JPH0798963B2 - Sintering furnace for rare earth magnet alloys - Google Patents
Sintering furnace for rare earth magnet alloysInfo
- Publication number
- JPH0798963B2 JPH0798963B2 JP61074024A JP7402486A JPH0798963B2 JP H0798963 B2 JPH0798963 B2 JP H0798963B2 JP 61074024 A JP61074024 A JP 61074024A JP 7402486 A JP7402486 A JP 7402486A JP H0798963 B2 JPH0798963 B2 JP H0798963B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- sintered
- sintering furnace
- sintering
- inner cylinder
- 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.)
- Expired - Fee Related
Links
Landscapes
- Powder Metallurgy (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は磁石合金,特に希土類磁石合金の焼結炉に関す
る。TECHNICAL FIELD The present invention relates to a sintering furnace for magnet alloys, especially rare earth magnet alloys.
(従来の技術) 従来の磁石合金等の焼結炉の構成は第2図で模式的に示
すように断熱材3の内側に発熱体2を設けその間に被焼
結体1を置き,その被焼結体の上下に熱の反射板4を配
してなる。この焼結炉は焼結に際して炉内を真空にする
か,不活性ガスを充たすかする。これは炉内雰囲気中に
含まれる酸素及びその他の活性ガス成分が被焼結体に吸
収されることを防ぐためである。通常被焼結体の体積は
炉内容積に比べて極めて小さいものであるため炉内に存
在し得る酸素等のガス成分が,比較的小さい被焼結体に
影響を与えることが大きかった。(Prior Art) As shown in FIG. 2, a conventional sintering furnace for magnet alloys has a heating element 2 provided inside a heat insulating material 3 and a sintered body 1 placed between them. Heat reflection plates 4 are arranged above and below the sintered body. In this sintering furnace, the inside of the furnace is evacuated or filled with an inert gas during sintering. This is to prevent oxygen and other active gas components contained in the furnace atmosphere from being absorbed by the body to be sintered. Since the volume of the sintered body is usually much smaller than the internal volume of the furnace, gas components such as oxygen that may exist in the furnace have a large effect on the relatively small sintered body.
ここで,例えば第2図に示すような構造を有する焼結炉
に存在し得る酸素量を,仮定数値を基に計算してみる。Here, for example, the amount of oxygen that can exist in the sintering furnace having the structure shown in FIG. 2 will be calculated based on the assumed numerical value.
先ず炉全体の体積を5立方メートル,被焼結体の重量を
50kg,1.25×10-2m3(ρ≒4.0g/cm3)とすれば炉との体
積比は400対1となる。次にリーク量を2lusec,そして焼
結サイクルを6時間とする。First, the volume of the entire furnace is 5 cubic meters, and the weight of the sintered body is
If it is 50 kg, 1.25 × 10 -2 m 3 (ρ≈4.0 g / cm 3 ), the volume ratio with the furnace will be 400: 1. Next, the leak amount is set to 2 lusec and the sintering cycle is set to 6 hours.
上記の仮定のもとに10-3Torrの時のO2量を計算すると
5m3の炉全体に含まれているO2量は1.8×10-2(gr)で
あり,50kgの被加熱物がすべてO2をトラップしたとすれ
ば被加熱物のO2量は0.36ppmとなる。しかしながら,例
えばSm-Co系磁石合金の様に,活性な金属を含む合金等
では,3000ppm程度の酸素が含まれているのが常で,原料
中の酸素量300〜400ppmを考慮すると,製造工程での酸
素混入量はきわめて多い。Based on 10 -3 O 2 amount when calculating the amount of O 2 contained in the entire furnace 5 m 3 when the Torr assumptions above are 1.8 × 10 -2 (gr), the heated object of 50kg O 2 amount of but the heated object if the trap all O 2 becomes 0.36 ppm. However, for example, alloys containing active metals, such as Sm-Co based magnet alloys, usually contain about 3000 ppm of oxygen, and considering the amount of oxygen in the raw material of 300 to 400 ppm, the manufacturing process The amount of oxygen mixed in is extremely large.
これは,主に,粉砕,成形工程で吸着したC−H−O化
合物が焼結昇温過程で成形体より放出されて,炉内の低
温部(炉壁反射板,断熱材等)にトラップされ,さらに
焼結温度までの昇温時,それがC,H,Oに分解し,再び被
加熱物に吸収されるためである。This is mainly because the C-H-O compound adsorbed in the crushing and molding process is released from the molded body in the sintering temperature rising process and trapped in the low temperature part (furnace wall reflection plate, heat insulating material, etc.) in the furnace. This is because when the temperature is raised to the sintering temperature, it decomposes into C, H, O and is absorbed again by the object to be heated.
(発明が解決しようとする問題点) 以上のような従来の焼結炉においては,焼結炉内容積と
被焼結体の体積(容積)との比が極めて大きいために,
焼結加熱中に被焼結体から放出される酸素等のガスが,
(脱ガスされない分)炉壁,断熱材などにトラップさ
れ,後に昇温過程で再びそれらから放出されて被焼結体
に吸収されることによって焼結体の特性に劣化をもたら
すという問題があった。(Problems to be Solved by the Invention) In the conventional sintering furnace as described above, since the ratio of the internal volume of the sintering furnace to the volume (volume) of the sintered body is extremely large,
Gases such as oxygen released from the sintered body during sintering heating
(Not degassed) There is a problem that the characteristics of the sintered body are deteriorated by being trapped in the furnace wall, heat insulating material, etc., and then released from them again during the temperature rising process and absorbed by the sintered body. It was
従って本発明の目的は,上記のような,不可避である被
焼結体からの酸素等のガスの放出があっても,焼結炉構
成材にトラップされて,再度放出される酸素量を極力小
ならしめ,被焼結体の特性劣化を防止することができる
焼結炉を提供することにある。Therefore, an object of the present invention is to minimize the amount of oxygen that is trapped in the sintering furnace constituents and is released again, even if the above-described inevitable release of gas such as oxygen from the body to be sintered. An object of the present invention is to provide a sintering furnace that can be made small and can prevent the deterioration of the characteristics of the material to be sintered.
(問題点を解決するための手段) 本発明による焼結炉においては,炉内に気密性の内筒を
設け,その内筒の内部に被焼結体を収容するようにし
た。また内筒の真空排気口近傍に酸素や水素等の活性ガ
スと反応すTi,Al等の金属からなるゲッターを配して被
焼結体から放出されるガスを捕捉するようにしてなる。(Means for Solving the Problems) In the sintering furnace according to the present invention, an airtight inner cylinder is provided in the furnace, and the body to be sintered is accommodated in the inner cylinder. Further, a getter made of a metal such as Ti or Al that reacts with an active gas such as oxygen or hydrogen is arranged near the vacuum exhaust port of the inner cylinder to capture the gas released from the sintered body.
(作用) 本発明においては,炉内に気密性の内筒を有し,その中
に被焼結体を収容するので,被焼結体の周囲の容積が従
来の炉内容積より小さいものとなる。この内筒の内部が
均熱ゾーンとなって焼結を行うこととなるが,焼結にあ
たり気密性内筒内部での容積と被加熱物との容積が近い
のでO2混入量が少ないこと,加熱脱ガス時,被加熱物
より内筒が高温のため,放出ガスが内筒に付着しにくい
こと,および真空排気口に設けたゲッターが放出ガスの
吸収および排気系からのO2等の戻りを防止することな
どにより,焼結体の物性を劣化させることがなくなる。(Operation) In the present invention, since the furnace has the airtight inner cylinder and the body to be sintered is housed therein, the volume around the body to be sintered is smaller than the conventional furnace volume. Become. The inside of this inner cylinder serves as a soaking zone for sintering. However, since the volume inside the airtight inner cylinder and the volume to be heated are close to each other during sintering, the amount of O 2 mixed is small, During heating degassing, the inner cylinder is hotter than the object to be heated, so the released gas is less likely to adhere to the inner cylinder, and the getter provided at the vacuum exhaust port absorbs the emitted gas and returns O 2 etc. from the exhaust system. By preventing this, the physical properties of the sintered body will not be deteriorated.
(実施例) 第1図は本発明の実施例を示し,5は発熱体2の内側に配
された気密性の内筒を示し,6はゲッターを示す。本発明
になる焼結炉は図示したように加熱室7,焼結室8,冷却室
9,及びそれらに夫々設けた真空引き装置10と被焼結体を
焼結室へ搬入しかつ搬出してきて冷却するのに働く,冷
却室内へ設けたエレベータ11からなる。断熱材3は,加
熱室7に配置されている。発熱体2は,断熱材3の内側
に配置されている。前記の気密性の内筒5は被焼結体の
外周面の極く近傍にまでその収容区画を狭めており,こ
のために被焼結体に対する均熱ゾーンが極端に狭められ
ている。その結果被焼結体が加熱されたときに放出され
る酸素等の活性ガスの滞留空間が小さくなること及び,
従来における焼結炉のように放出されたガスが発熱体や
断熱材に接することがないことから前記ガスのトラップ
量も少なくなる。(Embodiment) FIG. 1 shows an embodiment of the present invention, 5 indicates an airtight inner cylinder arranged inside the heating element 2, and 6 indicates a getter. The sintering furnace according to the present invention includes a heating chamber 7, a sintering chamber 8 and a cooling chamber as shown in the figure.
9, and a vacuuming device 10 provided in each of them, and an elevator 11 provided in the cooling chamber, which works to carry in and carry out the body to be sintered and cool it. The heat insulating material 3 is arranged in the heating chamber 7. The heating element 2 is arranged inside the heat insulating material 3. The airtight inner cylinder 5 has its accommodation compartment narrowed to a position very close to the outer peripheral surface of the body to be sintered, so that the soaking zone for the body to be sintered is extremely narrowed. As a result, the retention space of active gas such as oxygen released when the sintered body is heated is reduced, and
Since the released gas does not come into contact with the heating element or the heat insulating material as in the conventional sintering furnace, the amount of trapping of the gas is reduced.
ここで上記と同じような仮定にたって,第1図で示すよ
うな構造における酸素量について試算してみると,内筒
体積を0.2m2,被焼結体重量を50kg,1.25×10-2m3(ρ≒
4.0g/cm3)とすれば内筒と被焼結体との体積比は約16対
1と極めて小さくなる。また真空洩れはないものとすれ
ば10-3Torrの時のO2量を計算すると,機密性内筒に含
まれているO2量は7.5×10-5(gr)あり,50kgの被焼結
体がすべてO2をトラップしたとすれば,1.5×10-3ppmの
O2量がある。この量は上記の従来例に比較すると非常
に少ない量である。Here, based on the same assumptions as above, a trial calculation of the oxygen content in the structure shown in Fig. 1 shows that the inner cylinder volume is 0.2 m 2 , the weight of the sintered body is 50 kg, and 1.25 × 10 -2. m 3 (ρ≈
If it is 4.0 g / cm 3 ), the volume ratio between the inner cylinder and the body to be sintered is about 16 to 1, which is extremely small. Further, when calculating the amount of O 2 when the 10 -3 Torr Assuming no leakage vacuum, the amount of O 2 contained in the confidentiality inner cylinder is 7.5 × 10 -5 (gr), the bake 50kg if sintered body was trapped all O 2, there is O 2 amount of 1.5 × 10 -3 ppm. This amount is very small compared to the above-mentioned conventional example.
次に,従来の焼結炉および本発明による気密性内筒をも
つ焼結炉によって熱処理した被焼結体のO2量を以下に
示す 上記の実施例より,従来よりも本発明での熱処理の方が
O2量が1/3以下になっていることがわかる。よって炉
壁,発熱体,反射板,断熱材等からの放出ガスを極力抑
えた,更にゲッタ効果のすぐれた炉の構造であることが
言える。Next, the amount of O 2 of the sintered body that has been heat-treated in the conventional sintering furnace and the sintering furnace having the airtight inner cylinder according to the present invention is shown below. From the above examples, it can be seen that the heat treatment in the present invention has an O 2 amount of 1/3 or less than that in the conventional case. Therefore, it can be said that the structure of the furnace has an excellent getter effect, in which the gas released from the furnace wall, heating element, reflector, heat insulating material, etc. is suppressed as much as possible.
又,Sm-Co系磁石合金の焼結による被焼結体の重量の減少
率を比較すると次の様になる。Further, the weight reduction rate of the sintered body due to the sintering of the Sm-Co magnet alloy is compared as follows.
次に本発明による希土類磁石合金の焼結方法について説
明すると,先ず被焼結体1を冷却室9で常温下で脱ガス
を行い,エレベータ11により被焼結体1を加熱室7に設
けた気密性の内筒5内に装填させ,真空引き装置を作動
し,金属からなるゲッターを加熱し,発熱体2により被
焼結体を徐昇法により加熱し,被焼結体から放出される
ガスを除去し,焼結を進め,そして最後に所定時間の焼
結を終えた被焼結体を冷却室へ降ろして急冷する。この
場合のゲッターとしては酸素,水素,窒素等のガスと活
性に反応するTi,Al,Caなどを原料とする板状の金属から
なるものが用いられる。本発明の気密性内筒をもつ焼結
炉では,真空排気口に設けたゲッターが放出ガスの吸収
および排気系からのO2等の戻りを防止するため,被焼
結体に吸収されるO2は全くなくきわめてクリーンな焼
結が可能である。 Next, a method of sintering a rare earth magnet alloy according to the present invention will be described. First, the sintered body 1 is degassed in the cooling chamber 9 at room temperature, and the sintered body 1 is provided in the heating chamber 7 by the elevator 11. The gas is discharged from the body to be sintered by loading it into the airtight inner cylinder 5, operating the vacuuming device, heating the getter made of metal, and heating the body to be sintered by the heating element 2 by the gradually increasing method. The sintered body is removed, the sintering is advanced, and finally the body to be sintered, which has been sintered for a predetermined time, is lowered into the cooling chamber and rapidly cooled. In this case, a getter made of a plate-shaped metal made of Ti, Al, Ca, or the like, which is a material that reacts actively with a gas such as oxygen, hydrogen, or nitrogen, is used. In the sintering furnace having the airtight inner cylinder of the present invention, the getter provided at the vacuum exhaust port absorbs the released gas and prevents the return of O 2 and the like from the exhaust system, so that the O 2 absorbed by the sintered body is absorbed. There is no 2 and extremely clean sintering is possible.
また,Sm-Co系磁石合金の様に,蒸気圧の高い元素を含む
合金の焼結の場合,本発明の焼結炉は炉内実効容積が小
さい為,金属の蒸発を抑える効果,仮に蒸発してもSmを
ゲッター部に埋積させる事ができるため,炉の維持上,
きわめて有利になる等の特長を有する。Further, in the case of sintering an alloy containing an element having a high vapor pressure, such as an Sm-Co magnet alloy, the sintering furnace of the present invention has a small effective volume in the furnace. Even if Sm can be buried in the getter,
It has features such as being extremely advantageous.
更に,本発明による焼結炉は希土類系の合金であればSm
-Co系,Gd-Co系,Tb-Co系を問わず全て有効に働くもので
ある。Furthermore, if the sintering furnace according to the present invention is a rare earth alloy, Sm
It works effectively regardless of -Co system, Gd-Co system, and Tb-Co system.
(効果) 以上説明したように,本発明による焼結炉によれば,希
土類磁石合金の焼結時に,焼結体の物性を損う酸素等の
ガスを吸収することがなくなり,物性の安定した焼結体
を得ることができる効果が得られる。(Effects) As described above, according to the sintering furnace of the present invention, when the rare earth magnet alloy is sintered, it does not absorb a gas such as oxygen that impairs the physical properties of the sintered body, and the physical properties are stable. The effect that a sintered body can be obtained is obtained.
第1図は本発明による焼結炉の側断面, 第2図は従来の焼結炉の側断面を示す模式図である。 図中 1……被焼結体,2……発熱体,3……断熱材,4……反射
板,5……内筒,6……ゲッター,7……加熱室,9……冷却
室,10……真空引き装置,11……エレベータ。FIG. 1 is a side view of a sintering furnace according to the present invention, and FIG. 2 is a schematic view showing a side section of a conventional sintering furnace. In the figure 1 …… Sintered body, 2 …… Heating element, 3 …… Insulation material, 4 …… Reflector, 5 …… Inner cylinder, 6 …… Getter, 7 …… Heating chamber, 9 …… Cooling chamber , 10 ... vacuum evacuation device, 11 ... elevator.
Claims (1)
熱材の内側に配置されている発熱体と、この発熱体の内
側に配置され被焼結体を収容する一端開口の内筒と、こ
の内筒の開口部の近くに配置され酸素および水素等の活
性ガスと反応するゲッターとを備えていることを特徴と
する希土類磁石合金の焼結炉。1. A heat insulating material disposed in a heating chamber, a heat generating element disposed inside the heat insulating material, and an inner cylinder having one end opening which is disposed inside the heat generating element and accommodates a body to be sintered. And a getter which is disposed near the opening of the inner cylinder and which reacts with an active gas such as oxygen and hydrogen, and a sintering furnace for rare earth magnet alloys.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61074024A JPH0798963B2 (en) | 1986-03-31 | 1986-03-31 | Sintering furnace for rare earth magnet alloys |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61074024A JPH0798963B2 (en) | 1986-03-31 | 1986-03-31 | Sintering furnace for rare earth magnet alloys |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62230901A JPS62230901A (en) | 1987-10-09 |
| JPH0798963B2 true JPH0798963B2 (en) | 1995-10-25 |
Family
ID=13535140
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61074024A Expired - Fee Related JPH0798963B2 (en) | 1986-03-31 | 1986-03-31 | Sintering furnace for rare earth magnet alloys |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0798963B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TW436526B (en) * | 1998-07-28 | 2001-05-28 | Kawasaki Steel Co | Box annealing furnace, method for annealing metal sheet using the same, and annealed metal sheet |
| JP4581449B2 (en) * | 2004-03-23 | 2010-11-17 | 日立金属株式会社 | Manufacturing method of rare earth sintered magnet |
| JP5094031B2 (en) * | 2006-03-23 | 2012-12-12 | 大平洋金属株式会社 | Method for producing scandium-containing alloy |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS567831Y2 (en) * | 1975-12-04 | 1981-02-20 | ||
| JPS5981029U (en) * | 1982-11-25 | 1984-05-31 | 日本電気ホームエレクトロニクス株式会社 | hearth tube |
-
1986
- 1986-03-31 JP JP61074024A patent/JPH0798963B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62230901A (en) | 1987-10-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US8375891B2 (en) | Vacuum vapor processing apparatus | |
| EP1160820A1 (en) | Combination of materials for the low temperature triggering of the activation of getter materials and getter devices containing the same | |
| CA1051507A (en) | Gas discharge display panel fabrication | |
| CA2581860A1 (en) | Method of controlling the oxygen content of a powder | |
| CN110106334B (en) | Device and method for continuous grain boundary diffusion and heat treatment | |
| JPH0798963B2 (en) | Sintering furnace for rare earth magnet alloys | |
| GB2607681A (en) | Method for heat treating an object | |
| US4415385A (en) | Diffusion of impurities into semiconductor using semi-closed inner diffusion vessel | |
| JPH0587459A (en) | Vacuum heat treating furnace | |
| JPH10172978A (en) | Substrate processor | |
| JPH09111309A (en) | Continuous sintering furnace | |
| JPS58100403A (en) | Method of sintering rare-earth cobalt magnet | |
| US2456968A (en) | Process for outgassing photocells containing antimony | |
| JP2684456B2 (en) | Heat treatment equipment | |
| GB1452779A (en) | Getter devices | |
| JPH05299364A (en) | Trap device | |
| JPH0684877A (en) | Method and apparatus for drying Si wafer storage case | |
| JP3100528B2 (en) | Baking method of insulated container | |
| JP3419414B2 (en) | Exhaust mechanism of sputtering equipment | |
| JP3176104B2 (en) | Semiconductor manufacturing equipment | |
| JP2581489B2 (en) | Cooler and method of manufacturing the same | |
| CN109735687B (en) | Device and method for continuously performing grain boundary diffusion and heat treatment | |
| KR100270422B1 (en) | Apparatus for heat treatment | |
| JPS63253623A (en) | Ion implantation apparatus | |
| WO1994018695A1 (en) | Apparatus for heat treatment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |