを装入して溶解することができる。  FIG. 5 shows a crucible provided with a current-carrying part 17. The current-carrying part 17 is formed by bending an iron plate or the like in accordance with the inner shape of the crucible so as to be in contact with the inner wall of the water-cooled copper crucible. Melting by this method · The following rare earth magnet scrap can be charged and melted inside the skull left after tapping.

このと き残ったスカルの収縮によ り坩堝の間に間隙が生じ、 これが原 因になって導電性が悪化しそ して坩堝が溶損するこ と もあるので、 これ を防止するためにァノ一ド側の坩堝と スカルの導通を確実にする通電部 1 7 を設けるこ とが好ま しい。 なお、 第 5 図では、 3本のプラズマ ト一 チによるプラズマアーク炉で使用される坩堝が示されており 、 それぞれ 2本の トーチ間に通電部が配置されるよ う に 3個の通電部が設けられて いる。 このよ う に トーチに対応して通電部 1 7を設ける と、 さ らにスカ ル部を小さく 断熱部を大き く取るこ とができ、 安全性を向上させて、 な お溶解量を増やすこ とができる。 この通電部用の金属はスカル中で一部 溶けるが、 通電は確保されるため、 スカルを取り除かないで継続して溶 解を続ける限り は、 取り替える必要はない。 At this time, a gap is formed between the crucibles due to the shrinkage of the remaining skull, which causes the conductivity to deteriorate and the crucible to be melted. It is preferable to provide an energizing section 17 for ensuring conduction between the crucible on one side and the skull. In Fig. 5, three plasma transistors are used. 1 shows a crucible used in a plasma arc furnace with three conductors, and three conducting parts are provided so that the conducting parts are arranged between two torches, respectively. By providing the energizing section 17 corresponding to the torch in this way, the scalar section can be made smaller and the heat insulation section can be made larger, improving safety and increasing the amount of melting. Can be. Although the metal for the current-carrying part is partially melted in the skull, it does not need to be replaced as long as the skull is not removed and the melting is continued without interruption.

本発明の第 3方法の実施形態を示す第 6 図において、 金属電極 2 0は 例えば坩堝底部を覆う板状電極であり 、 坩堝を底部 2 1 と側壁部 2 2に 上下方向に分離し、 板状電極 2 0を底部 2 1 と側壁部 2 2で挟み、 電極 2 0の外周部から電源への通電を確保するよ うな構造とする。 あるいは、 坩堝底部に穴を設け、 そこに棒状の電極を差し込み、 通電を確保するこ と も可能である。 このよ うな坩堝構造とする場合、 希土類磁石のスクラ ップを溶解後は、 坩堝を傾倒し出湯する。 また、 第 8図に示すよ うに、 坩堝底部 2 1 に出湯口 2 5を設けた坩堝構造とすること もできる。 発明を実施するための最良の形態  In FIG. 6 showing an embodiment of the third method of the present invention, the metal electrode 20 is, for example, a plate-like electrode covering the bottom of the crucible, and the crucible is vertically separated into a bottom 21 and a side wall 22. The electrode 20 is sandwiched between the bottom 21 and the side wall 22 so as to ensure that power is supplied from the outer periphery of the electrode 20 to the power supply. Alternatively, it is also possible to provide a hole at the bottom of the crucible and insert a rod-shaped electrode into the hole to ensure current supply. In the case of such a crucible structure, after the rare earth magnet scrap is melted, the crucible is tilted and heated. Further, as shown in FIG. 8, a crucible structure in which a tap hole 25 is provided at the bottom 21 of the crucible may be employed. BEST MODE FOR CARRYING OUT THE INVENTION

実施例 1 (第 1発明の実施例) Example 1 (Example of the first invention)

N d F e B系磁石のス ク ラ ップ (分析値 : N d + P r — 2 9 . 0 w t % , D y - 2 . 5 w t % , A 1 - 0 . 3 2 w t % , B — 1 . 0 3 w t % , O — 0 . 6 6 w t % , C — 0 . 0 4 w t %、 F e残) を原料と し て、 底部を焼結アルミ ナ板で断熱した水冷銅坩堝 (第 1 図) を配置し 5 O k Wのツイ ン ト一チプラズマアーク溶解炉 (第 2図) を用いて、 アル ゴンガスをプラズマ化して溶解し、 一次イ ンゴッ トを得た。  Scrap of NdFeB magnet (analytical value: Nd + Pr-29. 0 wt%, Dy-2.5 wt%, A1-0.332 wt%, B — 1.03 wt%, O — 0.66 wt%, C — 0.04 wt%, Fe remaining) as raw materials and a water-cooled copper crucible (bottom) insulated with a sintered aluminum plate. Argon gas was turned into plasma and melted using a 5 O kW twin-chip plasma arc melting furnace (Fig. 2) to obtain a primary ingot.

一次イ ンゴッ トの分析値 : N d + P r — 2 5 . 2 w t % , D y — 2 . 1 w t % , A 1 - 0 . 3 4 w t % , B — 1 . 0 0 w t % , O — 0 . 0 1 8 w t % , C - 0 . 0 4 w t %、 F e残であった。 ノくツチ毎の溶解量は 1 . 5 k gであり 、 この合金の融点は 1 2 0 0〜 1 2 5 0 °Cであるこ と力 ら、 溶融温度はこれよ り 3 0 0 °C以上高い 1 5 5 0でと した。 坩堝 1 は、 内径 1 7 0 mm、 深さ 7 0 mmであり 、 その 底部に厚さが 2 O mmのアルミナ焼結板 2 を配置した。 Analytical value of primary ingot: Nd + Pr-25. 2 wt%, Dy-2.1 wt%, A1-0.34 wt%, B-1.00 wt%, O — 0.018 wt%, C-0.04 wt%, Fe remaining. The melting amount of each knuckle is 1.5 kg, and the melting point of this alloy is 1200 to 125 ° C, so the melting temperature is more than 300 ° C higher than this. We decided at 1550. The crucible 1 had an inner diameter of 170 mm and a depth of 70 mm, and an alumina sintered plate 2 having a thickness of 2 Omm was disposed at the bottom.

なお、 一次溶解収率は、 製品重量を装入原料重量で除して計算した。 このツイ ン トーチプラズマアーク溶解炉における溶解時間は 1 3分であ り、 一次ィンゴッ トの溶解電力は 2. 8 k Wh Z k gであった。 坩堝底 部が断熱されているため、 溶解時間は短く 、 溶解電力も小さい。  The primary dissolution yield was calculated by dividing the product weight by the charged raw material weight. The melting time in this twin torch plasma arc melting furnace was 13 minutes, and the melting power of the primary ingot was 2.8 kWh Zkg. Since the crucible bottom is insulated, the melting time is short and the melting power is small.

得られた合金を原料と して、 真空高周波誘導溶解炉を用いてアルゴン ガス雰囲気中で溶解した。 このとき、 通常はバージン原料に一次イ ンゴ ッ トを添加し磁石合金組成とするが、 こ こでは収率を調べるために、 全 量を一次ィンゴッ トだけで溶解した。 得られた一次ィンゴッ トの溶解収 率および二次溶解の溶解収率、 ならびに一次イ ンゴッ 卜の平均酸素分析 値を表 1 に示した。  The obtained alloy was used as a raw material and melted in an argon gas atmosphere using a vacuum high-frequency induction melting furnace. At this time, the primary ingot is usually added to the virgin raw material to make the magnet alloy composition, but in order to investigate the yield, the entire amount was melted with the primary ingot alone. Table 1 shows the dissolution yield of the obtained primary ingot, the dissolution yield of the secondary dissolution, and the average oxygen analysis value of the primary ingot.

表 1 に示すよ うに、 スクラ ップをツイ ン トーチプラズマアーク溶解す ることで、 酸素濃度が著しく低減した一次ィ ンゴッ トを高周波誘導溶解 すると、 スラグ発生量が少なく 、 かつ、 バージン原料のみを用いて溶解 したときの平均収率である 9 5 %に近い二次溶解収率が得られた。  As shown in Table 1, by melting the scrap by twin torch plasma arc melting the primary ingot with a significantly reduced oxygen concentration by high frequency induction melting, the amount of slag generated is small and only the virgin raw material is used. A secondary dissolution yield close to 95%, which is the average yield when dissolving in water, was obtained.

実施例 2 (第 2発明の実施例) Example 2 (Example of the second invention)

実施例 1 で使用した N d F e B系磁石のスクラ ップを原料と して、 ァ ルミナ坩堝 (第 2図) を配置し、 実施例 1 と同じく 5 0 k Wのッイ ン ト ーチプラズマアーク炉で溶解し、 一次イ ンゴッ トを得た。 一次イ ンゴッ 卜の分析値 : N d + P r — 2 5. 0 w t % , D y — 2. 2 w t % , A 1 - 0. 3 8 w t % , B - 0. 9 9 w t % , O— 0. 0 1 9 w t % , C - 0. ◦ 4 w t %、 F e残であった。 バッチの溶解量は 1 . 5 k g , 溶融 温度は 1 5 5 0 °Cで、 いずれも実施例 1 と同じである。 アルミ ナ坩堝 7 は、 内径 1 7 0 mm, 深さ 7 0 mm, 厚さ 3 0 mmを配置した。 この溶 解時間は 1 2分であり 、 一次イ ンゴッ 卜 の溶解電力は 2 . 6 k W h k gであった。 実施例 1 と同様に、 溶解時間は短くかつ溶解電力も小さレ、。 このときの溶解収率と平均酸素濃度を表 1 に示した。 これらの値も実施 例 1 と同様であり 、 高収率で酸素濃度が著しく低減したイ ンゴッ トを得 ることができた。 A scrap of the NdFeB magnet used in Example 1 was used as a raw material, and an alumina crucible (FIG. 2) was arranged. It was melted in a chi-plasma arc furnace to obtain a primary ingot. Analytical value of primary ingot: N d + P r — 25.0 wt%, D y — 2.2 wt%, A 1-0.38 wt%, B-0.99 wt%, O — 0.019 wt%, C-0. ◦ 4 wt%, Fe remaining. The dissolution amount of the batch was 1.5 kg, and the melting temperature was 1550 ° C. The aluminum crucible 7 has an inner diameter of 170 mm, a depth of 70 mm, and a thickness of 30 mm. This solution The solution time was 12 minutes and the dissolution power of the primary ingot was 2.6 kWhkg. As in Example 1, the dissolution time was short and the dissolution power was low. Table 1 shows the dissolution yield and average oxygen concentration at this time. These values were also the same as in Example 1, and an ingot with a high yield and a remarkably reduced oxygen concentration could be obtained.

比較例 1  Comparative Example 1

実施例 1 で使用した N d F e B系磁石のスクラップとバージン原料を、 1 5 k Wの真空高周波誘導溶解炉を用いて溶解した。 溶解量は 5 k gで、 スクラ ップのバージン原料に対する添加量は 5 0 %と した。 得られた一 次イ ンゴッ ト の溶解収率および平均酸素分析値を表 1 に示した。 なお、 溶解収率は、 バージン原料の溶解収率をバージン原料のみで溶解した時 の平均収率である 9 5 %と仮定し、 全体の収率に合わせるよ うにスク ラ ップのみの溶解の収率を計算で求め、 その値を示した。  The NdFeB-based magnet scrap and virgin raw material used in Example 1 were melted using a 15 kW vacuum high-frequency induction melting furnace. The amount of dissolution was 5 kg, and the amount of scrap added to the virgin material was 50%. Table 1 shows the dissolution yield and average oxygen analysis value of the obtained primary ingot. The dissolution yield is assumed to be 95%, which is the average yield when dissolving the virgin raw material using only the virgin raw material, and the dissolving yield of only the scrap is adjusted to match the overall yield. The yield was calculated and the value was given.

スク ラ ップの再利用の方法と して、 バージン原料と共に、 直接、 高周 波誘導炉で溶解し磁石用合金を得よ う と した場合、 スラグ発生量が多く 、 操業が困難で、 収率も低く 、 かつ、 得られた合金の組成も安定しなかつ た。  As a method of recycling the scrap, if the virgin raw material is melted directly in a high frequency induction furnace to obtain an alloy for magnets, a large amount of slag is generated, and the operation is difficult. Rate was low, and the composition of the obtained alloy was not stable.

比較例 2 Comparative Example 2

実施例 1 で使用した N d F e B系磁石のスクラップを原料と して、 1 5 k Wの真空高周波誘導溶解炉を用いて 5 k gを溶解し、 一次イ ンゴッ トを得た。 一次イ ンゴッ トの分析値 : N d + P r — 2 5 . 0 w t % , D y - 2 . 3 w t % , A 1 - 0 . 3 5 w t % , B— 1 . 0 1 w t % , O - 0 . 0 2 0 w t % , C - 0 . 0 4 w t %、 F e残であった。  Using the scrap of the NdFeB-based magnet used in Example 1 as a raw material, 5 kg was melted using a 15 kW vacuum high-frequency induction melting furnace to obtain a primary ingot. Analytical value of primary ingot: Nd + Pr-25.0 wt%, Dy-2.3 wt%, A1-0.35 wt%, B-1.01 wt%, O -0.020 wt%, C-0.04 wt%, Fe remaining.

実施例 1 と同じく 、 この一次イ ンゴッ トを再度、 真空高周波誘導溶解 炉を用いて溶解した。 実施例 1 と同様に、 溶解収率と平均酸素分析値を 求めそれらを表 1 、 2に示した。 比較例 3 As in Example 1, this primary ingot was melted again using a vacuum high-frequency induction melting furnace. As in Example 1, the dissolution yield and average oxygen analysis value were determined and are shown in Tables 1 and 2. Comparative Example 3

実施例 1 で使用した N d F e B系磁石のスク ラ ップ原料をと して、 全く 断熱をしない水冷銅坩堝を用いた 5 0 k Wのツイ ン トーチプラズ マアーク溶解炉を用いて 1 . 5 k g を溶解し、 一次ィンゴッ トを得た。 一次イ ンゴッ トの分析値 : N d + P r — 2 8 . 0 w t % , D y - 2 . 4 w t % , A 1 - 0 . 3 2 w t % , B - 1 . 0 2 w t % , O— 0 . 4 2 w t % , C - 0 . 0 4 w t %、 F e残であった。 この装置では融点 が 1 2 0 0〜 1 2 5 0 °Cのスクラ ップを溶解することはできるが、 坩 堝が断熱されていないので、 溶融温度を十分上げるこ とはできず 1 3 0 0 °C止ま り であった。 スカルも厚く 、 装入した原料の半分程度がス カルと して坩堝内に残った。 このプラズマアーク溶解炉における溶解 時間は 2 2分であり、 一次イ ンゴッ トに対する溶解電力は 1 3 k W h / k gであった。 実施例 1 と 同 じ く 、 こ の一次イ ン ゴッ ト を真空高周波誘導溶解 炉を用いて溶解した。 実施例 と 同様に、 溶解収率と平均酸素分析 値を求めそれらを表 1 に示 した。  The scrap material of the NdFeB magnet used in Example 1 was used as a raw material in a 50 kW twin torch plasma arc melting furnace using a water-cooled copper crucible without any heat insulation. 5 kg was dissolved to obtain a primary ingot. Analytical value of primary ingot: Nd + Pr—28.0 wt%, Dy-2.4 wt%, A1-0.322 wt%, B-1.02 wt%, O — 0.42 wt%, C-0.04 wt%, Fe remaining. This device can melt scrap with a melting point of 1200 to 125 ° C, but the melting temperature cannot be raised sufficiently because the crucible is not insulated. It stopped at 0 ° C. The skull was also thick, and about half of the charged raw material remained in the crucible as a skull. The melting time in this plasma arc melting furnace was 22 minutes, and the melting power for the primary ingot was 13 kWh / kg. As in the case of Example 1, this primary ingot was melted using a vacuum high-frequency induction melting furnace. In the same manner as in the examples, the dissolution yield and the average oxygen analysis value were determined and are shown in Table 1.

表 1 に示すよ うに、 一次イ ンゴッ ト中の酸素分析値が非常に高く 、 脱酸効果は不十分である。 スクラ ップを通常の水冷坩堝坩堝を具備し たプラズマアーク炉溶解した場合、 断熱されていないため、 溶解には 至っても高温に保持されないので、 酸化物の分離が不十分で、 一次ィ ンゴッ ト中の酸素濃度は高いままである こ とが明らかである。 このた め、 高周波誘導炉における二次溶解において収率は低く 、 スクラップ をそのまま溶解した時と同程度であった。 イ ンゴッ ト の溶解収率、 酸素分析値 As shown in Table 1, the oxygen analysis value in the primary ingot is very high, and the deoxidizing effect is insufficient. When the scrap is melted in a plasma arc furnace equipped with a normal water-cooled crucible crucible, it is not insulated, and is not kept at a high temperature even if it is melted. It is clear that the oxygen concentration inside remains high. For this reason, the yield in the secondary melting in the high frequency induction furnace was low, and was about the same as when scrap was melted as it was. Ingot dissolution yield, oxygen analysis

Figure imgf000021_0001
Figure imgf000021_0001

実施例 3 (第 2発明の実施例) Example 3 (Example of the second invention)

実施例 1で使用した N d F e B系磁石のスクラ ップ (分析値 : N d + P r — 2 9. 0 w t % , D y— 2. 5 w t % , A 1 - 0. 3 2 w t % B— 1 . 0 3 w t % , O - 0. 6 6 w t % , C— 0. 0 4 w t % ) 6 k gを原料と して、 底部を焼結アルミナ板で断熱した水冷銅坩堝 (第 1図) を配置した 3 0 k Wのタングステンアーク溶解炉を用いて、 ァ ルゴンガス雰囲気中で溶解し、 一次イ ンゴッ トを得た。 一次イ ンゴッ 卜の分析値 : N d + P r — 2 5. 1 w t % , D y - 2. 2 w t % , A 1 — 0. 3 2 w t % , B— 1 . 0 2 w t % , O— 0. 0 1 8 w t % , C - 0. 0 4 w t %、 F e残であった。  Scrap of the NdFeB magnet used in Example 1 (analytical value: Nd + Pr—29.0 wt%, Dy—2.5 wt%, A1-0.32) wt% B—1.03 wt%, O-0.66 wt%, C—0.04 wt%) Water-cooled copper crucible (6 kg) with the bottom insulated by a sintered alumina plate ( Using a 30 kW tungsten arc melting furnace equipped with (Fig. 1), it was melted in an argon gas atmosphere to obtain a primary ingot. Analytical value of primary ingot: Nd + Pr-25.1 wt%, Dy-2.2 wt%, A1-0.32 wt%, B-1.02 wt%, O — 0.018 wt%, C-0.04 wt%, Fe remaining.

バッチ毎の溶解量は 1. 5 k gであり 、 この合金の融点は 1 3 0 0 °C であること力ゝら、 溶融温度はこれよ り 3 0 0 °C高い 1 6 0 0 °Cと した。 坩堝 1 は、 内容積が直径 1 1 O m m、 深さ 7 0 m mであり 、 その底部 に厚さが 2 0 m mのアルミナ焼結板 2 を配置した。 The melting amount per batch is 1.5 kg and the melting point of this alloy is 1300 ° C Therefore, the melting temperature was set to 160 ° C., which is higher by 300 ° C. than this. The crucible 1 had an inner volume of 11 O mm in diameter and a depth of 70 mm, and an alumina sintered plate 2 having a thickness of 20 mm was arranged on the bottom thereof.

このアーク溶解炉における溶解時間は 1 1分であり 、 一次イ ンゴッ 卜の溶解電力は 1 . 5 k W hノ k gであった。 底部が断熱されている ため、 溶解時間は短く 、 溶解電力も小さい。  The melting time in this arc melting furnace was 11 minutes, and the melting power of the primary ingot was 1.5 kWh / kg. Because the bottom is insulated, the melting time is short and the melting power is small.

得られた合金を原料と して、 真空高周波誘導溶解炉を用いてァルゴ ンガス雰囲気中で溶解した。 このとき、 通常はバージン原料に一次ィ ンゴッ トを添加し磁石合金組成とするが、 こ こでは収率を調べるため に、 全量を一次イ ンゴッ トだけで溶解した。 得られた一次イ ンゴッ ト の溶解収率および二次溶解の溶解収率、 ならびに一次ィ ンゴッ トの平 均酸素分析値を表 2に示した。  The obtained alloy was used as a raw material and melted in an argon gas atmosphere using a vacuum high-frequency induction melting furnace. At this time, the primary ingot is usually added to the virgin raw material to make the composition of the magnet alloy, but in order to investigate the yield, the entire amount was melted with the primary ingot alone. Table 2 shows the dissolution yield of the obtained primary ingot, the dissolution yield of the secondary dissolution, and the average oxygen analysis value of the primary ingot.

表 2に示すよ うに、 スクラ ップを高温アーク溶解することで、 酸素 濃度が著しく低減した一次イ ンゴッ トを高周波誘導溶解すると、 スラ グ発生量が少なく 、 かつ、 バージン原料のみを用いて溶解したときの 平均収率である 9 5 %に近い二次溶解収率が得られた。  As shown in Table 2, high-frequency induction melting of the primary ingot, whose oxygen concentration was significantly reduced by high-temperature arc melting of the scrap, reduced the amount of slag generated and melted using only virgin material. A secondary dissolution yield close to 95%, which is the average yield when performing this, was obtained.

実施例 4 (第 2発明の実施例) Example 4 (Example of the second invention)

実施例 3で使用した坩堝 (第 1 図) に代えて図 5に示した、 水冷銅 坩堝内壁に接して純鉄板 (厚さ 1 m m X幅 1 5 m m , 3枚) による通 電部を設けた坩堝を用いて、 実施例 1 で使用した N d F e B系磁石の スクラ ップの溶解を行ったと ころ、 次の分析値の一次インゴッ トが得 られた。 N d + P r — 2 6 . 0 w t % , D y - 2 . 4 w t % , A 1 - 0 . 3 3 w t % , B - 1 . 0 0 w t % , O— 0 . 0 1 6 w t % , C - 0 . 0 4 w t %、 F e残であった。 なお、 坩堝の溶損は 3 0回以上繰 り返し溶解しても全く無かった。  Instead of the crucible used in Example 3 (Fig. 1), a conductive part made of a pure iron plate (thickness 1 mm x width 15 mm, 3 pieces) was provided in contact with the inner wall of the water-cooled copper crucible shown in Fig. 5 When the scrap of the NdFeB-based magnet used in Example 1 was melted using the crucible, a primary ingot of the following analysis value was obtained. N d + Pr-26.0 wt%, Dy-2.4 wt%, A 1-0.33 wt%, B-1.0 0 0 wt%, O-0.0 16 wt% , C-0.04 wt%, Fe remaining. In addition, there was no melting of the crucible even if it was melted repeatedly 30 times or more.

このよ うに通電部を設けた場合、 被溶解物と水冷坩堝の間のアーク 発生が最少限に抑えられるため、 繰り返し溶解を行っても坩堝は溶損 しにく く 、 耐久性を飛躍的に向上することができた。 純鉄板はスカル とは一部で溶着はするものの、 スカル側に残るので、 一次イ ンゴッ ト への溶け込みによる組成変動への影響は無視できるレベルであった。 実施例 5 (第 2発明の実施例) When the current-carrying part is provided in this manner, arcing between the material to be melted and the water-cooled crucible is minimized, so that the crucible is not easily melted even after repeated melting, and the durability is dramatically improved. Could be improved. Pure iron plate is partially welded to the skull, but remains on the skull side, so the primary ingot The effect on the composition fluctuation due to the penetration into the steel was negligible. Example 5 (Example of the second invention)

実施例 1 で使用した N d F e B系磁石と同じスクラ ップ 5 k g を原 料と して、 底部を焼結アルミナ板で断熱した第 1 図に示す水冷銅坩堝 を用いたプラズマアーク溶解炉を用いて、 アルゴンガス雰囲気中で溶 解し、 一次ィンゴッ トを得た。 溶融温度は実施例と同じ 1 6 0 0。じと した。 一次イ ンゴッ トの分析値は N d + P r — 2 4. 8 w t % , D y — 2. 1 w t % , A 1 - 0. 3 5 w t % , B - 0. 9 8 w t % , O - 0. 0 1 8 w t % , C - 0. 0 4 w t %、 F e残であった。  Plasma arc melting using a water-cooled copper crucible shown in Fig. 1 in which the same 5 kg scrap as the NdFeB magnet used in Example 1 was used as a raw material and the bottom was insulated with a sintered alumina plate. Using a furnace, melting was performed in an argon gas atmosphere to obtain a primary ingot. The melting temperature was the same as in the example, 160. I did. The analysis value of the primary ingot was Nd + Pr-24.8 wt%, Dy-2.1 wt%, A1-0.35 wt%, B-0.98 wt%, O -0.018 wt%, C-0.04 wt%, Fe remaining.

さ らに、 実施例 3 と同じ方法で、 この一次イ ンゴッ トを用いて磁石 合金を溶解铸造した。 実施例 1 と同様に、 溶解収率を求め、 一次イ ン ゴッ トの平均酸素分析値を測定し、 これらを表 2に示した。 表 2に示 すよ うに、 プラズマアーク溶解炉においても、 スクラ ップを高温溶解 することで、 実施例 3 と同じく 、 酸素濃度の著しい低減と高い二次溶 解収率が得られた。  Further, in the same manner as in Example 3, a magnetic alloy was melt-formed using this primary ingot. In the same manner as in Example 1, the dissolution yield was determined, and the average oxygen analysis value of the primary ingot was measured. As shown in Table 2, also in the plasma arc melting furnace, remarkably reducing the oxygen concentration and a high secondary melting yield were obtained as in Example 3 by melting the scrap at a high temperature.

実施例 6 (第 2発明の実施例) Example 6 (Example of the second invention)

S m C o系磁石合金の原料を、 真空高周波誘導溶解炉で溶解後、 坩 堝内に残留した残留物 ( S m— 3 1 . 6 w t % , F e - 4. 6 w t % , Z r — 2. 0 w t % , O— 2. 8 w t %、 C o残) を、 底部を焼結ァ ルミナ板で断熱した水冷銅坩堝 (図 1 ) を配置した 3 0 k Wのタンダ ステンアーク溶解炉を用いて、 アルゴンガス雰囲気中で溶解すること で、 メ タル分を回収することができた。 溶解量は 1. 5 k gで、 得ら れた一次ィンゴッ トの溶解収率は 7 5 %であり、 組成分析値は S m— 1 5. 0 w t % , F e — 2 8. 0 w t % , C u— 4. 6 w t %、 Z r 2. 5 w t % , O— 0. 0 2 1 w t %, C o残であった。 この結果か ら分かるよ うに、 S m C o系磁石合金の製造における高周波誘導炉坩 堝内の高酸素濃度残留物も、 高温アーク溶解することで、 著しく酸素 が低減し、 C oのみならず S mや Z r などの高価な金属分を、 再使用 可能なメ タルと して、 高い収率で回収するこ とができた。 実施例 7 (第 2発明の実施例) After the raw material of the SmCo-based magnet alloy is melted in a vacuum high-frequency induction melting furnace, the residue remaining in the crucible (Sm—31.6 wt%, Fe-4.6 wt%, Zr — 2.0 wt%, O—2.8 wt%, Co remaining) and a 30 kW tungsten-arc melting furnace with a water-cooled copper crucible (Figure 1) insulated with a sintered aluminum plate at the bottom Metals could be recovered by melting in an argon gas atmosphere using a furnace. The dissolution amount is 1.5 kg, the dissolution yield of the obtained primary ingot is 75%, and the composition analysis value is Sm-15.0 wt%, Fe-28.0 wt% , Cu—4.6 wt%, Zr 2.5 wt%, O—0.021 wt%, Co remaining. As can be seen from the results, the high oxygen concentration residue in the high-frequency induction furnace crucible in the production of SmCo-based magnetic alloys is also significantly reduced in oxygen by high-temperature arc melting. Expensive metals such as Sm and Zr could be recovered in high yield as reusable metal. Example 7 (Example of the second invention)

実施例 3で使用した N d F e B系磁石のスクラ ップに、 酸化の著し い N dメ タルを含むバージン原料を 1 0 %加え、 実施例 3 と同じ方法 で一次ィンゴッ トを得た。 このイ ンゴッ トの酸素分析値は実施例 1 と 有意差がない程度に十分低下した。  To the scrap of the NdFeB magnet used in Example 3, 10% of a virgin material containing Nd metal, which is significantly oxidized, was added, and a primary ingot was obtained in the same manner as in Example 3. Was. The oxygen analysis value of this ingot was sufficiently reduced to no significant difference from Example 1.

実施例 8 (第 1発明の実施例) Example 8 (Example of the first invention)

実施例 1で使用した N d F e B系磁石のスクラ ップ 4 5 k g を原料 と して、 側部を焼結アルミナ円筒 2 3で断熱し、 底部のみを水冷銅板 2 4 と した第 8図に示す坩堝を配置した 3 0 0 kWのプラズマアーク 溶解炉を用いて、 アルゴンガス雰囲気中で溶解し、 一次イ ンゴッ トを 得た。 一次イ ンゴッ トの分析値は N d + P r — 2 5. 8 w t % , D y — 2. 3 w t % , A 1 - 0. 3 4 w t % , B— 1 . 0 0 w t % , O - 0. 0 1 8 w t % , C - 0. 0 4 w t %、 F e残であった。  A scrap of 45 kg of the NdFeB magnet used in Example 1 was used as a raw material, the side was insulated with a sintered alumina cylinder 23, and only the bottom was a water-cooled copper plate 24. Using a 300 kW plasma arc melting furnace in which the crucibles shown in the figure were arranged, melting was performed in an argon gas atmosphere to obtain a primary ingot. Analytical value of primary ingot is Nd + Pr-25.8 wt%, Dy-2.3 wt%, A1-0.34 wt%, B-1.00 wt%, O -0.018 wt%, C-0.04 wt%, Fe remaining.

溶解温度は実施例 3 と同じ 1 6 0 0でと した。 坩堝 1 は、 内径 3 2 O mm、 深さ 1 5 0 mmで厚さ 3 0 mmの焼結アルミナ円筒 2 3であ り、 その底部に水冷銅板 2 4 を配置した。  The dissolution temperature was set at 160, the same as in Example 3. The crucible 1 was a sintered alumina cylinder 23 having an inner diameter of 32 O mm, a depth of 150 mm and a thickness of 30 mm, and a water-cooled copper plate 24 was disposed at the bottom.

さ らに、 実施例 3 と同じく 、 この一次ィンゴッ トを用いて磁石合金 を溶解铸造した。 表 2に示すよ うに、 この方法においても、 スクラッ プを高温溶解するこ とで、 酸素濃度を著しい低減と高い二次溶解収率 が得られた。 Further, as in Example 3, the magnetic alloy was melt-formed using this primary ingot. As shown in Table 2, in this method, too, by dissolving the scrap at a high temperature, the oxygen concentration was significantly reduced and a high secondary dissolution yield was obtained.

表 2 Table 2

一次イ ンゴッ トの溶解収率、 酸素分析値  Primary ingot dissolution yield, oxygen analysis

Figure imgf000025_0001
実施例 9 (第 2発明の実施例)
Figure imgf000025_0001
Example 9 (Example of the second invention)

実施例 6 と同様に N d F e B系磁石スクラ ップ原料を溶解し、 出湯 した後、 その溶湯が完全に固化する前に、 アルゴンガス雰囲気を破ら ずに、 原料を追加装入し、 再度、 通電し溶解した。 坩堝内の溶湯が一 杯になったら、 その一部を坩堝の傾動によ り 出湯し、 また、 原料を追 装するこ とで、 連続的に溶解することができた。 また、 坩堝上部の出 湯口にメ タルが固化し、 この部分に通電初期に異常アークが飛ぶので、 この部分の固化メ タルを少し切り欠いて出湯口を作った。 このよ うな方法によって溶解しても、 実施例 8 と同じ一次イ ンゴッ 卜が得られた。 As in Example 6, after the NdFeB-based magnet scrap raw material was melted and discharged, before the molten metal was completely solidified, additional raw materials were added without breaking the argon gas atmosphere. Again, electricity was applied to dissolve. When the molten metal in the crucible became full, a part of the molten metal was poured out by tilting the crucible, and the raw material was added, so that it could be melted continuously. In addition, the metal solidified in the tap at the top of the crucible, and an abnormal arc flew in this part at the beginning of energization, so the solidified metal in this part was cut out slightly to make the tap. The same primary ingot as in Example 8 was obtained by dissolution by such a method.

実施例 1 0 (第 3発明の実施例) Example 10 (Example of the third invention)

実施例 3で使用した N d F e B系磁石のスクラ ップ 4 5 k g原料と して、 側部を焼結アルミナ円筒で断熱し、 かつ、 底部も焼結アルミナ 板で断熱し、 その内部に通電部と して純鉄製の円形板を設置した第 6 図に示す坩堝を配置した 3 0 0 k Wのプラズマアーク溶解炉を用いて、 アルゴンガス雰囲気中で溶解し、 一次イ ンゴッ トが得た。  Scrap of NdFeB-based magnet used in Example 3 45 kg As a raw material, the sides were insulated with a sintered alumina cylinder, and the bottom was also insulated with a sintered alumina plate. Using a 300 kW plasma arc melting furnace equipped with a crucible as shown in Fig. 6 in which a circular plate made of pure iron was installed as a current-carrying part, melting was performed in an argon gas atmosphere, and the primary ingot was cooled. Obtained.

溶解温度は実施例 1 と同じ 1 6 0 0 °Cと した。 坩堝 1 は、 内経 3 2 O mm、 深さ 1 5 O mmで厚さ 3 0 mmの焼結アルミナ円筒 1 0であ り、 その底部に外経 3 2 O mm, 厚さ 3 O mmの焼結アルミナ円形板 を配置し、 その内側に 0. 5 mmの純鉄円形板を配置した。  The dissolution temperature was set at 160 ° C., the same as in Example 1. The crucible 1 is a sintered alumina cylinder 10 having an inner diameter of 32 O mm, a depth of 15 O mm and a thickness of 30 mm, and an outer diameter of 32 O mm and a thickness of 3 O mm at the bottom thereof. A sintered alumina circular plate was placed, and a 0.5 mm pure iron circular plate was placed inside.

この方法においても、 実施例 6 と同じイ ンゴッ トが得られた。  In this method, the same ingot as in Example 6 was obtained.

実施例 1 1 (第 3発明の実施例) Example 1 1 (Example of the third invention)

実施例 3で使用した N d F e B系磁石のスクラ ップを原料と して、 側部を焼結アルミ ナ円筒 2 2で断熱し、 かつ、 底部の中央に出湯口 2 5の空いた ドーナツ状の焼結アルミナ板 2 1 で断熱し、 その内側に通 電部と して純鉄部と して純鉄製の円形板 2 0を設置した第 8図に示す 坩堝を配置した 3 0 0 k wのプラズマアーク溶解炉を用いて、 ァルゴ ンガス雰囲気中で溶解した。 溶解すると鉄板の中央が破れ、 溶湯は下 部に流出し、 その下に設置した铸型中に一次イ ンゴッ トを得た。 一次 イ ンゴッ トの分析値は N d + P r — 2 5. 5 w t % , D y— 2. 2 w t % , A 1 - 0. 3 5 w t % , B - 1. 0 1 w t % , O— 0. 0 1 8 w t % , C— 0. 0 4 w t %、 F e残であった。  Using the scrap of the NdFeB magnet used in Example 3 as a raw material, the side part was insulated with a sintered alumina cylinder 22 and the tap hole 25 was left in the center of the bottom. The crucible shown in FIG. 8 was provided, in which a doughnut-shaped sintered alumina plate 21 was insulated, and a pure iron circular plate 20 was installed as a conducting part inside the pure iron part as a conducting part. Melting was performed in an argon gas atmosphere using a kw plasma arc melting furnace. When melted, the center of the steel plate was broken, and the molten metal flowed to the bottom, and a primary ingot was obtained in the mold installed underneath. The analysis value of the primary ingot was Nd + Pr-25.5 wt%, Dy-2.2 wt%, A1-0.35 wt%, B-1.01 wt%, O — 0.018 wt%, C— 0.04 wt%, Fe remaining.

この実施例では底部の焼結アルミ ナ板が、 内径 1 0 O mm、 外径 3 2 0 mm, 厚さ 3 0 m mの ドーナツ状であるほ力、は、 実施例 1 0 と同 じ条件で溶解した。 この方法では、 スラグと一部のメ タルが坩堝内に 残るので、 スラグの巻き込みの少ない 4 0 k gのイ ンゴッ 卜が得られ た。 実施例 1 2 (第 3発明の実施例) In this example, the sintered aluminum plate at the bottom was a doughnut having an inner diameter of 10 O mm, an outer diameter of 320 mm, and a thickness of 30 mm under the same conditions as in Example 10. Dissolved. In this method, slag and some metal remained in the crucible, so that a 40 kg ingot with little slag entrainment was obtained. Example 1 2 (Example of the third invention)

実施例 1 0 と同じ条件で溶解 · 出湯後、 坩堝内に残った固化メ タル の上部にあるスラグを部分的に削り取り 、 下側のメタル層を露出して 通電部分を確保してから、 原料を追加装入し、 再通電を行い溶解を行 う方法を操り返した。 この際、 残存固化メ タルの中央に穴の空いたチ ヤージもあつたので、 この場合は鉄箔あるいは鉄板を置いて孔を塞い で原料を装入した。 この方法では、 実施例 1 0 と同じインゴッ トが得 られた。 産業上の利用可能性  After melting and tapping under the same conditions as in Example 10, the slag on the upper part of the solidified metal remaining in the crucible was partially scraped off, the lower metal layer was exposed and the energized part was secured. Was added, and the method of melting by re-energizing was repeated. At this time, there was also a charge with a hole in the center of the remaining solidified metal. In this case, iron foil or an iron plate was placed to close the hole and the raw material was charged. In this method, the same ingot as in Example 10 was obtained. Industrial applicability

以上説明したよ うに、 従来は希土類磁石スクラ ップ中の酸素濃度を 低かさせる有効な方法がなかったので、 せいぜいスクラ ップ使用量を 制限してバージン原料と溶解するこ とで満足する他はなかった。 本発 明による と、 このよ うな制限はないために現在磁石製造工程で発生し ているスクラ ップを効率良く経済的に再利用するこ とができる。 この ために、 資源の有効活用と生産量の増大が達成できる。  As explained above, there has been no effective method to lower the oxygen concentration in the rare earth magnet scrap, so it is satisfactory to limit the amount of scrap used and dissolve it with the virgin raw material at best. There was no. According to the present invention, since there is no such restriction, the scrap generated in the magnet manufacturing process can be efficiently and economically reused. For this reason, effective utilization of resources and increase in production can be achieved.

Claims

請 求 の範 囲 The scope of the claims 1. 希土類磁石のス ク ラ ップを一次溶解して希土類磁石製造用原料 を得る方法において、  1. In a method of obtaining a raw material for manufacturing rare earth magnets by first melting a scrap of a rare earth magnet, 溶湯保持部の一部又は全部を断熱 ( 2 ) した水冷坩堝 ( 1 ) あるい は耐火物製坩堝 ( 7 ) に希土類磁石のスク ラ ップ ( 3 ) を装入し、 前 記坩堝 ( 1 ) の上方に位置するよ う に設けられた少なく と も 1対の陽 極と陰極よ り なるプラズマ トーチ ( 1 0 ) によ り希土類磁石のスク ラ ップを溶解するこ と を特徴とする希土類磁石ス ク ラ ップの溶解方法。  A rare-earth magnet scrap (3) is charged into a water-cooled crucible (1) or a refractory crucible (7) in which part or all of the molten metal holding part is insulated (2). The rare earth magnet scrap is melted by a plasma torch (10) consisting of at least one pair of cathode and cathode, which is provided above the Dissolving method for rare earth magnet scrap. 2. 前記希土類磁石のスク ラ ップを溶解時、 該希土類磁石のスクラ ップの融点よ り 2 0 0 °C以上の高温に溶湯を保持する こ と を特徴とす る請求の範囲第 1項記載の希土類磁石ス ク ラ ップの溶解方法。  2. The method according to claim 1, wherein when melting the scrap of the rare earth magnet, the molten metal is kept at a temperature higher than 200 ° C. from the melting point of the scrap of the rare earth magnet. Dissolving method of rare earth magnet scrap described in section. 3. 前記希土類磁石のス ク ラ ップに、 希土類磁石構成元素の 1種以 上を主成分とする金属又は合金からなるバージン原料を加えて溶解す る請求の範囲第 1又は 2項記載の希土類磁石スク ラ ップの溶解方法。  3. The rare earth magnet scrap according to claim 1 or 2, wherein a virgin raw material made of a metal or an alloy mainly containing at least one of the rare earth magnet constituent elements is added to and dissolved in the rare earth magnet scrap. Rare earth magnet scrap melting method. 4. 溶解された希土類磁石スク ラ ップの溶湯の一部を出湯し、 残部 の溶湯が前記坩堝内にて未固化の状態にある と きに希土類磁石のス ク ラ ップを追加装入するこ とを特徴とする請求の範囲第 1項から第 3項 までの何れか 1項記載の希土類磁石スク ラ ップの溶解方法。  4. Dissolve a part of the melted rare-earth magnet scrap and add the rare-earth magnet scrap when the remaining melt is not solidified in the crucible. The method for melting a rare earth magnet scrap according to any one of claims 1 to 3, characterized in that: 5. 希土類磁石のスク ラ ップを一次溶解して希土類磁石製造用原料 を得る方法において、  5. In the method of obtaining the raw material for rare earth magnet production by primary melting the rare earth magnet scrap, 溶湯保持部が断熱部分 ( 2 ) と水冷部分とを有する坩堝 ( 1 ) に希 土類磁石のスク ラ ップ ( 3 ) を装入し、 タ ングステンアークまたは移 行型プラズマアーク ( 1 5 ) にて希土類磁石のスク ラ ップを溶解する こ とを特徴とする希土類磁石スク ラ ップの溶解方法。  A scrap (3) of rare earth magnet is charged in a crucible (1) having a heat insulating part (2) and a water-cooled part in the molten metal holding part, and a tungsten arc or a transitional plasma arc (15) A method for dissolving a rare earth magnet scrap, characterized by dissolving the rare earth magnet scrap in (1). 6. 前記希土類磁石のスク ラ ップを溶解後、 該希土類磁石のスク ラ ップの融点の 2 0 0 °C以上の高温に溶湯を保持する こ と を特徴とする 請求の範囲第 5項記載の希土類磁石ス ク ラ ップの溶解方法。  6. The method according to claim 5, wherein after melting the scrap of the rare earth magnet, the molten metal is kept at a high temperature of 200 ° C. or more, which is the melting point of the scrap of the rare earth magnet. Dissolving method of rare earth magnet scrap described. 7. 前記希土類磁石のスク ラ ップに、 希土類磁石構成元素の 1種以 上を主成分とする金属または合金からなるバージン原料を加えて溶解 する請求の範囲第 6 又は 7項記載の希土類磁石スク ラ ップの溶解方法, 7. To the scrap of the rare earth magnet, add a virgin material composed of a metal or alloy containing at least one of the rare earth magnet constituent elements as a main component and melt. The method for dissolving a rare earth magnet scrap according to claim 6 or 7, 8. 溶解された希土類磁石スク ラ ップの溶湯の一部を出湯し、 残部 の溶湯が前記坩堝内にて未固化の状態にある と きに希土類磁石のスク ラ ップを追加装入する こ と を特徴とする請求の範囲第 5から第 7項ま での何れか 1 項記載の希土類磁石スクラ ップの溶解方法。 8. Dissolve a part of the melted rare earth magnet scrap and add the rare earth magnet scrap when the rest of the melt is unsolidified in the crucible. The method for dissolving a rare earth magnet scrap according to any one of claims 5 to 7, characterized in that: 9. 希土類磁石のス ク ラ ップを一次溶解して希土類磁石製造用原料 を得る方法において、 溶湯保持部が断熱構造 ( 2 1 , 2 2 ) を有する 坩堝 ( 1 ) に希土類磁石のスクラ ップ ( 3 ) を装入し、 該坩堝の断熱 面を局部的に被覆する第 1 の電極 ( 2 0 ) と該坩堝上方に配置された 第 2の電極 ( 1 5 ) と の間でタ ングステンアーク または移行型プラズ マアークを発生させる こ とによ り 、 希土類磁石のスク ラ ップを溶解す るこ とを特徴とする希土類磁石ス ク ラ ップの溶解方法。  9. In the method of obtaining a raw material for rare earth magnet production by primary melting of the rare earth magnet scrap, the molten metal holding part has a heat insulating structure (21, 22) in a crucible (1). And a second electrode (15) disposed above the crucible and a first electrode (20) for locally covering the heat insulating surface of the crucible. A method for dissolving a rare earth magnet scrap, which comprises dissolving a rare earth magnet scrap by generating an arc or a transition type plasma arc. 1 0. 前記希土類磁石のスク ラ ップを溶解後、 該希土類磁石のスク ラ ップの融点の 2 0 0 °C以上の高温に溶湯を保持するこ とを特徴とす る請求の範囲第 9項記載の希土類磁石スク ラ ップの溶解方法。  10. The method according to claim 1, wherein after the scrap of the rare earth magnet is melted, the molten metal is kept at a high temperature of 200 ° C. or more, which is the melting point of the scrap of the rare earth magnet. 9. The method for dissolving a rare earth magnet scrap according to item 9. 1 1 . 前記希土類磁石のスク ラ ップに、 希土類磁石構成元素の 1種 以上を主成分とする金属又は合金からなるバージン原料を加えて溶解 する請求の範囲第 9又は 1 0記載の希土類磁石スク ラ ップの溶解方法, 11. The rare earth magnet according to claim 9 or 10, wherein a virgin raw material made of a metal or an alloy containing at least one of the rare earth magnet constituent elements as a main component is added to the rare earth magnet scrap and melted. How to dissolve scrap, 1 2. 前記坩堝 ( 1 ) の底部を貫通する出湯孔を被覆する前記第 1 の電極 ( 2 0 ) 力 前記希土類磁石スク ラ ップの全量が溶解後, 溶湯 中に溶解される よ う にした請求の範囲第 9から第 1 1 項までの何れか 1項記載の希土類磁石スク ラ ップの溶解方法。 1 2. The power of the first electrode (20) for covering the tap hole penetrating the bottom of the crucible (1) so that the entire amount of the rare earth magnet scrap is dissolved in the molten metal after melting. 12. The method for melting a rare earth magnet scrap according to any one of claims 9 to 11, wherein: 1 3. 前記希土類磁石スク ラ ップの溶湯中を前記出湯孔から出湯す る際に、 前記希土類磁石ス ク ラ ップの溶湯上のス ラ グ層を出湯流に混 入させないこ と を特徴とする請求の範囲第 1 2項記載の希土類磁石ス ク ラ ップの溶解方法。  1 3. When the molten metal of the rare-earth magnet scrap is discharged from the tap hole, the slag layer on the molten metal of the rare-earth magnet scrap should not be mixed into the molten metal flow. 13. The method for melting a rare earth magnet scrap according to claim 12, wherein 1 4. 少なく と も 1 対の陽極と陰極よ り なるプラズマ トーチ ( 1 0 ) を備えたプラズマアーク溶解炉内に、 溶湯保持部の一部又は全部 を断熱した水冷坩堝 ( 1 ) あるいは耐火物製坩堝 ( 7 ) を配置したこ とを特徴とする希土類磁石スク ラ ップの溶解装置。 1 4. In a plasma arc melting furnace equipped with a plasma torch (10) consisting of at least one pair of anode and cathode, a water-cooled crucible (1) or refractory in which part or all of the molten metal holding part is insulated. The crucible (7) A melting device for rare earth magnet scraps. 1 5 . 前記坩堝の底部全体を被覆する よ う に耐火物板 ( 2 ) を配置 して前記断熱部分と した請求の範囲第 1 4項記載の希土類磁石スク ラ ップの溶解装置。  15. The rare-earth magnet scrap melting apparatus according to claim 14, wherein a refractory plate (2) is disposed so as to cover the entire bottom of the crucible and serves as the heat-insulating portion. 1 6 . タ ングステンアークまたは移行型プラズマアーク炉 ( 1 5 ) 内に、 溶湯保持部が断熱部分と水冷部分と を有する坩堝 ( 1 ) を配置 したこ と を特徴とする希土類磁石ス ク ラ ップの溶解装置。  16. A rare-earth magnet scrap, characterized in that a crucible (1) in which a molten metal holding part has an insulating part and a water-cooling part is arranged in a tungsten arc or transition type plasma arc furnace (15). Melting equipment. 1 7 . 前記水冷部分の坩堝壁の一部を覆う よ う に金属板 ( 2 ) を電 極の一部と して配置したこ と を特徴とする請求の範囲第 1 6項記載の 希土類磁石ス ク ラ ップの溶解装置。  17. The rare earth magnet according to claim 16, wherein a metal plate (2) is arranged as a part of the electrode so as to cover a part of the crucible wall of the water-cooled part. Scrap melting equipment. 1 8 . 前記坩堝の底部全体を被覆する よ う に耐火物板 ( 2 ) を配置 して前記断熱部分と した請求の範囲第 1 6又は 1 7項記載の希土類磁 石スク ラ ップの溶解装置。  18. The dissolution of the rare earth magnet scrap according to claim 16 or 17, wherein a refractory plate (2) is disposed so as to cover the entire bottom of the crucible and is used as the heat insulating portion. apparatus. 1 9 . タ ングステンアークまたは移行型プラズマアーク炉内に、 溶 湯保持部が断熱構造 ( 2 1 , 2 2 ) を有する坩堝と、 該坩堝の断熱面 を局部的に被覆する第 1 の電極 ( 2 0 ) と、 該坩堝上方に配置された 第 2の電極 ( 1 5 ) と含んでなる こ とを特徴とする希土類磁石スク ラ ップの溶解装置。  19. In a tungsten arc or transition type plasma arc furnace, a crucible having a molten metal holding portion having a heat insulating structure (21, 22), and a first electrode (for locally covering the heat insulating surface of the crucible) 20) and a second electrode (15) disposed above the crucible, a melting apparatus for a rare earth magnet scrap, comprising: 2 0 . 前記坩堝の底部を貫通する出湯口を形成したこ と を特徴とす る請求の範囲第 1 9項記載の希土類磁石ス ク ラ ップの溶解装置。  20. The apparatus for melting a rare earth magnet scrap according to claim 19, wherein a tap hole penetrating the bottom of the crucible is formed. 2 1 . 重量百分率で、 3 111と じ 6 の合計で 1 0 4 0 1 % N d が 5 w t %以下、 F e 力 S 2 5 w t %以下、 C u力 S 4 〜 : I 0 w t % Z r 力 S 1 4 w t %、 酸素が 0 . 1 w t %以下、 残部が主と して C o で あり 、 さ らに酸素を除く 希土類磁石製造工程に起因する不可避的不純 物、 及び F e を除く 一次溶解に起因 した侵入入元素である こ と を特徴 とする希土類磁石ス ク ラ ップの一次溶解合金。  2 1. In terms of weight percentage, the sum of 3 111 and 6 is 1041% Nd is 5 wt% or less, Fe force S2 is 5 wt% or less, Cu force S4 〜: I 0 wt% Zr force S 14 wt%, oxygen is 0.1 wt% or less, the balance is mainly Co, and unavoidable impurities and Fe that are caused by the rare earth magnet manufacturing process excluding oxygen Primary melting alloy of rare earth magnet scrap characterized by being an intrusion element caused by primary melting. 2 2 . 重量百分率で、 N d , P r 及び D yが合計で 2 0 3 5 w t % B力 S ◦ . 9 1 . 2 w t % A 1 力; 0 . 1 〜 : 1 w t % C o 力 S 5 w t % 以下、 C u力 S 0 . 5 w t %以下、 N b力 S 1 w t %以下, 酸素力; 0 . 1 w t %以下、 残部が主と して F e であり 、 さ らに酸素を除く希土類磁 石製造工程に起因する不可避的不純物、 及び F e を除く 一次溶解に起 因した侵入入元素であるこ とを特徴とする希土類磁石スクラ ップの一 次溶解合金。 22. By weight percentage, Nd, Pr and Dy total 2035 wt% B force S ◦ .91.2 wt% A1 force; 0.1 ~: 1 wt% Co force S 5 wt% or less, Cu power S 0.5 wt% or less, Nb power S 1 wt% or less, oxygen power; 0.1 wt% or less, with the remainder being mainly Fe, inevitable impurities due to the rare earth magnet manufacturing process excluding oxygen, and invading elements caused by primary dissolution excluding Fe, Primary molten alloy with rare earth magnet scrap. 2 3. 前記不可避的不純物が 0. 1 %以下の Cである請求項 2 1又 は 2 2記載の希土類磁石スクラ ップの一次溶解合金。  23. The primary molten alloy of a rare earth magnet scrap according to claim 21 or 22, wherein the unavoidable impurity is C of 0.1% or less. 2 4. イ ンゴッ ト形状である請求項 2 1 から 2 3項までの何れか 1 項記載の希土類磁石スクラ ップの一次溶解合金。  24. The primary molten alloy of the rare earth magnet scrap according to any one of claims 21 to 23, wherein the alloy is in an ingot shape. 2 5. イ ンゴッ トの重量が l 〜 5 0 k gである請求項 2 4記載の希 土類磁石スク ラ ップの一次溶解合金。  25. The primary molten alloy of a rare earth magnet scrap according to claim 24, wherein the weight of the ingot is l to 50 kg. 2 6. 希土類磁石が焼結磁石である請求項 2 1 から 2 5項までの何 れか 1項記載の希土類磁石スクラ ップの一次溶解合金。  26. The primary molten alloy of the rare-earth magnet scrap according to any one of claims 21 to 25, wherein the rare-earth magnet is a sintered magnet. 2 7. 溶湯保持部の一部又は全部を断熱 ( 2 ) した水冷坩堝 ( 1 ) あるいは耐火物製坩堝 ( 7 ) に希土類磁石のスク ラ ップ ( 3 ) を装入 し、 前記坩堝 ( 1 ) の上方に位置するよ う に設けられた少なく と も 1 対の陽極と陰極よ り なるプラズマ トーチ ( 1 0 ) によ り希土類磁石の スク ラ ップを溶解することによ り溶製された請求項 2 1 から 2 6項ま での何れか 1記載の希土類磁石ス ク ラ ップの一次溶解合金。  2 7. A rare-earth magnet scrap (3) is placed in a water-cooled crucible (1) or a refractory crucible (7) in which part or all of the molten metal holding part is insulated (2), and the crucible (1) is charged. ) Is formed by melting the scrap of the rare-earth magnet by a plasma torch (10) consisting of at least one pair of anode and cathode provided so as to be located above The primary molten alloy of the rare earth magnet scrap according to any one of claims 21 to 26. 2 8. 溶湯保持部が断熱部分 ( 2 ) と水冷部分とを有する坩堝 ( 1 ) に希土類磁石のスクラップ ( 3 ) を装入し、 タングステンアークまた は移行型プラズマアーク ( 1 5 ) にて希土類磁石のスクラップを溶解 することによ り溶製された請求項 2 1 から 2 6項までの何れか 1記載 の希土類磁石スクラップの一次溶解合金。  2 8. A scrap (3) of a rare earth magnet is charged into a crucible (1) having a heat insulating part (2) and a water-cooled part in the molten metal holding part, and the rare earth is transferred by a tungsten arc or a transition type plasma arc (15). The primary molten alloy of the rare earth magnet scrap according to any one of claims 21 to 26, produced by melting a scrap of a magnet. 2 9. 溶湯保持部が断熱構造 ( 2 1 , 2 2 ) を有する坩堝 ( 1 ) に 希土類磁石のスクラ ップ ( 3 ) を装入し、 該坩堝の断熱面を局部的に 被覆する第 1 の電極 ( 2 0 ) と該坩堝上方に配置された第 2の電極 ( 1 5 ) との間でタングステンアークまたは移行型プラズマアークを発生 させるこ とによ り 、 希土類磁石のスクラ ップを溶解することによ り溶 製された請求項 2 1 から 2 6項までの何れか 1記載の希土類磁石スク ラ ップの一次溶解合金, 2 9. A rare earth magnet scrap (3) is charged into a crucible (1) having a heat insulating structure (2 1, 2 2) having a molten metal holding section, and a first heat treatment is performed to locally cover the heat insulating surface of the crucible. By generating a tungsten arc or a transition type plasma arc between the second electrode (20) and the second electrode (15) arranged above the crucible, the scrap of the rare earth magnet is melted. 27. The rare-earth magnet disk according to any one of claims 21 to 26, Primary molten alloy in lap,
PCT/JP1999/007264 1998-12-25 1999-12-24 Method and device for melting rare earth magnet scrap and primary molten alloy of rare earth magnet Ceased WO2000039514A1 (en)

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DE102014206223A1 (en) 2014-04-01 2015-10-01 Fme Freiberger Metallrecycling Und Entwicklungsdienstleistungen Gmbh Process for the recovery of rare earths from rare earth-containing compositions
DE102014224015A1 (en) 2014-11-25 2016-05-25 Fme Freiberger Metallrecycling Und Entwicklungsdienstleistungen Gmbh Process for the recovery of rare earths from rare earth-containing phosphors
DE102014224015B4 (en) 2014-11-25 2019-07-04 Fme Freiberger Metallrecycling Und Entwicklungsdienstleistungen Gmbh Process for the recovery of rare earths from rare earth-containing phosphors
JPWO2022019172A1 (en) * 2020-07-21 2022-01-27

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