JP2002285208A - Method for preparing rare earth alloy powder material, and method for manufacturing rare earth alloy sintered compact using the same - Google Patents
Method for preparing rare earth alloy powder material, and method for manufacturing rare earth alloy sintered compact using the sameInfo
- Publication number
- JP2002285208A JP2002285208A JP2001091012A JP2001091012A JP2002285208A JP 2002285208 A JP2002285208 A JP 2002285208A JP 2001091012 A JP2001091012 A JP 2001091012A JP 2001091012 A JP2001091012 A JP 2001091012A JP 2002285208 A JP2002285208 A JP 2002285208A
- Authority
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- Japan
- Prior art keywords
- rare earth
- earth alloy
- preparing
- powder material
- alloy
- 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.)
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Links
- 239000000843 powder Substances 0.000 title claims abstract description 148
- 229910045601 alloy Inorganic materials 0.000 title claims abstract description 131
- 239000000956 alloy Substances 0.000 title claims abstract description 131
- 238000000034 method Methods 0.000 title claims abstract description 69
- 229910052761 rare earth metal Inorganic materials 0.000 title claims abstract description 60
- 150000002910 rare earth metals Chemical class 0.000 title claims abstract description 58
- 239000000463 material Substances 0.000 title claims abstract description 43
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 22
- 239000000314 lubricant Substances 0.000 claims abstract description 55
- 238000010298 pulverizing process Methods 0.000 claims abstract description 27
- 239000007787 solid Substances 0.000 claims abstract description 25
- 239000002245 particle Substances 0.000 claims description 22
- 239000011261 inert gas Substances 0.000 claims description 12
- NUKZAGXMHTUAFE-UHFFFAOYSA-N methyl hexanoate Chemical compound CCCCCC(=O)OC NUKZAGXMHTUAFE-UHFFFAOYSA-N 0.000 claims description 12
- JGHZJRVDZXSNKQ-UHFFFAOYSA-N methyl octanoate Chemical compound CCCCCCCC(=O)OC JGHZJRVDZXSNKQ-UHFFFAOYSA-N 0.000 claims description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 8
- 239000001301 oxygen Substances 0.000 claims description 8
- 229910052760 oxygen Inorganic materials 0.000 claims description 8
- 238000010791 quenching Methods 0.000 claims description 8
- 230000000171 quenching effect Effects 0.000 claims description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 6
- 239000001257 hydrogen Substances 0.000 claims description 6
- 229910052739 hydrogen Inorganic materials 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 5
- 238000005245 sintering Methods 0.000 claims description 5
- 238000003860 storage Methods 0.000 claims description 4
- 238000003825 pressing Methods 0.000 claims description 3
- 238000002360 preparation method Methods 0.000 claims 1
- 230000015572 biosynthetic process Effects 0.000 abstract description 4
- 238000000859 sublimation Methods 0.000 abstract description 4
- 230000008022 sublimation Effects 0.000 abstract description 4
- 239000002994 raw material Substances 0.000 description 14
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 12
- 238000007254 oxidation reaction Methods 0.000 description 10
- 238000005266 casting Methods 0.000 description 9
- 230000003647 oxidation Effects 0.000 description 7
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 6
- 229910001882 dioxygen Inorganic materials 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- CBOQJANXLMLOSS-UHFFFAOYSA-N ethyl vanillin Chemical compound CCOC1=CC(C=O)=CC=C1O CBOQJANXLMLOSS-UHFFFAOYSA-N 0.000 description 6
- 238000000465 moulding Methods 0.000 description 6
- 239000000203 mixture Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 229910000521 B alloy Inorganic materials 0.000 description 4
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 239000013078 crystal Substances 0.000 description 4
- 229910001873 dinitrogen Inorganic materials 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- DSSYKIVIOFKYAU-XCBNKYQSSA-N (R)-camphor Chemical compound C1C[C@@]2(C)C(=O)C[C@@H]1C2(C)C DSSYKIVIOFKYAU-XCBNKYQSSA-N 0.000 description 3
- 241000723346 Cinnamomum camphora Species 0.000 description 3
- 230000032683 aging Effects 0.000 description 3
- 229910052796 boron Inorganic materials 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 229960000846 camphor Drugs 0.000 description 3
- 229930008380 camphor Natural products 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- UQLDLKMNUJERMK-UHFFFAOYSA-L di(octadecanoyloxy)lead Chemical compound [Pb+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O UQLDLKMNUJERMK-UHFFFAOYSA-L 0.000 description 3
- 229940073505 ethyl vanillin Drugs 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 239000012188 paraffin wax Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- -1 tetragonal compound Chemical class 0.000 description 3
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000001110 calcium chloride Substances 0.000 description 2
- 229910001628 calcium chloride Inorganic materials 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- KPLQYGBQNPPQGA-UHFFFAOYSA-N cobalt samarium Chemical compound [Co].[Sm] KPLQYGBQNPPQGA-UHFFFAOYSA-N 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- UKMSUNONTOPOIO-UHFFFAOYSA-N docosanoic acid Chemical compound CCCCCCCCCCCCCCCCCCCCCC(O)=O UKMSUNONTOPOIO-UHFFFAOYSA-N 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 229930195729 fatty acid Natural products 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- VKOBVWXKNCXXDE-UHFFFAOYSA-N icosanoic acid Chemical compound CCCCCCCCCCCCCCCCCCCC(O)=O VKOBVWXKNCXXDE-UHFFFAOYSA-N 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000003801 milling Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 229910000938 samarium–cobalt magnet Inorganic materials 0.000 description 2
- JXSRRBVHLUJJFC-UHFFFAOYSA-N 7-amino-2-methylsulfanyl-[1,2,4]triazolo[1,5-a]pyrimidine-6-carbonitrile Chemical compound N1=CC(C#N)=C(N)N2N=C(SC)N=C21 JXSRRBVHLUJJFC-UHFFFAOYSA-N 0.000 description 1
- 235000021357 Behenic acid Nutrition 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 235000021353 Lignoceric acid Nutrition 0.000 description 1
- CQXMAMUUWHYSIY-UHFFFAOYSA-N Lignoceric acid Natural products CCCCCCCCCCCCCCCCCCCCCCCC(=O)OCCC1=CC=C(O)C=C1 CQXMAMUUWHYSIY-UHFFFAOYSA-N 0.000 description 1
- 229910052779 Neodymium Inorganic materials 0.000 description 1
- 229910052772 Samarium Inorganic materials 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- QJVKUMXDEUEQLH-UHFFFAOYSA-N [B].[Fe].[Nd] Chemical compound [B].[Fe].[Nd] QJVKUMXDEUEQLH-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 125000003545 alkoxy group Chemical group 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 229940116226 behenic acid Drugs 0.000 description 1
- 229910052810 boron oxide Inorganic materials 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 238000009750 centrifugal casting Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- JKWMSGQKBLHBQQ-UHFFFAOYSA-N diboron trioxide Chemical compound O=BOB=O JKWMSGQKBLHBQQ-UHFFFAOYSA-N 0.000 description 1
- 238000004512 die casting Methods 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 125000001301 ethoxy group Chemical group [H]C([H])([H])C([H])([H])O* 0.000 description 1
- FARYTWBWLZAXNK-WAYWQWQTSA-N ethyl (z)-3-(methylamino)but-2-enoate Chemical compound CCOC(=O)\C=C(\C)NC FARYTWBWLZAXNK-WAYWQWQTSA-N 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- HGPXWXLYXNVULB-UHFFFAOYSA-M lithium stearate Chemical compound [Li+].CCCCCCCCCCCCCCCCCC([O-])=O HGPXWXLYXNVULB-UHFFFAOYSA-M 0.000 description 1
- 125000000956 methoxy group Chemical group [H]C([H])([H])O* 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- QEFYFXOXNSNQGX-UHFFFAOYSA-N neodymium atom Chemical compound [Nd] QEFYFXOXNSNQGX-UHFFFAOYSA-N 0.000 description 1
- 229910001172 neodymium magnet Inorganic materials 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 229910001404 rare earth metal oxide Inorganic materials 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- KZUNJOHGWZRPMI-UHFFFAOYSA-N samarium atom Chemical compound [Sm] KZUNJOHGWZRPMI-UHFFFAOYSA-N 0.000 description 1
- 150000004671 saturated fatty acids Chemical class 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 229910052727 yttrium Inorganic materials 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01F—MAGNETS; INDUCTANCES; TRANSFORMERS; SELECTION OF MATERIALS FOR THEIR MAGNETIC PROPERTIES
- H01F1/00—Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties
- H01F1/01—Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials
- H01F1/03—Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials characterised by their coercivity
- H01F1/032—Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials characterised by their coercivity of hard-magnetic materials
- H01F1/04—Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials characterised by their coercivity of hard-magnetic materials metals or alloys
- H01F1/047—Alloys characterised by their composition
- H01F1/053—Alloys characterised by their composition containing rare earth metals
- H01F1/055—Alloys characterised by their composition containing rare earth metals and magnetic transition metals, e.g. SmCo5
- H01F1/0555—Alloys characterised by their composition containing rare earth metals and magnetic transition metals, e.g. SmCo5 pressed, sintered or bonded together
- H01F1/0557—Alloys characterised by their composition containing rare earth metals and magnetic transition metals, e.g. SmCo5 pressed, sintered or bonded together sintered
Landscapes
- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Power Engineering (AREA)
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
- Powder Metallurgy (AREA)
- Hard Magnetic Materials (AREA)
- Manufacturing Cores, Coils, And Magnets (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、R−Fe−B系焼
結磁石の製造方法および、R−Fe−B系焼結磁石の製
造に用いられる原料の合金粉末材料の調製方法並びに保
存方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an R--Fe--B sintered magnet, a method for preparing an alloy powder material as a raw material used for producing an R--Fe--B sintered magnet, and a method for storing the same. About.
【0002】[0002]
【従来の技術】希土類合金の焼結磁石(永久磁石)は、
一般に、希土類合金の粉末をプレス成形し、得られた粉
末の成形体を焼結し、時効処理することによって製造さ
れる。現在、サマリウム・コバルト系磁石と、ネオジム
・鉄・ボロン系磁石の二種類が各分野で広く用いられて
いる。なかでも、ネオジム・鉄・ボロン系磁石(以下、
「R−Fe−B系磁石」と称する。RはYを含む希土類
元素、Feは鉄、Bはボロンである。)は、種々の磁石
の中で最も高い最大磁気エネルギー積を示し、価格も比
較的安いため、各種電子機器へ積極的に採用されてい
る。2. Description of the Related Art Rare earth alloy sintered magnets (permanent magnets)
Generally, it is manufactured by pressing a rare earth alloy powder, sintering the obtained powder compact, and subjecting it to aging treatment. At present, two types of samarium / cobalt magnets and neodymium / iron / boron magnets are widely used in various fields. Among them, neodymium-iron-boron magnets (hereinafter referred to as
It is called "R-Fe-B magnet". R is a rare earth element containing Y, Fe is iron, and B is boron. ) Shows the highest maximum magnetic energy product among various magnets and is relatively inexpensive, so that it is actively employed in various electronic devices.
【0003】R−Fe−B系焼結磁石は、主にR2Fe
14Bの正方晶化合物からなる主相、Nd等からなるRリ
ッチ相、およびBリッチ相から構成されている。なお、
Feの一部がCoやNiなどの遷移金属と置換されても
よく、ボロン(B)の一部が炭素(C)で置換されても
よい。本発明が好適に適用されるR−Fe−B系焼結磁
石は、例えば、米国特許第4,770,723号および
米国特許第4,792,368号の明細書に記載されて
いる。[0003] R-Fe-B sintered magnets are mainly composed of R 2 Fe.
It is composed of a main phase composed of a tetragonal compound of 14 B, an R-rich phase composed of Nd and the like, and a B-rich phase. In addition,
A part of Fe may be substituted with a transition metal such as Co or Ni, and a part of boron (B) may be substituted with carbon (C). R-Fe-B based sintered magnets to which the present invention is suitably applied are described, for example, in U.S. Pat. No. 4,770,723 and U.S. Pat. No. 4,792,368.
【0004】このような磁石となるR−Fe−B系合金
を作製するために、従来は、インゴット鋳造法が用いら
れてきた。一般なインゴット鋳造法によると、出発原料
である希土類金属、電解鉄およびフェロボロン合金を高
周波溶解し、得られた溶湯を鋳型内で比較的ゆっくりと
冷却することによって合金インゴットが作製される。[0004] Ingot casting has conventionally been used to produce such an R-Fe-B alloy as a magnet. According to a general ingot casting method, a rare earth metal, an electrolytic iron, and a ferroboron alloy, which are starting materials, are subjected to high-frequency melting, and the obtained molten metal is cooled relatively slowly in a mold to produce an alloy ingot.
【0005】近年、合金の溶湯を単ロール、双ロール、
回転ディスク、または回転円筒鋳型の内面などに接触さ
せることによって、比較的速く冷却し、合金溶湯から、
インゴットよりも薄い凝固合金(「合金フレーク」と称
することにする。)を作製するストリップキャスト法や
遠心鋳造法に代表される急冷法が注目されている。この
ような急冷法によって作製された合金片の厚さは、一般
に、約0.03mm以上約10mm以下の範囲にある。
急冷法によると、合金溶湯は冷却ロールに接触した面
(ロール接触面)から凝固し始め、ロール接触面から厚
さ方向に結晶が柱状に成長してゆく。その結果、ストリ
ップキャスト法などによって作製された急冷合金は、短
軸方向のサイズが約0.1μm以上約100μm以下
で、長軸方向のサイズが約5μm以上約500μm以下
のR2Fe14B結晶相と、R2Fe14B結晶相の粒界に分
散して存在するRリッチ相とを含有する組織を持つにい
たる。Rリッチ相は希土類元素Rの濃度が比較的高い非
磁性相であり、その厚さ(粒界の幅に相当する)は約1
0μm以下になる。In recent years, molten alloys have been rolled in single rolls, twin rolls,
By contacting the rotating disk, or the inner surface of the rotating cylindrical mold, etc., it cools relatively quickly, and from the molten alloy,
A quenching method typified by a strip casting method or a centrifugal casting method for producing a solidified alloy (hereinafter referred to as “alloy flake”) thinner than an ingot has been attracting attention. The thickness of the alloy piece produced by such a quenching method is generally in the range of about 0.03 mm or more and about 10 mm or less.
According to the quenching method, the molten alloy begins to solidify from the surface in contact with the chill roll (roll contact surface), and crystals grow columnar from the roll contact surface in the thickness direction. As a result, the quenched alloy produced by the strip casting method or the like has an R 2 Fe 14 B crystal having a minor axis size of about 0.1 μm to about 100 μm and a major axis size of about 5 μm to about 500 μm. It has a structure containing a phase and an R-rich phase dispersed and present at the grain boundaries of the R 2 Fe 14 B crystal phase. The R-rich phase is a non-magnetic phase in which the concentration of the rare earth element R is relatively high, and its thickness (corresponding to the width of the grain boundary) is about 1
0 μm or less.
【0006】急冷合金は、従来のインゴット鋳造法(金
型鋳造法)によって作製された合金(インゴット合金)
に比較して相対的に短い時間(冷却速度:102℃/秒
以上、104℃/秒以下)で冷却されているため、組織
が微細化され、結晶粒径が小さいという特徴を有してい
る。また、粒界の面積が広く、Rリッチ相は粒界内に広
く広がっているため、Rリッチ相の分散性にも優れると
いう利点がある。これらの特徴が故に、急冷合金を用い
ることによって、優れた磁気特性を有する磁石を製造す
ることができる。[0006] The quenched alloy is an alloy (ingot alloy) produced by a conventional ingot casting method (die casting method).
Since the cooling is performed in a relatively short time (cooling rate: 10 2 ° C / sec or more and 10 4 ° C / sec or less), the structure is refined and the crystal grain size is small. ing. Further, since the area of the grain boundary is large and the R-rich phase is widely spread in the grain boundary, there is an advantage that the dispersibility of the R-rich phase is excellent. Because of these characteristics, a magnet having excellent magnetic properties can be manufactured by using a quenched alloy.
【0007】また、Ca還元法(あるいは還元拡散法)
と呼ばれる方法も知られている。この方法は以下の工程
を含む。まず、希土類酸化物のうちの少なくとも1種
と、鉄粉および純ボロン粉と、フェロボロン粉およびホ
ウ素酸化物のうちの少なくとも1種とを所定の割合で含
む混合粉、あるいは上記構成元素の合金粉または混合酸
化物を所定の割合で含む混合粉に、金属カルシウム(C
a)および塩化カルシウム(CaCl)を混合し、不活
性ガス雰囲気下で還元拡散処理を施す。得られた反応生
成物をスラリー化し、これを水処理することによって、
R−Fe−B系合金の固体が得られる。Also, the Ca reduction method (or reduction diffusion method)
A method called is also known. The method includes the following steps. First, a mixed powder containing at least one of rare earth oxides, iron powder and pure boron powder, and at least one of ferroboron powder and boron oxide at a predetermined ratio, or an alloy powder of the above constituent elements Alternatively, mixed calcium (C)
a) and calcium chloride (CaCl) are mixed and subjected to a reduction diffusion treatment under an inert gas atmosphere. By slurrying the obtained reaction product and treating it with water,
An R-Fe-B based alloy solid is obtained.
【0008】なお、本明細書において、固体合金の塊を
「合金塊」と呼び、従来のインゴット鋳造法によって得
られる合金インゴットおよびストリップキャスト法など
の急冷法によって得られる合金フレークなどの溶湯を冷
却して得られた凝固合金だけでなく、Ca還元法によっ
て得られる固体合金など、種々の形態の固体合金を含む
ものとする。In the present specification, a solid alloy lump is referred to as an “alloy lump”, and a molten metal such as an alloy ingot obtained by a conventional ingot casting method and an alloy flake obtained by a rapid cooling method such as a strip casting method is cooled. In addition to the solidified alloy obtained as a result, various types of solid alloys such as a solid alloy obtained by a Ca reduction method are included.
【0009】プレス成形に供される合金粉末は、これら
の合金塊を、例えば水素吸蔵法および/または種々の機
械的粉砕法(例えばディスクミルが用いられる)で粉砕
し、得られた粗粉末(例えば、平均粒径10μm〜50
0μm)を例えばジェットミルを用いた乾式粉砕法で微
粉砕することによって得られる。The alloy powder to be subjected to press molding is obtained by crushing these alloy lumps by, for example, a hydrogen absorbing method and / or various mechanical crushing methods (for example, using a disk mill), and obtaining a coarse powder ( For example, the average particle size is 10 μm to 50 μm.
0 μm) by, for example, fine pulverization by a dry pulverization method using a jet mill.
【0010】プレス成形に供せられるR−Fe−B系合
金粉末の平均粒径は、磁気特性の観点から、1μm〜1
0μmの範囲内にあることが好ましい。なお、粉末の
「平均粒径」は、特にことわらない限り、ここでは、質
量中位径(mass median diameter:MMD)を指すことに
する。[0010] The average particle size of the R-Fe-B-based alloy powder to be subjected to press molding is 1 μm to 1 μm from the viewpoint of magnetic properties.
It is preferably in the range of 0 μm. The “average particle size” of the powder herein refers to the mass median diameter (MMD) unless otherwise specified.
【0011】しかしながら、一般に、希土類合金粉末
は、酸化されやすく、発熱や発火の惧れすらある。その
中でも、特に、ストリップキャスト合金に代表される急
冷法によって作製された合金の粉末は、特に酸化されや
すい。急冷合金の粉末粒子の表面には、酸化され易いR
リッチ相が表れやすいため、特にその危険性が高いと考
えられる。However, in general, rare earth alloy powders are easily oxidized, and there is a risk of heat generation or even ignition. Among them, in particular, alloy powder produced by a quenching method represented by a strip cast alloy is particularly easily oxidized. The surface of the quenched alloy powder particles has an easily oxidized R
It is considered that the risk is particularly high because a rich phase is likely to appear.
【0012】この問題を回避するために、例えば、希土
類合金の粉末の表面に薄い酸化膜を形成する方法が、特
公平6−6728号公報(出願人:住友特殊金属株式会
社、出願日:1986年7月24日)に開示されてい
る。In order to avoid this problem, for example, a method of forming a thin oxide film on the surface of rare earth alloy powder is disclosed in Japanese Patent Publication No. 6-6728 (applicant: Sumitomo Special Metals Co., Ltd., filing date: 1986). July 24).
【0013】一方、このように平均粒径が小さな粉末を
用いると流動性やプレス成形性(キャビティ充填性およ
び圧縮性を含む)が悪く、生産性が悪いという問題があ
る。On the other hand, when the powder having the small average particle size is used, there is a problem that fluidity and press moldability (including cavity filling property and compressibility) are poor and productivity is poor.
【0014】この問題を解決する方法として、合金粉末
粒子の表面を潤滑剤で覆うことが検討されている。As a method for solving this problem, it has been studied to cover the surface of the alloy powder particles with a lubricant.
【0015】例えば、特開平08−111308号公報
および対応米国特許5、666、635号(譲受人:住
友特殊金属株式会社)の明細書には、平均粒径10μm
〜500μmのR−Fe−B系合金の粗粉末に、少なく
とも1種の脂肪酸エステルを液状化した潤滑剤を、0.
02質量%〜5.0質量%添加混合後、不活性ガスを用
いたジェットミル粉砕を行い、平均粒径1.5μm〜5
μmの微粉末を作製する技術が開示されている。For example, in the specification of Japanese Patent Application Laid-Open No. 08-111308 and the corresponding US Pat. No. 5,666,635 (assignee: Sumitomo Special Metals Co., Ltd.), the average particle size is 10 μm.
A lubricant obtained by liquefying at least one kind of fatty acid ester is added to a coarse powder of an R-Fe-B-based alloy having a thickness of about 500 µm.
After adding and mixing 02% by mass to 5.0% by mass, the mixture was subjected to jet mill pulverization using an inert gas to obtain an average particle size of 1.5 μm
A technique for producing a fine powder of μm is disclosed.
【0016】また、特公平7−098962号公報は、
固形パラフィンやショウノウを潤滑剤として用いること
を開示しているが、合金を微粉砕した後に潤滑剤を添加
しているため、合金の酸化を抑制する効果が低い。さら
に、上記公報には、合金の酸化を抑制するために、固形
パラフィンやショウノウを湿式で混合することが好まし
いと記載されている。Further, Japanese Patent Publication No. 7-098962 discloses that
Although the use of solid paraffin or camphor as a lubricant is disclosed, the effect of suppressing the oxidation of the alloy is low because the lubricant is added after the alloy is finely pulverized. Further, the above publication describes that it is preferable to mix solid paraffin and camphor in a wet manner in order to suppress the oxidation of the alloy.
【0017】さらに、特許2915560号公報には、
有機溶剤を用いずに潤滑剤で粉末表面を被覆する方法と
して、R−Fe−B系合金の粗粉末に潤滑剤としての高
級脂肪酸等を乾式で添加・混合した後、得られた粗粉末
を微粉砕する方法を開示している。Further, Japanese Patent No. 2915560 discloses that
As a method of coating the powder surface with a lubricant without using an organic solvent, after adding and mixing a higher fatty acid or the like as a lubricant in a dry manner to a coarse powder of an R-Fe-B-based alloy, A method of milling is disclosed.
【0018】[0018]
【発明が解決しようとする課題】特公平6−6728号
公報に記載されているように酸化膜を形成すると、磁気
特性が低下するので好ましくない。特に、モータ用の永
久磁石など、高い保磁力が要求される用途に用いられる
焼結磁石を製造することが難しいという問題がある。It is not preferable to form an oxide film as described in Japanese Patent Publication No. 6-6728, since the magnetic characteristics are deteriorated. In particular, there is a problem that it is difficult to manufacture a sintered magnet used for an application requiring a high coercive force, such as a permanent magnet for a motor.
【0019】一方、上述の潤滑剤を用いる方法では、流
動性および成形を改善できるものの、希土類合金粉末の
酸化を防止する効果が充分ではなく、安定な希土類合金
粉末材料を得るためには、特公平6−6728号公報に
記載されているように酸化膜を形成することが必要とな
り、上記の問題を解決することが難しい。On the other hand, although the method using the above-mentioned lubricant can improve the fluidity and the molding, the effect of preventing the rare earth alloy powder from being oxidized is not sufficient. As described in Japanese Patent Publication No. 6-6728, it is necessary to form an oxide film, and it is difficult to solve the above problem.
【0020】本発明は、上記の諸点に鑑みてなされたも
のであり、本発明の主な目的は、酸化膜の形成が抑制さ
れ、且つ、流動性に優れた希土類合金粉末材料の製造方
法およびそれを用いた希土類合金焼結体の製造方法を提
供することにある。The present invention has been made in view of the above points, and a main object of the present invention is to provide a method of manufacturing a rare earth alloy powder material which suppresses formation of an oxide film and has excellent fluidity. An object of the present invention is to provide a method for producing a rare earth alloy sintered body using the same.
【0021】[0021]
【課題を解決するための手段】本発明による希土類合金
粉末材料の調製方法は、(a)希土類合金の粗粉砕粉末
を準備する工程と、(b)常温で昇華性を有する固体の
潤滑剤が存在する状態で、前記粗粉砕粉末を微粉砕する
ことによって、前記潤滑剤によって表面が覆われた前記
希土類合金の微粉末から実質的に構成される粉末材料を
調製する工程とを包含し、そのことによって上記目的が
達成される。According to the present invention, there is provided a method for preparing a rare earth alloy powder material comprising the steps of (a) preparing a coarsely pulverized powder of a rare earth alloy, and (b) solid lubricant having sublimability at room temperature. Preparing a powder material substantially consisting of the rare earth alloy fine powder, the surface of which is covered by the lubricant, by finely pulverizing the coarsely pulverized powder in the presence thereof. This achieves the above object.
【0022】なお、本願明細書においては、実質的に希
土類合金のみの粉末(表面の酸化物層は含み得る)から
なる「希土類合金粉末」に対して、「希土類合金粉末」
だけでなく、潤滑剤を含む、プレス成形に供せられる粉
末材料を「希土類合金粉末材料」と呼び、区別する。In the present specification, the term "rare earth alloy powder" is used in contrast to the term "rare earth alloy powder" consisting essentially of a powder of a rare earth alloy (which may include an oxide layer on the surface).
In addition, a powder material containing a lubricant and subjected to press molding is called a “rare earth alloy powder material” and is distinguished.
【0023】前記希土類合金は、R−Fe−B系合金で
あってよい。The rare earth alloy may be an R—Fe—B based alloy.
【0024】工程(b)は、酸素ガス酸素ガスの含有量
が200ppm以下の不活性ガス雰囲気中で実行される
ことが好ましい。工程(b)は、ジェットミルを用いて
実行され得る。Step (b) is preferably carried out in an inert gas atmosphere having an oxygen gas content of 200 ppm or less. Step (b) can be performed using a jet mill.
【0025】前記微粉末の酸素含有量は、3000pp
m以下であることが好ましく、2000ppm以下であ
ることがさらに好ましい。The oxygen content of the fine powder is 3000 pp
m or less, more preferably 2000 ppm or less.
【0026】前記潤滑剤は、末端にCH3を有する有機
分子からなることが好ましい。The lubricant preferably comprises an organic molecule having a terminal CH 3 .
【0027】工程(a)は、前記希土類合金の合金塊を
準備する工程と、前記合金塊を水素吸蔵法によって粗粉
砕する工程とを包含してよい。The step (a) may include a step of preparing an alloy lump of the rare earth alloy and a step of coarsely pulverizing the alloy lump by a hydrogen storage method.
【0028】前記合金塊は、急冷法によって作製された
合金フレークであってよい。[0028] The alloy ingot may be an alloy flake produced by a quenching method.
【0029】前記希土類合金の前記微粉末の平均粒径
は、2μm〜10μmの範囲内にあることが好ましい。The average particle size of the fine powder of the rare earth alloy is preferably in the range of 2 μm to 10 μm.
【0030】工程(b)の後に、前記希土類合金粉末材
料に、さらに、カプロン酸メチルおよびカプリル酸メチ
ルの内の少なくとも1種を添加し、混合する工程を包含
することが好ましい。Preferably, after the step (b), a step of adding at least one of methyl caproate and methyl caprylate to the rare earth alloy powder material and mixing the same is further included.
【0031】本発明による希土類合金焼結体の製造方法
は、上記のいずれかの方法で調製された希土類合金粉末
材料を準備する工程と、(c)前記粉末材料をプレス成
形することによって成形体を得る工程と、(d)前記成
形体を焼結することによって焼結体を得る工程とを包含
し、そのことによって上記目的が達成される。The method for producing a rare earth alloy sintered body according to the present invention comprises the steps of: preparing a rare earth alloy powder material prepared by any of the above methods; and (c) press-forming the powder material. And (d) a step of obtaining a sintered body by sintering the molded body, whereby the object is achieved.
【0032】本発明による希土類焼結磁石の製造方法
は、上記方法で製造された希土類合金焼結体を準備する
工程と、前記希土類合金焼結体を着磁する工程とを包含
する。The method for producing a rare earth sintered magnet according to the present invention includes a step of preparing a rare earth alloy sintered body produced by the above method and a step of magnetizing the rare earth alloy sintered body.
【0033】[0033]
【発明の実施の形態】以下、本発明による実施形態の希
土類合金焼結体の製造方法を説明する。以下の実施形態
の説明においては、特に、サマリウム・コバルト系合金
粉末よりも酸化されやすいR−Fe−B系合金粉末を用
いた焼結磁石の製造方法を例に本発明の特徴を説明する
が、本発明はこれに限られず、サマリウム・コバルト系
合金焼結体の製造方法に適用することもできる。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A method for manufacturing a rare earth alloy sintered body according to an embodiment of the present invention will be described below. In the following description of the embodiments, in particular, the features of the present invention will be described with an example of a method of manufacturing a sintered magnet using an R-Fe-B-based alloy powder that is more easily oxidized than a samarium-cobalt-based alloy powder. However, the present invention is not limited to this, and can be applied to a method for manufacturing a samarium-cobalt-based alloy sintered body.
【0034】本実施形態のR−Fe−B系合金焼結体の
製造方法は、(a)R−Fe−B系合金の粗粉砕粉末を
準備する工程と、(b)常温で昇華性を有する固体の潤
滑剤が存在する状態で、粗粉砕粉末を微粉砕することに
よって、潤滑剤によって表面が覆われた合金の微粉末か
ら実質的に構成される粉末材料を調製する工程と、
(c)粉末材料をプレス成形することによって成形体を
得る工程と、(d)成形体を焼結することによって焼結
体を得る工程とを包含する。この後の任意の時点で、希
土類合金焼結体を着磁することによって焼結磁石が得ら
れる。The method for producing an R—Fe—B alloy sintered body according to the present embodiment includes (a) a step of preparing a coarsely pulverized powder of an R—Fe—B alloy, and (b) sublimation at room temperature. In the presence of a solid lubricant having, by finely pulverizing the coarsely pulverized powder, preparing a powder material substantially composed of fine powder of alloy whose surface is covered by the lubricant,
(C) a step of obtaining a compact by pressing the powder material to obtain a compact; and (d) a step of obtaining a sintered compact by sintering the compact. At any point after this, a sintered magnet is obtained by magnetizing the rare earth alloy sintered body.
【0035】常温で昇華性を有する固体の潤滑剤が存在
する状態で、粗粉砕粉末を微粉砕するので、固体の潤滑
剤から昇華することによって生成された気体状の潤滑剤
が、粉砕によって生成された活性の高い表面に付着す
る。その結果、合金の微粉末の表面の酸化が抑制される
とともに、流動性や成形性が改善される。ここで、「昇
華性を有する」とは、25℃で1.00Pa以上の蒸気
圧を有することをいう。The coarsely pulverized powder is finely pulverized in the presence of a solid lubricant having sublimability at room temperature, so that a gaseous lubricant produced by sublimation from the solid lubricant is produced by the pulverization. Adheres to highly active surfaces. As a result, oxidation of the surface of the alloy fine powder is suppressed, and fluidity and moldability are improved. Here, “having sublimability” means having a vapor pressure of 1.00 Pa or more at 25 ° C.
【0036】従って、特公平6−6728号公報に記載
されているように合金微粉末の表面に積極的に酸化膜を
形成することなく、安定な合金粉末材料を得ることが可
能となる。すなわち、酸素ガスの含有量が200ppm
以下の不活性ガス(希ガスおよび窒素ガスを含む)雰囲
気中で、粗粉砕を実行しても、合金の微粉末が酸化され
ることが抑制される。また、潤滑剤の添加・混合および
微粉砕の工程を全て、乾式法で実行することができるの
で、製造プロセスを簡略化できる。これらの工程は、ジ
ェットミルを用いて実行することができる。Accordingly, a stable alloy powder material can be obtained without actively forming an oxide film on the surface of the alloy fine powder as described in Japanese Patent Publication No. 6-6728. That is, the content of oxygen gas is 200 ppm
Even if the coarse pulverization is performed in the following inert gas (including a rare gas and a nitrogen gas) atmosphere, oxidation of the alloy fine powder is suppressed. Further, since all of the steps of adding / mixing the lubricant and finely pulverizing can be performed by a dry method, the manufacturing process can be simplified. These steps can be performed using a jet mill.
【0037】常温で昇華性を有する固体の潤滑剤として
は、特に、末端にCH3を有する有機分子からなる潤滑
剤を用いることが好ましい。分子末端のCH3は、希土
類合金の表面との親和性が高く、微粉砕によって生成さ
れた活性な表面に速やかに付着し、酸化を抑制する効果
が高い。なお、分子末端のCH3は、メチル基やエチル
基などのアルキル基、およびメトキシ基やエトキシ基な
どのアルコキシ基に含まれるものであってよい。また、
常温(25℃)での蒸気圧は1Pa以上のものが好まし
い。As a solid lubricant having sublimability at room temperature, it is particularly preferable to use a lubricant comprising an organic molecule having CH 3 at a terminal. CH 3 at the molecular end has a high affinity for the surface of the rare-earth alloy, is quickly attached to the active surface generated by the fine pulverization, and has a high effect of suppressing oxidation. Note that CH 3 at the molecular end may be included in an alkyl group such as a methyl group or an ethyl group, or an alkoxy group such as a methoxy group or an ethoxy group. Also,
The vapor pressure at room temperature (25 ° C.) is preferably 1 Pa or more.
【0038】昇華性を有する固体潤滑剤の添加量は、希
土類合金粉末の質量に対して、0.01質量%から0.
5質量%の範囲内にあることが好ましい。0.01質量
%よりも少ないと、微粉末の表面を充分に被覆すること
ができないために、酸化を抑制する効果が充分に発揮さ
れないことがある。また、0.5質量%よりも多いと、
焼結体中に残存し、磁気特性を低下させることがある。
昇華性を有する固体潤滑剤とともに、他の固体潤滑剤を
用いることもできる。このとき、昇華性を有する固体潤
滑剤の添加量は、全潤滑剤量の50質量%以上あること
が好ましい。また、潤滑剤をさらに後添加する場合も含
め、全潤滑剤の合計が0.5質量%を超えないことが好
ましい。昇華性を有する固体潤滑剤と併用される昇華性
を有しない固体潤滑剤としては、ステアリン酸鉛、ステ
アリン酸銅、ステアリン酸リチウムやステアリン酸を好
適に用いることができる。The amount of the solid lubricant having sublimability is from 0.01% by mass to 0.1% by mass based on the mass of the rare earth alloy powder.
Preferably it is in the range of 5% by mass. If the amount is less than 0.01% by mass, the surface of the fine powder cannot be sufficiently coated, and the effect of suppressing oxidation may not be sufficiently exhibited. Further, when it is more than 0.5% by mass,
It may remain in the sintered body and deteriorate magnetic properties.
Other solid lubricants can be used together with the sublimable solid lubricant. At this time, the amount of the solid lubricant having sublimability is preferably 50% by mass or more of the total amount of the lubricant. In addition, it is preferable that the total of all the lubricants does not exceed 0.5% by mass even when the lubricant is further added later. As the non-sublimable solid lubricant used in combination with the sublimable solid lubricant, lead stearate, copper stearate, lithium stearate and stearic acid can be suitably used.
【0039】本発明の製造方法は、高い保磁力を有する
磁石の製造において効果的であり、酸素含有量が300
0ppm以下、特に2000ppm以下の微粉末を用い
る場合に効果的である。例えば、上記特公平6−672
8号公報に記載されている方法に従って、0.5〜2%
の酸素ガスを混合した窒素ガスを用いてジェットミルで
粉砕すると、微粉末中の酸含有量が5000ppm〜6
000ppmとなり、磁気特性が低下する。例えば、上
述したように、酸素ガス含有量が200ppm以下の不
活性ガス雰囲気下で、微粉砕工程を実行すると、酸素含
有量が3000ppm以下の微粉末を得ることができ
る。The production method of the present invention is effective in producing a magnet having a high coercive force and has an oxygen content of 300.
It is effective when a fine powder of 0 ppm or less, particularly 2000 ppm or less is used. For example, the above-mentioned Tokuhei 6-672
No. 8 according to the method described in JP-A No. 8
When pulverized by a jet mill using nitrogen gas mixed with oxygen gas, the acid content in the fine powder is 5000 ppm to 6 ppm.
000 ppm, and the magnetic properties deteriorate. For example, as described above, when the pulverization step is performed in an inert gas atmosphere having an oxygen gas content of 200 ppm or less, a fine powder having an oxygen content of 3000 ppm or less can be obtained.
【0040】また、R−Fe−B系合金の粗粉末が、合
金塊を水素吸蔵法によって粗粉砕することによって得ら
れたものであると、酸化され易いRリッチな相が粗粉末
の表面に表れていることが多いので、本発明の効果が顕
著となる。さらに、R−Fe−B系合金の合金塊が、ス
トリップキャスト法で代表される急冷法によって作製さ
れた合金フレークであるときに、粗粉末の表面にRリッ
チ相が表れることが多い。粗粉末の平均粒径としては、
50μm〜1mmの範囲内にあることが好ましく、10
0μm〜800μmの範囲内にあることがさらに好まし
い。Further, when the coarse powder of the R—Fe—B alloy is obtained by coarsely pulverizing an alloy lump by the hydrogen absorbing method, an easily oxidized R-rich phase is formed on the surface of the coarse powder. In many cases, the effect of the present invention is remarkable. Furthermore, when the R-Fe-B-based alloy ingot is an alloy flake produced by a quenching method represented by a strip casting method, an R-rich phase often appears on the surface of the coarse powder. As the average particle size of the coarse powder,
It is preferably in the range of 50 μm to 1 mm,
More preferably, it is in the range of 0 μm to 800 μm.
【0041】固体潤滑剤が昇華することによって生成し
た潤滑剤の気体が存在する状態で粗粉末を微粉砕するこ
とによって得られる微粉末の平均粒径は、磁気特性およ
び成形性の観点から、2μm〜10μmの範囲内にある
ことが好ましい。この微粉末のBET法による比表面積
は、約0.45m2/g〜約0.55m2/gの範囲内に
ある。The average particle size of the fine powder obtained by finely pulverizing the coarse powder in the presence of the lubricant gas generated by sublimation of the solid lubricant is 2 μm from the viewpoint of magnetic properties and moldability. It is preferably in the range of 10 to 10 μm. BET specific surface area of the fine powder is in the range of about 0.45 m 2 / g to about 0.55 m 2 / g.
【0042】得られた粉末材料に対し、さらに、潤滑剤
を添加してもよい。後添加する潤滑剤としては、カプロ
ン酸メチルおよびカプリル酸メチルのいずれかまたは両
方を用いることが好ましい。例えば、潤滑剤は、主成分
としてカプロン酸メチルおよびカプリル酸メチルの少な
くとも1種を2〜20質量%、添加成分として炭素数が
20〜24の飽和脂肪酸(例えば、アラキジン酸、ベヘ
ン酸、リグノセリン酸)の少なくとも1種を0.005
〜0.5質量%、残部が沸点が40℃〜200℃の炭化
水素系溶剤(例えば、ノルマルパラフィン、イソパラフ
ィン、シクロパラフィン)を用いることが好ましい。カ
プロン酸メチルおよびカプリル酸メチルは、流動性およ
び成形時の圧縮性を改善する効果に優れている。A lubricant may be further added to the obtained powder material. It is preferable to use either or both of methyl caproate and methyl caprylate as the lubricant to be added later. For example, the lubricant contains 2 to 20% by mass of at least one of methyl caproate and methyl caprylate as a main component, and a saturated fatty acid having 20 to 24 carbon atoms as an additional component (for example, arachidic acid, behenic acid, lignoceric acid). ) At least one of 0.005
It is preferable to use a hydrocarbon-based solvent (e.g., normal paraffin, isoparaffin, cycloparaffin) having a boiling point of 40 to 200 ° C with a boiling point of 0.5 to 0.5% by mass. Methyl caproate and methyl caprylate have excellent effects of improving fluidity and compressibility during molding.
【0043】得られた粉末材料をプレス成形する。合金
粉末材料のプレス成形は、例えば、電動プレスを用い、
約0.8MA/m〜1.3MA/mの磁界中で配向させ
つつ、0.5ton/cm2〜1.0ton/cm2の圧
力で圧縮成形すれば、3.9g/cm3〜4.6g/c
m3の成形体密度を有する成形体を得ることができる。The obtained powder material is pressed. Press molding of the alloy powder material, for example, using an electric press,
While being oriented in a magnetic field of about 0.8MA / m~1.3MA / m, when compression molded at a pressure of 0.5ton / cm 2 ~1.0ton / cm 2 , 3.9g / cm3~4.6g / C
A compact having a compact density of m 3 can be obtained.
【0044】このようにして得られる成形体を、例えば
約1000℃〜約1180℃の温度で、約1〜2時間焼
結する。得られた焼結体を、例えば約450℃〜約80
0℃の温度で、約1〜8時間時効処理することによっ
て、R−Fe−B系焼結磁石が得られる。なお、焼結磁
石に含まれる炭素の量を減らし、磁気特性を向上するた
めに、上記焼結工程の前に、合金粉末の表面を覆う潤滑
剤を加熱除去(除去)する工程を付加しても良い。加熱
除去工程は、例えば、約 200℃から600℃の温度
で、約2Paの圧力下で、約3〜約6時間実行される。The thus obtained molded body is sintered at a temperature of, for example, about 1000 ° C. to about 1180 ° C. for about 1 to 2 hours. The obtained sintered body is, for example, about 450 ° C. to about 80 ° C.
By aging at a temperature of 0 ° C. for about 1 to 8 hours, an R—Fe—B based sintered magnet is obtained. In addition, in order to reduce the amount of carbon contained in the sintered magnet and improve the magnetic characteristics, a step of heating and removing (removing) the lubricant covering the surface of the alloy powder before the sintering step is added. Is also good. The heat removal step is performed, for example, at a temperature of about 200 ° C. to 600 ° C. under a pressure of about 2 Pa for about 3 to about 6 hours.
【0045】本実施形態によると、酸化膜の形成が抑制
され、且つ、流動性に優れたR−Fe−B系合金粉末の
製造方法およびそれを用いたR−Fe−B系合金焼結体
の製造方法が提供される。According to the present embodiment, a method for producing an R-Fe-B-based alloy powder in which the formation of an oxide film is suppressed and which has excellent fluidity, and an R-Fe-B-based alloy sintered body using the same. Is provided.
【0046】[0046]
【実施例】以下、本発明のR−Fe−B系焼結磁石の製
造方法について、実施例を挙げて説明するが、本発明は
以下の実施例によって何ら限定されるものではない。EXAMPLES Hereinafter, the method for producing an R-Fe-B based sintered magnet of the present invention will be described with reference to examples, but the present invention is not limited to the following examples.
【0047】Nd:30.8質量%、Pr:3.6質量
%、Dy:0.8質量%、B:1.0質量%、Co:
0.9質量%、Al:0.23質量%、Cu:0.10
質量%、残部Feおよび不可避不純物からなる組成の合
金フレークをストリップキャスト法で製造した。合金フ
レークの厚さは約0.2mm〜約0.4mmであり、大
きさは約2〜10mmであった。Nd: 30.8% by mass, Pr: 3.6% by mass, Dy: 0.8% by mass, B: 1.0% by mass, Co:
0.9% by mass, Al: 0.23% by mass, Cu: 0.10.
An alloy flake having a composition consisting of mass%, balance Fe and unavoidable impurities was produced by a strip casting method. The thickness of the alloy flake was about 0.2 mm to about 0.4 mm and the size was about 2 to 10 mm.
【0048】この合金フレークを水素吸蔵法によって粉
砕することによって合金粗粉末を得た。水素吸蔵法は、
公知の方法で実行され得る。例えば、特願平2000−
198508号に記載の方法を用いることができる。得
られた粗粉末の平均粒径は、100〜800μmであっ
た。この粗粉末中の含まれる酸素量は、約1200pp
mであった。This alloy flake was pulverized by a hydrogen storage method to obtain an alloy coarse powder. The hydrogen storage method is
It can be performed in a known manner. For example, Japanese Patent Application No. 2000-
The method described in 198508 can be used. The average particle size of the obtained coarse powder was 100 to 800 μm. The amount of oxygen contained in this coarse powder is about 1200 pp
m.
【0049】得られた粗粉末に、下記の表1に示す所定
量の潤滑剤を添加し、図1に示すジェットミル装置を用
いて微粉砕した。ジェットミル粉砕は、酸素ガス含有量
が200ppm以下で、純度が99.5%以上の窒素ガ
ス雰囲気中で実行した。A predetermined amount of a lubricant shown in Table 1 below was added to the obtained coarse powder, and the mixture was finely pulverized using a jet mill shown in FIG. Jet mill pulverization was performed in a nitrogen gas atmosphere having an oxygen gas content of 200 ppm or less and a purity of 99.5% or more.
【0050】まず、図1を参照しながら、ジェットミル
装置10を用いた、微粉砕工程を説明する。First, the pulverizing step using the jet mill device 10 will be described with reference to FIG.
【0051】ジェットミル粉砕装置10は、粗粉末を供
給する原料投入機12と、原料投入機12から投入され
た粗粉末を粉砕する粉砕機14と、粉砕機14で粉砕さ
れた粉末を分級するサイクロン分級機16と、サイクロ
ン分級機16によって分級された所定の粒度を有する微
粉末を集める回収タンク18とを備えている。The jet mill pulverizing device 10 supplies a raw material, a pulverizer 14 for supplying the coarse powder, a pulverizer 14 for pulverizing the coarse powder supplied from the raw material input unit 12, and a classifier for the pulverized powder. The apparatus includes a cyclone classifier 16 and a collection tank 18 for collecting fine powder having a predetermined particle size classified by the cyclone classifier 16.
【0052】原料投入機12は、粗粉末を収容する原料
タンク20と、原料タンク20からの粗粉末の供給量を
コントロールするモータ22と、モータ22に接続され
たスパイラル状の供給機(スクリューフィーダ)24と
を有している。The raw material input device 12 includes a raw material tank 20 for storing coarse powder, a motor 22 for controlling the amount of coarse powder supplied from the raw material tank 20, and a spiral feeder (screw feeder) connected to the motor 22. ) 24.
【0053】粉砕機14は、縦長の略円筒状の粉砕機本
体26を有しており、粉砕機本体26の下部には、不活
性ガス(例えば窒素ガス)を高速で噴出させるノズルを
取り付けるための複数のノズル口28が設けられてい
る。粉砕機本体26の側部には、粉砕機本体26内に粗
粉末を投入するための原料投入パイプ30が接続されて
いる。The crusher 14 has a vertically long, substantially cylindrical crusher main body 26, and a lower part of the crusher main body 26 is provided with a nozzle for ejecting an inert gas (for example, nitrogen gas) at a high speed. Are provided. A raw material input pipe 30 for inputting coarse powder into the crusher main body 26 is connected to a side portion of the crusher main body 26.
【0054】原料投入パイプ30には、供給する粗粉末
を一旦保持し、粉砕機14内部の圧力を閉じ込めるため
のバルブ32が設けられており、バルブ32は、一対の
上バルブ32aと下バルブ32bとを有している。供給
機24と原料投入パイプ30とはフレキシブルパイプ3
4によって連結されている。The raw material input pipe 30 is provided with a valve 32 for temporarily holding the supplied coarse powder and confining the pressure inside the crusher 14. The valve 32 includes a pair of an upper valve 32a and a lower valve 32b. And The feeder 24 and the raw material input pipe 30 are a flexible pipe 3
4 are connected.
【0055】粉砕機14は、粉砕機本体26の内部上方
に設けられた分級ロータ36と、粉砕機本体26の外部
上方に設けられたモータ38と、粉砕機本体26の上方
に設けられた接続パイプ40とを有している。モータ3
8は分級ロータ36を駆動し、接続パイプ40は分級ロ
ータ36で分級された微粉末を粉砕機14の外部に排出
する。The crusher 14 includes a classification rotor 36 provided inside and above the crusher body 26, a motor 38 provided above and outside the crusher body 26, and a connection provided above the crusher body 26. And a pipe 40. Motor 3
Reference numeral 8 drives the classification rotor 36, and the connection pipe 40 discharges the fine powder classified by the classification rotor 36 to the outside of the crusher 14.
【0056】粉砕機14は、支持部となる複数の脚部4
2を備えている。粉砕機14の外周近傍には基台44が
配置され、粉砕機14の脚部42と基台44との間に
は、ロードセルなどの重量検出器46が設けられてい
る。この重量検出器46からの出力に基づいて、制御部
48はモータ22の回転数を制御し、それによって粗粉
末の投入量をコントロールすることができる。The pulverizer 14 has a plurality of legs 4 serving as support portions.
2 is provided. A base 44 is disposed near the outer periphery of the crusher 14, and a weight detector 46 such as a load cell is provided between the leg 42 of the crusher 14 and the base 44. Based on the output from the weight detector 46, the control unit 48 controls the number of revolutions of the motor 22, and thereby can control the amount of the coarse powder to be charged.
【0057】サイクロン分級機16は、分級機本体64
を有し、分級機本体64の内部には、排気パイプ66が
上方から挿入されている。分級機本体64の側部には、
分級ロータ36で分級された微粉末を導入する導入口6
8が設けられており、導入口68はフレキシブルパイプ
70によって接続パイプ40と接続されている。分級機
本体64の下部には取り出し口72が設けられており、
この取り出し口72に所望の微粉末の回収タンク18が
接続されている。The cyclone classifier 16 comprises a classifier body 64
An exhaust pipe 66 is inserted into the classifier main body 64 from above. On the side of the classifier body 64,
Inlet 6 for introducing the fine powder classified by the classification rotor 36
8 are provided, and the inlet 68 is connected to the connection pipe 40 by a flexible pipe 70. An outlet 72 is provided at the lower part of the classifier main body 64,
The desired fine powder collection tank 18 is connected to the outlet 72.
【0058】フレキシブルパイプ34および70は、樹
脂もしくはゴム等によって構成されたもの、または剛性
の高い材料を蛇腹状もしくはコイル状に構成することに
よって柔軟性を持つように構成されたものであることが
好ましい。このような柔軟性のあるパイプ34および7
0を用いると、原料タンク20、供給機24、分級機本
体64および回収タンク18の重量変化が粉砕機14の
脚部42には伝達されない。そのため、脚部42に設け
た重量検出器46によって重量を検出すれば、粉砕機1
4内に滞留した粗粉末の重量やその変化量を正確に検知
でき、粉砕機14内に供給される粗粉末の量を正確に制
御することができる。The flexible pipes 34 and 70 may be made of resin, rubber or the like, or may be made of a highly rigid material in a bellows shape or a coil shape so as to have flexibility. preferable. Such flexible pipes 34 and 7
When 0 is used, a change in weight of the raw material tank 20, the feeder 24, the classifier main body 64, and the collection tank 18 is not transmitted to the leg 42 of the crusher 14. Therefore, if the weight is detected by the weight detector 46 provided on the leg 42, the crusher 1
4 can accurately detect the weight of the coarse powder and the amount of change in the coarse powder, and can accurately control the amount of the coarse powder supplied into the crusher 14.
【0059】次に、ジェットミル粉砕装置10による微
粉砕工程を説明する。Next, the fine pulverization process by the jet mill pulverizer 10 will be described.
【0060】まず、上述のようにして得られた合金の粗
粉末に、昇華性を有する固体潤滑剤(必要に応じて他の
固体潤滑剤を含む:いずれも粉状)を例えばロッキング
ミキサを用いて混合する。First, a sublimable solid lubricant (including other solid lubricants if necessary: all in powder form) is added to the coarse powder of the alloy obtained as described above using, for example, a rocking mixer. Mix.
【0061】得られた粗粉末を原料タンク20に投入す
る。原料タンク20内の粗粉末は、供給器24によって
粉砕機14に供給される。このとき、モータ22の回転
数を制御することによって粗粉末の供給量を調節するこ
とができる。供給器24から供給される粗粉末は、バル
ブ32において一旦堰きとめられる。ここで、一対の上
バルブ32aと下バルブ32bは、交互に開閉動作を行
なっている。すなわち、上バルブ32aが開状態のと
き、下バルブ32bは閉状態となり、上バルブ32aが
閉状態のとき、下バルブ32bが開状態となる。このよ
うに一対のバルブ32aおよび32bを交互に開閉する
ことによって、粉砕機14内の圧力が原料投入機12側
にもれないようにすることができる。その結果、粗粉末
は、上バルブ32aが開状態となったときに一対の上バ
ルブ32aと下バルブ32bとの間に供給される。そし
て、次に下バルブ32bが開状態になったときに、原料
投入パイプ30に導かれ、粉砕機14内に導入されるこ
とになる。バルブ30は制御回路48とは別のシーケン
ス回路(不図示)によって高速に駆動され、粗粉末が粉
砕機14内に連続的に供給される。The obtained coarse powder is put into the raw material tank 20. The coarse powder in the raw material tank 20 is supplied to the crusher 14 by the supply device 24. At this time, the supply amount of the coarse powder can be adjusted by controlling the rotation speed of the motor 22. The coarse powder supplied from the supply device 24 is temporarily stopped by the valve 32. Here, the pair of upper valve 32a and lower valve 32b alternately open and close. That is, when the upper valve 32a is open, the lower valve 32b is closed, and when the upper valve 32a is closed, the lower valve 32b is open. By alternately opening and closing the pair of valves 32a and 32b in this manner, the pressure in the crusher 14 can be prevented from flowing to the raw material input device 12 side. As a result, the coarse powder is supplied between the pair of upper valve 32a and lower valve 32b when the upper valve 32a is opened. Then, when the lower valve 32b is opened next time, it is guided to the raw material charging pipe 30 and introduced into the crusher 14. The valve 30 is driven at a high speed by a sequence circuit (not shown) different from the control circuit 48, and the coarse powder is continuously supplied into the crusher 14.
【0062】粉砕機14内に導入された粗粉末は、ノズ
ル口28からの不活性ガスの高速噴射によって粉砕機1
4内に巻き上げられ、装置内で高速気流とともに旋回す
る。そして、粗粉末同士の相互衝突によって細かく砕か
れる。この過程で、昇華性を有する固体潤滑剤は、粉砕
(摩砕)に伴って発生した熱によって昇華し、一瞬にし
て、合金の微粉末のフレッシュな表面(新たに生成され
た活性の高い表面)に付着すると考えられる。The coarse powder introduced into the crusher 14 is crushed by a high-speed injection of an inert gas from a nozzle port 28.
4 and revolves with the high-speed airflow in the device. Then, the coarse powder is finely crushed by mutual collision. In this process, the sublimable solid lubricant is sublimated by the heat generated during the grinding (grinding), and instantly becomes a fresh surface of the alloy fine powder (a newly generated highly active surface). ).
【0063】このようにして微粉砕され、潤滑剤が表面
に付着した粉末粒子は、上昇気流に乗って分級ロータ3
6に導かれ、分級ロータ36で分級され、粗い粒子は再
び粉砕されることになる。一方、所定粒径以下に粉砕さ
れた粒子は、接続パイプ40、フレキシブルパイプ70
を経由して導入口68からサイクロン分級機16の分級
機本体64内に導入される。分級機本体16内では、所
定粒径以上の相対的に大きな粒子が下部に設けられた回
収タンク18に堆積されるが、超微粉は不活性ガス気流
とともに、排気パイプ66を通りバグフィルタ82に至
り、バグフィルタ82で捕集される。不活性ガスは、バ
グフィルタ82を通過し、コンプレッサ84で圧縮さ
れ、一旦タンク86に貯蔵された後、再び、ノズル口2
8から粉砕機14内へ高速噴射される。このように不活
性ガスを循環使用することによって、不活性ガスの消費
量を低減することができる。The powder particles thus finely pulverized and having the lubricant attached to the surface are ridden by an ascending airflow to classify the rotor 3.
6 and classified by the classification rotor 36, and the coarse particles are again pulverized. On the other hand, particles pulverized to a predetermined particle size or less are connected pipe 40, flexible pipe 70
Through the inlet 68 into the classifier body 64 of the cyclone classifier 16. In the classifier main body 16, relatively large particles having a predetermined particle size or more are accumulated in a recovery tank 18 provided at a lower portion. Then, it is collected by the bag filter 82. The inert gas passes through the bag filter 82, is compressed by the compressor 84, and is temporarily stored in the tank 86.
8 is injected into the crusher 14 at high speed. By circulating and using the inert gas in this manner, the consumption of the inert gas can be reduced.
【0064】また、本発明では、室温で固体の潤滑剤を
使用しているので、バグフィルタ82が目詰まりするこ
とが防止できるので、上述のような循環型の粉砕装置を
構成することが可能になる。微粉砕工程において添加さ
れる固体潤滑剤の融点は、100℃を超えるものが好ま
しく、更に、150℃以上であることが好ましい。Further, in the present invention, since the solid lubricant is used at room temperature, the bag filter 82 can be prevented from being clogged, so that the above-mentioned circulation type pulverizing apparatus can be constituted. become. The melting point of the solid lubricant added in the pulverization step is preferably higher than 100 ° C, and more preferably 150 ° C or higher.
【0065】上述したように、排気パイプ66を通じて
超微粉を除去し、それによって回収タンク18で捕集す
る粉末に占める超微粉(粒径1μm以下)の個数比率を
10%以下に調節する。このようにして、Rを多く含む
超微粉が取り除かれると、焼結体中のRが酸素との結合
に消費される量を少なくし、磁気特性を向上することが
できるという利点が得られる。逆に、Rを多く含む超微
粉の割合が多すぎると、不活性ガス中の酸素ガス含有量
を減らしても、微粉末に含まれる酸素の量を3000p
pm以下にすることが困難になる。As described above, the ultrafine powder is removed through the exhaust pipe 66, whereby the number ratio of the ultrafine powder (particle size 1 μm or less) in the powder collected in the collection tank 18 is adjusted to 10% or less. In this manner, when the ultrafine powder containing a large amount of R is removed, there is an advantage that the amount of R in the sintered body consumed for bonding with oxygen can be reduced and the magnetic properties can be improved. Conversely, if the proportion of the ultrafine powder containing a large amount of R is too large, the amount of oxygen contained in the fine powder can be reduced by 3000 p even if the oxygen gas content in the inert gas is reduced.
pm or less.
【0066】上記の微粉砕工程によって、例えば、平均
粒径が約4μmで、しかも、1μm以下の超微粉の個数
が粉末全体の10%以下である微粉末を得ることができ
る。なお、焼結磁石の製造に用いられる微粉末の平均粒
径は2μm以上で10μm以下であることが好ましい。
なお、本発明によると、この微粉末の表面は、潤滑剤に
覆われており、酸化が抑制されている。By the above-mentioned fine pulverizing step, for example, a fine powder having an average particle size of about 4 μm and the number of ultrafine powders of 1 μm or less being 10% or less of the whole powder can be obtained. The average particle size of the fine powder used for manufacturing the sintered magnet is preferably 2 μm or more and 10 μm or less.
According to the present invention, the surface of the fine powder is covered with a lubricant, and oxidation is suppressed.
【0067】この後、更に潤滑剤を添加する場合は、微
粉末をロッキングミキサ内に充填し、例えば、0.3質
量%の潤滑剤を添加・混合すればよい。Thereafter, when further adding a lubricant, the fine powder may be filled in a rocking mixer, and for example, a lubricant of 0.3% by mass may be added and mixed.
【0068】得られたR−Fe−B系合金粉末材料を電
動プレスを用いて、約0.8MA/mの磁界中で配向さ
せつつ、230MPaの圧力で圧縮成形し、幅10mm
×高さ15mm×長さ20mmの成形体を得た。The obtained R-Fe-B-based alloy powder material was compression-molded at a pressure of 230 MPa using an electric press while orienting in a magnetic field of about 0.8 MA / m, and the width was 10 mm.
A molded article having a height of 15 mm and a length of 20 mm was obtained.
【0069】得られた成形体をAr雰囲気中で約108
0℃にて約1時間焼結し、次いでAr雰囲気中で約60
0℃にて、約1時間、時効処理を行って焼結磁石を得
た。The obtained molded product was placed in an Ar atmosphere at about 108
Sinter at 0 ° C for about 1 hour, then in Ar atmosphere for about 60 hours.
Aging treatment was performed at 0 ° C. for about 1 hour to obtain a sintered magnet.
【0070】下記の表1に示した潤滑剤を粗粉末に表1
に示した添加量で微粉砕前に添加(表1中の前添加)
し、上述のジェトミル粉砕装置10を用いて、粗粉末を
微粉砕しながら、その表面に潤滑剤を付与した。実施例
4では、上記微粉砕工程で得られた潤滑剤で被覆された
微粉末に、更に、潤滑剤を添加した(表1中の後添
加)。The lubricants shown in Table 1 below were added to the coarse powder in Table 1.
Add before milling with the amount shown in (Prior addition in Table 1)
Then, while the coarse powder was finely pulverized using the above-mentioned jet mill pulverizer 10, a lubricant was applied to the surface thereof. In Example 4, a lubricant was further added to the fine powder coated with the lubricant obtained in the above-mentioned fine pulverization step (post-addition in Table 1).
【0071】得られた実施例1〜4および比較例による
合金粉末材料を30℃、相対湿度90%の雰囲気中に放
置し、最高到達温度を測定し、その温度上昇分を表1に
示した。この温度上昇の程度は、合金の酸化反応の程度
の指標となる。すなわち、合金粉末の表面が潤滑剤に被
覆されていないものは、酸化反応が進行し、温度が上昇
する。The obtained alloy powder materials according to Examples 1 to 4 and Comparative Example were left in an atmosphere at 30 ° C. and a relative humidity of 90%, the highest temperature was measured, and the temperature rise was shown in Table 1. . The degree of this temperature rise is an indicator of the degree of the oxidation reaction of the alloy. That is, when the surface of the alloy powder is not coated with the lubricant, the oxidation reaction proceeds, and the temperature rises.
【0072】また、実施例1〜4の合金粉末材料は大気
中で成形体を作製した。一方、比較例については、合金
粉末材料を大気に晒さないようして、上述の様に成形体
を作製した。それぞれ得られた成形体を焼結し、着磁す
ることによって得られた焼結磁石を得た。得られた焼結
磁石の磁気特性および焼結体中の残留炭素量の結果を表
1に合わせて示す。The alloy powder materials of Examples 1 to 4 were formed into compacts in the atmosphere. On the other hand, with respect to the comparative example, a compact was produced as described above without exposing the alloy powder material to the atmosphere. The obtained molded bodies were sintered and magnetized to obtain sintered magnets. Table 1 also shows the results of the magnetic properties of the obtained sintered magnet and the amount of residual carbon in the sintered body.
【0073】[0073]
【表1】 [Table 1]
【0074】表1に示した結果から明らかなように、実
施例1(ショウノウ0.1質量%を前添加)、実施例2
(エチルバニリン0.1質量%を前添加)、実施例3
(エチルバニリン0.05質量%とステアリン酸鉛0.
05質量%を前添加)および実施例4(エチルバニリン
0.2質量%を前添加、さらにカプロン酸メチルとイソ
パラフィンとを15:85で混合し混合液を後添加)の
合金粉末材料は、30℃、相対湿度90%の雰囲気中に
放置した際の温度上昇は僅かで、これらの粉末材料にお
いて、合金粉末の表面は、それぞれの潤滑剤によって安
定に被覆されていることが分かる。これに対し、比較例
(ステアリン酸鉛0.1質量%を前添加)では、30
℃、相対湿度90%の雰囲気中に放置すると、激しく酸
化反応が進み、発火するに至った。As is clear from the results shown in Table 1, Example 1 (0.1% by mass of camphor was added in advance) and Example 2
Example 3 (0.1% by mass of ethyl vanillin was added beforehand), Example 3
(0.05% by mass of ethyl vanillin and 0.1% of lead stearate).
Alloy powder material of Example 4 (0.2% by mass of ethyl vanillin was pre-added, and methyl caproate and isoparaffin were mixed at a ratio of 15:85, and the mixture was post-added). The temperature rise when left in an atmosphere at 90 ° C. and a relative humidity of 90% is slight, and it can be seen that in these powder materials, the surface of the alloy powder is stably coated with the respective lubricant. On the other hand, in Comparative Example (0.1% by mass of lead stearate was added in advance), 30
When left in an atmosphere at a temperature of 90 ° C. and a relative humidity of 90%, the oxidation reaction proceeded violently, leading to ignition.
【0075】表1に示した磁気特性(残留磁束密度B
r、保磁力Hcjおよび最大エネルギー積)および残留
炭素量の結果を見ても、実施例1〜4の特性は比較例の
特性と遜色なく、良好な特性を有することが分かる。ま
た、実施例1〜4の焼結体は大気中で成形したにも拘わ
らず、酸素含有量は2500ppm以下と低かった。The magnetic properties (residual magnetic flux density B
From the results of (r, coercive force Hcj and maximum energy product) and the amount of residual carbon, it can be seen that the characteristics of Examples 1 to 4 are not inferior to those of the comparative example and have good characteristics. Moreover, despite the fact that the sintered bodies of Examples 1 to 4 were molded in the atmosphere, the oxygen content was as low as 2500 ppm or less.
【0076】さらに、実施例1〜4の合金粉末材料の流
動性および成形性は良好で、プレス成形過程において、
欠けや割れの発生は少なかった。Further, the fluidity and formability of the alloy powder materials of Examples 1 to 4 were good, and during the press forming process,
The occurrence of chipping and cracking was small.
【0077】[0077]
【発明の効果】本発明によると、希土類合金粉末の表面
に酸化膜が形成されることが抑制され、且つ、優れた流
動性を有する希土類合金粉末材料の製造方法およびそれ
を用いた希土類合金焼結体の製造方法が提供される。According to the present invention, the formation of an oxide film on the surface of a rare earth alloy powder is suppressed, and a method of manufacturing a rare earth alloy powder material having excellent fluidity and rare earth alloy firing using the same are provided. Provided is a method for manufacturing a body.
【0078】本発明は、特に酸化しやすい、急冷法によ
って作製されたR−Fe−B系合金粉末を用いて焼結磁
石を製造する際に、特に効果を奏する。The present invention is particularly effective when producing a sintered magnet using an R-Fe-B-based alloy powder which is easily oxidized and produced by a quenching method.
【図1】本発明における微粉砕工程を行なうために好適
に用いられるジェットミル粉砕装置10の構成を示す模
式図である。FIG. 1 is a schematic diagram showing a configuration of a jet mill pulverizing apparatus 10 suitably used for performing a fine pulverizing step in the present invention.
10 ジェットミル粉砕装置 12 原料投入機 14 粉砕機 16 サイクロン分級機 18 回収タンク 20 原料タンク 22、38 モータ 24 供給機(スクリューフィーダ) 26 粉砕機本体 28 ノズル口 30 原料投入パイプ 32a、32b DESCRIPTION OF SYMBOLS 10 Jet mill crusher 12 Material input machine 14 Crusher 16 Cyclone classifier 18 Recovery tank 20 Material tank 22, 38 Motor 24 Feeder (screw feeder) 26 Crusher main body 28 Nozzle port 30 Material input pipe 32a, 32b
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4K017 AA04 BA06 BB12 CA07 DA04 EA03 EA09 EK07 4K018 AA27 BA18 BB04 BC12 BC29 BD01 KA45 5E040 AA04 BD01 CA01 HB03 HB17 5E062 CC05 CD04 CE04 CG02 CG03 ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4K017 AA04 BA06 BB12 CA07 DA04 EA03 EA09 EK07 4K018 AA27 BA18 BB04 BC12 BC29 BD01 KA45 5E040 AA04 BD01 CA01 HB03 HB17 5E062 CC05 CD04 CE04 CG02 CG03
Claims (12)
る工程と、 (b)常温で昇華性を有する固体の潤滑剤が存在する状
態で、前記粗粉砕粉末を微粉砕することによって、前記
潤滑剤によって表面が覆われた前記希土類合金の微粉末
から実質的に構成される粉末材料を調製する工程と、 を包含する、希土類合金粉末材料の調製方法。(A) preparing a coarsely ground powder of a rare earth alloy; and (b) finely pulverizing the coarsely ground powder in the presence of a solid lubricant having sublimability at room temperature. Preparing a powder material substantially composed of fine powder of the rare earth alloy whose surface is covered with the lubricant.
である、請求項1に記載の希土類合金粉末材料の調製方
法。2. The method for preparing a rare earth alloy powder material according to claim 1, wherein the rare earth alloy is an R—Fe—B based alloy.
0ppm以下の不活性ガス雰囲気中で実行される、請求
項1または2に記載の希土類合金粉末材料の調製方法。3. The method according to claim 1, wherein the step (b) comprises:
The method for preparing a rare earth alloy powder material according to claim 1 or 2, wherein the method is performed in an inert gas atmosphere of 0 ppm or less.
行される、請求項3に記載の希土類合金粉末材料の調製
方法。4. The method for preparing a rare earth alloy powder material according to claim 3, wherein step (b) is performed using a jet mill.
pm以下である、請求項1から4のいずれかに記載の希
土類合金粉末材料の調製方法。5. The oxygen content of the fine powder is 3000 p
The method for preparing a rare earth alloy powder material according to any one of claims 1 to 4, which is not more than pm.
機分子からなる、請求項1から5のいずれかに記載の希
土類合金粉末材料の調製方法。6. The method for preparing a rare earth alloy powder material according to claim 1, wherein the lubricant comprises an organic molecule having CH 3 at a terminal.
を準備する工程と、前記合金塊を水素吸蔵法によって粗
粉砕する工程とを包含する、請求項1から6のいずれか
に記載の希土類合金粉末材料の調製方法。7. The method according to claim 1, wherein the step (a) includes a step of preparing an alloy lump of the rare earth alloy and a step of coarsely pulverizing the alloy lump by a hydrogen storage method. Preparation method of rare earth alloy powder material.
た合金フレークである、請求項7に記載の希土類合金粉
末材料の調製方法。8. The method for preparing a rare earth alloy powder material according to claim 7, wherein the alloy ingot is an alloy flake produced by a quenching method.
は、2μm〜10μmの範囲内にある、請求項1から8
のいずれかに記載の希土類合金粉末材料の調製方法。9. The fine powder of the rare earth alloy has an average particle size in a range of 2 μm to 10 μm.
The method for preparing a rare earth alloy powder material according to any one of the above.
末材料に、さらに、カプロン酸メチルおよびカプリル酸
メチルの内の少なくとも1種を添加し、混合する工程を
包含する、請求項1から9のいずれかに記載の希土類合
金粉末材料の調製方法。10. The method according to claim 1, further comprising, after the step (b), adding at least one of methyl caproate and methyl caprylate to the rare earth alloy powder material, followed by mixing. The method for preparing a rare earth alloy powder material according to any one of the above.
方法で調製された希土類合金粉末材料を準備する工程
と、 (c)前記粉末材料をプレス成形することによって成形
体を得る工程と、 (d)前記成形体を焼結することによって焼結体を得る
工程と、 を包含する、希土類合金焼結体の製造方法。11. A step of preparing a rare earth alloy powder material prepared by the method according to any one of claims 1 to 10, and (c) a step of pressing the powder material to obtain a compact. (D) a step of obtaining a sintered body by sintering the molded body; and a method of producing a rare earth alloy sintered body.
合金焼結体を準備する工程と、 前記希土類合金焼結体を着磁する工程と、 を包含する、希土類焼結磁石の製造方法。12. A method for producing a rare earth sintered magnet, comprising: a step of preparing a rare earth alloy sintered body produced by the method of claim 11; and a step of magnetizing the rare earth alloy sintered body.
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| JP2001091012A JP2002285208A (en) | 2001-03-27 | 2001-03-27 | Method for preparing rare earth alloy powder material, and method for manufacturing rare earth alloy sintered compact using the same |
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