JPS5813602B2 - Reduction sintering method using induction heating of steel powder - Google Patents
Reduction sintering method using induction heating of steel powderInfo
- Publication number
- JPS5813602B2 JPS5813602B2 JP53029808A JP2980878A JPS5813602B2 JP S5813602 B2 JPS5813602 B2 JP S5813602B2 JP 53029808 A JP53029808 A JP 53029808A JP 2980878 A JP2980878 A JP 2980878A JP S5813602 B2 JPS5813602 B2 JP S5813602B2
- Authority
- JP
- Japan
- Prior art keywords
- steel powder
- reduction
- induction heating
- powder
- sintering method
- 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
Links
Landscapes
- Powder Metallurgy (AREA)
Description
【発明の詳細な説明】
鉄粉を製造する水噴霧法によるアトマイズ粉や、熱間圧
延時に多量に排出されるミルスケール等の表面には高温
からの急冷の際に、水および空気中の酸素との反応によ
って酸化被膜が形成される。Detailed Description of the Invention: The surface of atomized powder produced by the water spray method used to produce iron powder, mill scale, etc. discharged in large quantities during hot rolling, is exposed to water and oxygen in the air during rapid cooling from high temperatures. An oxide film is formed by the reaction with
この種の粉末を粉末治金に使用する場合には水素等の強
還元雰囲気気流の炉中で1000〜1200℃の温度で
長時間の還元工程を必要としている。When this type of powder is used in powder metallurgy, it requires a long reduction process at a temperature of 1000 to 1200° C. in a furnace with a strong reducing atmosphere such as hydrogen gas.
そしてこの方法では水素ガスの還元反応によって露点も
上昇するため、多量の還元ガスを流す必要があり、また
水素を主体とした還元炉では爆発の危険もあり、設備上
十分な管理も必要とする。In this method, the dew point also rises due to the reduction reaction of hydrogen gas, so it is necessary to flow a large amount of reducing gas, and there is a risk of explosion in a reduction furnace that uses hydrogen as its main component, so sufficient equipment management is required. .
工業的な還元炉の生産設備では連続式のベルト搬送装置
を使用し、炉入口には空気進入防止用のフレーム用水素
も多量に必要で、かつ高温における水素気流中のメッシ
ュベルトの耐久性もコストアップの原因となる。Industrial reduction furnace production equipment uses a continuous belt conveyor, and a large amount of hydrogen is required for the frame at the furnace inlet to prevent air from entering, and the durability of the mesh belt in the hydrogen stream at high temperatures is also limited. This causes an increase in costs.
またこれらの酸化物を還元する場合、Ni,Mo系の酸
化物は比較的還元しやすいが、Mn,Cr系の酸化物で
は自由エネルギが低く還元しにくく、最高1200℃程
度の還元炉では還元に数時間を要する。In addition, when reducing these oxides, Ni and Mo-based oxides are relatively easy to reduce, but Mn and Cr-based oxides have low free energy and are difficult to reduce, and cannot be reduced in a reduction furnace at a maximum temperature of about 1200°C. It takes several hours.
本発明の目的は、これらの問題点を解決または改良しよ
うとするもので、未還元粉を使用し成形体の還元と同時
に焼結をも行なって工程を短縮しようとするものである
。The purpose of the present invention is to solve or improve these problems, and to shorten the process by using unreduced powder and sintering the compact at the same time as reducing the compact.
本発明では表面に多量の酸化物を有する金属粉末の表層
部分に、1〜7%のフェノール樹脂を密着した状態で均
一にコーティングし酸化物とじかに接触させたレジンコ
ーテツドパウダ(R.C.P)とした後、2〜6 to
n/cm’の圧力で圧粉成形し、ついで200〜400
℃の温度で約5〜10分間キュアリングする。In the present invention, a resin coated powder (R.C. P), then 2 to 6 to
Compacting at a pressure of n/cm', then 200 to 400
Cure for about 5-10 minutes at a temperature of .
このキュアリングは加熱して樹脂をかためることで、次
工程の誘導加熱時の樹脂燃焼時の煤の発生を防止するこ
とと、加熱初期の樹脂軟化により磁気力方向に圧粉体が
変形するのを防止するために行なう。By heating and hardening the resin, this curing prevents the generation of soot during the resin combustion during induction heating in the next process, and also prevents the green compact from deforming in the direction of the magnetic force due to the softening of the resin in the initial heating stage. This is done to prevent
図面はキュアリング後の成形体の常温強度であるところ
のプレホーム加熱後の成形圧力に対するラトラー値を示
すもので、図中aはキュアリングなしの場合、bは20
0℃で5分間、Cは300℃で5分間、dは400℃で
5分間それぞれキュアリングを施した場合をそれぞれ示
す。The drawing shows the Rattler value for the molding pressure after heating the preform, which is the room temperature strength of the molded product after curing, where a is the case without curing and b is 20.
Curing was performed at 0° C. for 5 minutes, C at 300° C. for 5 minutes, and d at 400° C. for 5 minutes.
なおここで使用された鋼粉はMn 0.74%、Cr
O.81%の低合金鋼粉に樹脂燃焼後20%の残留炭素
が残るフェノール樹脂を2.5%表面にコーティングし
たものであり、また12.25φで7.5grを成形し
た。The steel powder used here contained 0.74% Mn and Cr.
O. It is made by coating the surface of 81% low-alloy steel powder with 2.5% phenolic resin, which leaves 20% residual carbon after burning the resin, and is molded to 7.5 gr with a diameter of 12.25.
図中5 ton/cm’、の成形圧力では、キュアリン
グなしでラトラー値2.5%に対して、300℃では0
.1%にまで向上していることがわかる。In the figure, at a molding pressure of 5 ton/cm', the Rattler value was 2.5% without curing, but at 300°C it was 0.
.. It can be seen that this has improved to 1%.
縦型搬送の誘導加熱装置では積み重ねられた被加熱体の
重量に十分耐えられるラトラー値が必要である。An induction heating device for vertical conveyance requires a Rattler value that can sufficiently withstand the weight of stacked objects to be heated.
なお上記フェノール樹脂はノボラツク型、ノボラツク+
へキサミン型、レゾール型のいずれでもよいが、ヘキサ
ミンを混合しないノボラツク型は臭気ガスの発生が少な
く、残留炭素量調整が容易、2段硬化が可能であること
によりレゾール型より有利である。The above phenolic resins are novolac type, novolac +
Either the hexamine type or the resol type may be used, but the novolac type without hexamine is more advantageous than the resol type because it generates less odor gas, the amount of residual carbon can be easily adjusted, and two-stage curing is possible.
なお、上記レジンコーテツドパウダは、鋼粉を130℃
〜160℃に加熱してからフェノール樹脂を投入し、約
30秒混練した後、振動コンベア上にて送風冷却しなが
ら分級(フルイにかける)することにより得られる。The above resin coated powder is made by heating steel powder to 130°C.
It is obtained by heating to ~160°C, adding phenol resin, kneading for about 30 seconds, and then classifying (passing through a sieve) while cooling with air on a vibrating conveyor.
上記キュアリング完了した成形体は100ヘルツから1
00キロヘルツの誘導加熱装置によって粒内に渦電流を
生じ昇温速度が加速され、約1〜4分後に1000〜1
400℃になり、3〜5分間保持することにより還元焼
結反応が完了する。The molded body after the above curing is 100 Hz to 1
An eddy current is generated in the grains by an induction heating device of 0.00 kHz, accelerating the temperature increase rate, and after about 1 to 4 minutes, the temperature rises to 1000 to 1
The reduction sintering reaction is completed by reaching 400° C. and maintaining it for 3 to 5 minutes.
金属粉末の表面に残留した樹脂分解後の炭素は、金属粉
表面の酸化物と強力に反応してCOの還元ガス雰囲気を
粒内に生成し、高温加熱状態とあいまって還元速度は進
行する。The carbon remaining on the surface of the metal powder after the resin decomposition reacts strongly with the oxide on the surface of the metal powder to generate a CO reducing gas atmosphere inside the particles, and the reduction rate progresses in conjunction with the high temperature heating state.
被加熱体とコイル間には反応ガスを排出させるためのN
2等の無酸化ガス雰囲気流を流す。Between the heated body and the coil is N to discharge the reaction gas.
Flow a non-oxidizing gas atmosphere flow of grade 2.
従来は還元ガスとして水素もしくはAxアンモニア分解
ガスを使用しているが、本発明方法では、反応ガスを速
やに排出させるだけでよい無酸化ガスでよく、流量は従
来より少なくかつ爆発等の危険性もなく管理もやりやす
い。Conventionally, hydrogen or Ax ammonia decomposition gas is used as the reducing gas, but in the method of the present invention, a non-oxidizing gas is sufficient as it only requires the reaction gas to be quickly discharged, and the flow rate is lower than before and there is no risk of explosion etc. It is simple and easy to manage.
コーティングされたフェノール樹脂には還元作用があり
、同時に還元後粉末内に残留する炭素の添加量を調整す
る加炭効果もあり、また圧粉成形時の粒子間の潤滑効果
、成形時の結合剤の効果も同時にかねそなえている多目
的効果を有する。The coated phenolic resin has a reducing effect, and at the same time has a carburizing effect that adjusts the amount of carbon remaining in the powder after reduction. It also has a lubricating effect between particles during compaction, and is a binder during compaction. It has a multipurpose effect that also has the following effects at the same time.
上記金属粉末の表層部分にコーティングするフェノール
樹脂の量は、1%以下では、圧粉成形後キュアリングす
るときの搬送時にカケなどが起きやすくなってハンドリ
ングに不便をきたし、一方これが7%以上になると、キ
ュアリング時にフェノール樹脂の分解により発生するガ
スのため成形体の崩壊が生じ好ましくない。If the amount of phenolic resin coated on the surface layer of the metal powder is less than 1%, chips will easily occur during transportation during curing after compaction, making handling inconvenient; In this case, the molded body collapses due to the gas generated by the decomposition of the phenol resin during curing, which is undesirable.
そしてこのフェノール樹脂の還元時の有効な残留炭素分
は、フェノール樹脂量を上記したように1〜7%に限定
すると、鉄粉の酸素を脱酸するには10〜60%の範囲
にあればよいことになる。If the amount of phenolic resin is limited to 1 to 7% as mentioned above, the effective residual carbon content during reduction of this phenolic resin must be in the range of 10 to 60% to deoxidize the oxygen of iron powder. It will be a good thing.
残留炭素分が10%未満では脱酸が不十分の場合が起こ
るし、60%以上では炭素分が多すぎ、焼結体の強度が
弱くなってしまう。If the residual carbon content is less than 10%, deoxidation may be insufficient, and if it is 60% or more, the carbon content is too large and the strength of the sintered body becomes weak.
以下に本発明の実施例を示すと、C:0.03%、Cr
:0.81%、Mn : 0.7 4%、MO : 0
.2 3%、Si:0.03%初期酸素量7 2 0
0 ppmの70メッシュアンダの未還元低合金鋼粉に
燃焼後の残留炭素量20%を含むノボラツク型フェノー
ル樹脂をホット法にて2.5%(重量%)鋼粉表面にコ
ーティングしてレジンコーテツドパウダとした後、4t
on/cm’の成形圧力にて内外径、高さが23φ×4
2φ×14.5の円筒を成形し300℃で5分間キュア
リング後、3KCの高周波誘導加熱装置に窒素の無酸化
雰囲気流中にセットした。Examples of the present invention are shown below. C: 0.03%, Cr
: 0.81%, Mn: 0.74%, MO: 0
.. 2 3%, Si: 0.03% initial oxygen amount 7 2 0
0 ppm unreduced low-alloy steel powder under 70 mesh is coated with 2.5% (wt%) novolac-type phenolic resin containing 20% residual carbon after combustion on the surface of the steel powder using a hot method. After making it into powder, 4t
The inner and outer diameter and height are 23φ x 4 at a molding pressure of on/cm'.
A cylinder of 2φ×14.5mm was formed and cured at 300° C. for 5 minutes, and then set in a 3KC high-frequency induction heating device in a non-oxidizing atmosphere of nitrogen.
通電後約3分にて1300℃にまで上昇し、これを約5
分間保持した後常温にまで冷却し、酸素量を測定し55
0ppmにまで低減したことを確認した。The temperature rises to 1300℃ in about 3 minutes after electricity is applied, and this temperature is increased to about 5℃.
After holding for a minute, it was cooled to room temperature and the amount of oxygen was measured.
It was confirmed that the amount was reduced to 0 ppm.
また焼結体強度を知るため圧管リングテストを行ない十
分な焼結強度( 5 0 kg/cm’ )を有するこ
とを確認した。In order to determine the strength of the sintered body, a pressure tube ring test was conducted and it was confirmed that the sintered body had sufficient sintering strength (50 kg/cm').
【図面の簡単な説明】
図面はプレホーム加熱後のラトラー値を示す線図である
。[BRIEF DESCRIPTION OF THE DRAWINGS] The drawing is a diagram showing the Rattler value after heating the preform.
Claims (1)
な残留炭素分を10〜60%含むフェノール樹脂を、1
〜7%の範囲で上記鋼粉の表面に均一に被覆配合してレ
ジンコーテツドパウダとした後圧粉成形し、成形体をキ
ュアリングした後、窒素等の無酸化雰囲気中で、100
0〜1400℃の温度に誘導加熱することによって還元
と同時に焼結を行なうことを特徴とする鋼粉の誘導加熱
による還元焼結法。 2 残留炭素分を10〜60%含むノボラツク型フェノ
ール樹脂を1〜7%の範囲で鋼粉の表面に均一に被覆配
合し、成形時の潤滑剤、結合剤、表面酸化物の還元およ
び金属粉末への加炭効果を有することを特徴とする特許
請求の範囲第1項記載の鋼粉の誘導加熱による還元焼結
法。 3 10分以下の短時の誘導加熱により初期酸素量5,
0 0 0 〜2 0,0 0 0 ppmが還元され
て低酸素量となすようにした特許請求の範囲第1項記載
の鋼粉の誘導加熱による還元焼結法。[Scope of Claims] 1. A phenolic resin containing 10 to 60% of residual carbon that is effective during reduction is added to unreduced water-atomized low-alloy steel powder.
The surface of the above steel powder is uniformly coated and blended in a range of ~7% to form a resin-coated powder, which is then compacted and cured.
A reduction sintering method by induction heating of steel powder, characterized in that reduction and sintering are performed simultaneously by induction heating to a temperature of 0 to 1400°C. 2 A novolac type phenolic resin containing 10 to 60% residual carbon is uniformly coated on the surface of steel powder in the range of 1 to 7%, and used as a lubricant, binder, and surface oxide reduction agent during molding, and as a metal powder. The reduction sintering method by induction heating of steel powder according to claim 1, which has a carburizing effect on steel powder. 3 Initial oxygen amount 5,
The reduction sintering method by induction heating of steel powder according to claim 1, wherein 0 0 0 to 2 0,0 0 0 ppm is reduced to provide a low oxygen content.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53029808A JPS5813602B2 (en) | 1978-03-17 | 1978-03-17 | Reduction sintering method using induction heating of steel powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53029808A JPS5813602B2 (en) | 1978-03-17 | 1978-03-17 | Reduction sintering method using induction heating of steel powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS54122611A JPS54122611A (en) | 1979-09-22 |
| JPS5813602B2 true JPS5813602B2 (en) | 1983-03-15 |
Family
ID=12286315
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP53029808A Expired JPS5813602B2 (en) | 1978-03-17 | 1978-03-17 | Reduction sintering method using induction heating of steel powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5813602B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS595503A (en) * | 1982-06-09 | 1984-01-12 | シビエ・プロジエクト−ル | Opposing headlight for vehicle |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5925902A (en) * | 1982-07-31 | 1984-02-10 | Sumitomo Electric Ind Ltd | Sintering method |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5222511A (en) * | 1975-08-14 | 1977-02-19 | Ntn Toyo Bearing Co Ltd | Wear resistant composite sliding member |
-
1978
- 1978-03-17 JP JP53029808A patent/JPS5813602B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS595503A (en) * | 1982-06-09 | 1984-01-12 | シビエ・プロジエクト−ル | Opposing headlight for vehicle |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS54122611A (en) | 1979-09-22 |
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