JPS6124441B2 - - Google Patents

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Publication number
JPS6124441B2
JPS6124441B2 JP13471877A JP13471877A JPS6124441B2 JP S6124441 B2 JPS6124441 B2 JP S6124441B2 JP 13471877 A JP13471877 A JP 13471877A JP 13471877 A JP13471877 A JP 13471877A JP S6124441 B2 JPS6124441 B2 JP S6124441B2
Authority
JP
Japan
Prior art keywords
oil
chamber
sintering
vacuum
heat
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
Application number
JP13471877A
Other languages
Japanese (ja)
Other versions
JPS5468706A (en
Inventor
Shinichi Miura
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ricoh Co Ltd
Original Assignee
Ricoh Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Ricoh Co Ltd filed Critical Ricoh Co Ltd
Priority to JP13471877A priority Critical patent/JPS5468706A/en
Publication of JPS5468706A publication Critical patent/JPS5468706A/en
Publication of JPS6124441B2 publication Critical patent/JPS6124441B2/ja
Granted legal-status Critical Current

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  • Powder Metallurgy (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

(技術分野) 本発明は機械的強度がすぐれ精度の高い焼結体
を得るための製造方法に関するものである。 (従来技術) 一つの炉の中で焼結し種々の後処理を連続して
行うことは、例えば実公昭45−3532号公報、特公
昭45−13210号公報、実願昭50−100742号(実開
昭52−14312号)、特開昭50−25412号公報により
従来公知である。 しかし乍ら実公昭45−3532号公報に示された真
空焼結滲炭炉は滲炭性液体を炉内に導き、炉内に
設置した熱源によりガス化しているので滲炭層の
炭素濃度が他の固体滲炭に比べて高くなり、耐衝
撃性が悪く、滲炭層のはく離性が生じ易く、亀裂
が発生し易くなるので、滲炭ガスの活性程度を加
減した雰囲気中で拡散処理を行つて炭素濃度を調
節する後工程が必要となるので工程が複雑になる
という問題点があつた。 又特開昭45−13210号公報に示された組合わせ
炉は焼結区域に大気圧以上の圧力を発生させてい
るので、ガスと一緒に熱が外部に逃げ、1150℃に
なるのに1〜6時間もかゝり、更に雰囲気ガスに
より炉内が劣化するという問題点があつた。 又実願昭50−100742号(実開昭52−14312号)
に示された連続式真空処理装置は複数の独立した
真空室が夫々独立して真空排気し、搬送機構は各
室に独立して設置しているので構造が複雑になる
という問題点があつた。 又特開昭50−25412号公報に開示された加熱炉
内搬送装置は、被加熱体を炉室から炉室へ搬送す
る装置に関するものである。 (目 的) 本発明は、連続的に焼結→油焼入→含油を行な
うこと、特に真空破壊する前に製品を油に入れ、
油焼入するとともに真空を破壊する際に圧力が上
がるのを利用して含油を行ない焼入処理と含油処
理の各工程を同時処理し全工程を短縮化すること
を目的とするものである。 (構 成) 本発明は上記目的を達成するために1気圧より
も低い所定の圧力に減圧された減圧室内にて所定
温度に加熱して焼結を行う第1工程と、該減圧室
内にて所定温度迄降下させる第2工程と、更に該
減圧室内にて油中熱処理を行う第3工程と、油中
熱処理した製品を油中においたまま常圧に戻し含
油させる第4工程とよりなることを特徴とするも
のである。 第1図は本発明方法を実施する装置の一実施例
で、1は外気に連通した予備加熱室で煙突2が設
けられている。これは圧粉成形体成形時に混入さ
れたステアリン酸亜鉛等を飛ばすために設けられ
たものである。3は予備加熱室1に隣接した減圧
室で、その外壁所定位置に真空ポンプ4及び冷却
ガス送風装置5が設けられている。内部には予備
加熱室1の近傍にグラフアイトクロスからなる発
熱体6を設け、その上方にグラフアイトフエルト
数枚からなる断熱壁7で囲まれた加熱空間8が形
成され、その次に搬送コンベアー9が配置され、
その前方下方に焼入れ槽10が配置されている。
その下部に仕切壁11が摺動し得るように設けら
れ区割室12を形成し、該区割室12はバルブ1
3により外気と連通し得るようになつている。 次に本発明方法について一実施例をもちいて説
明する。先ず、圧粉成形体Wを予備加熱室にて
200℃〜800℃に加熱し圧粉成形体内の不純物や潤
滑剤を飛ばす。減圧室3は真空ポンプ4により
10-3Torr〜10-1Torr程度に減圧しておく。予備
加熱された圧粉成形体Wを減圧室3内の加熱空間
8に入れ1150℃に昇温する。この温度で約30分保
持する。次いで加熱空間8より出して搬送コンベ
アー9にのせ、数秒で焼入れ槽10に入れる。こ
の数秒間に1150℃で焼結された焼結体はA1変態
点以下の温度にならないように設定され800℃ま
で降温している。焼入れ槽10の中には油が入れ
られており、この油で急冷されて焼入れが行われ
る。次いで仕切壁11を摺動して開き、焼入れ槽
10を下方に移動してから仕切壁11を閉じ、バ
ルブ13を開いて区割室12を外気に連通する。
焼結体は油中に入つたまま常圧下におかれるので
焼結体内部に所定量の油が容易に浸透する。 本発明方法によると減圧室内で焼結を行うので
従来のように還元性ガスを流して酸化を防止する
必要がなく圧粉成形体を短時間に1200℃〜1300℃
に昇温することができ、1200℃以上の高温で繰返
し使用しても炉壁材を傷めることが少なく、第1
表に示す如く従来方法に比較し引張強度、延び等
の機械的性質を向上させることができ、又焼入れ
後の硬さも第2表に示す如く従来方法に比較して
硬くなつた。
(Technical Field) The present invention relates to a manufacturing method for obtaining a sintered body with excellent mechanical strength and high precision. (Prior art) Sintering in one furnace and performing various post-treatments continuously is described in, for example, Japanese Utility Model Publication No. 3532/1983, Japanese Patent Publication No. 13210/1983, and Japanese Utility Model Application No. 100742/1983 ( This is known from Japanese Utility Model Application Publication No. 52-14312) and Japanese Patent Application Publication No. 50-25412. However, in the vacuum sintering and decharring furnace disclosed in Publication No. 45-3532, the decarburizing liquid is introduced into the furnace and gasified by a heat source installed in the furnace, so that the carbon concentration in the decarburizing layer is lower than that of the charcoal layer. Compared to solid charcoal, it has poor impact resistance, and the charcoal layer is easily peeled off and cracks are easily generated. Therefore, the diffusion treatment is carried out in an atmosphere in which the degree of activation of the charcoal gas is controlled. There was a problem that the process became complicated because a post-process to adjust the carbon concentration was required. Furthermore, since the combination furnace shown in JP-A No. 45-13210 generates a pressure higher than atmospheric pressure in the sintering zone, heat escapes to the outside together with the gas, and the temperature rises to 1150℃. It took up to 6 hours to complete the process, and there was also the problem that the inside of the furnace deteriorated due to atmospheric gas. Also, Utility Application No. 1987-100742 (Utility Application No. 14312, Showa 52)
The continuous vacuum processing equipment shown in Figure 1 has multiple independent vacuum chambers that evacuate each chamber independently, and the transfer mechanism is installed independently in each chamber, resulting in a complicated structure. . Further, the heating furnace conveyance device disclosed in Japanese Patent Application Laid-Open No. 50-25412 relates to a device for conveying a heated object from a furnace chamber to a furnace chamber. (Purpose) The present invention involves sequentially performing sintering → oil quenching → oil impregnation, in particular, placing the product in oil before vacuum breaking.
The purpose of this method is to perform oil impregnation by utilizing the pressure that increases when the vacuum is broken during oil quenching, thereby shortening the entire process by performing the quenching and oil impregnation processes simultaneously. (Structure) In order to achieve the above object, the present invention includes a first step of heating to a predetermined temperature and sintering in a reduced pressure chamber reduced to a predetermined pressure lower than 1 atmosphere, and a first step of sintering in the reduced pressure chamber. It consists of a second step of lowering the temperature to a predetermined temperature, a third step of further performing heat treatment in oil in the reduced pressure chamber, and a fourth step of returning the heat-treated product to normal pressure while remaining in oil and impregnating it with oil. It is characterized by: FIG. 1 shows an embodiment of an apparatus for carrying out the method of the present invention, in which numeral 1 denotes a preheating chamber that communicates with the outside air, and a chimney 2 is provided therein. This was provided to blow away zinc stearate and the like mixed in during the compacting process. Reference numeral 3 denotes a decompression chamber adjacent to the preheating chamber 1, and a vacuum pump 4 and a cooling gas blower 5 are provided at predetermined positions on its outer wall. Inside, a heating element 6 made of graphite cloth is provided near the preheating chamber 1, and above it a heating space 8 is formed surrounded by a heat insulating wall 7 made of several pieces of graphite felt. 9 is placed,
A quenching tank 10 is arranged below the front.
A partition wall 11 is slidably provided in the lower part of the partition wall 11 to form a compartment 12, and the compartment 12 is connected to the valve 1.
3 allows communication with the outside air. Next, the method of the present invention will be explained using an example. First, the powder compact W is heated in a preheating chamber.
Heat to 200°C to 800°C to remove impurities and lubricant from the compacted body. The decompression chamber 3 is operated by a vacuum pump 4.
Reduce the pressure to about 10 -3 Torr to 10 -1 Torr. The preheated green compact W is placed in the heating space 8 in the vacuum chamber 3 and heated to 1150°C. Hold at this temperature for approximately 30 minutes. Then, it is taken out of the heating space 8, placed on a conveyor 9, and placed in a quenching tank 10 within a few seconds. During these few seconds, the temperature of the sintered body sintered at 1150°C was lowered to 800°C, which was set so that the temperature did not go below the A1 transformation point. Oil is placed in the quenching tank 10, and quenching is performed by quenching with this oil. Next, the partition wall 11 is slid open, the quenching tank 10 is moved downward, the partition wall 11 is closed, and the valve 13 is opened to communicate the divided chamber 12 with the outside air.
Since the sintered body is placed under normal pressure while immersed in oil, a predetermined amount of oil easily penetrates into the inside of the sintered body. According to the method of the present invention, sintering is carried out in a reduced pressure chamber, so there is no need to prevent oxidation by flowing reducing gas as in the conventional method, and the compacted product can be heated to 1200°C to 1300°C in a short time.
It is possible to raise the temperature to 1200℃ or higher, and even if used repeatedly at high temperatures of 1200℃ or more, there is little damage to the furnace wall material, making it the first
As shown in the table, mechanical properties such as tensile strength and elongation were improved compared to the conventional method, and the hardness after quenching was also higher than that of the conventional method, as shown in Table 2.

【表】【table】

【表】 又本発明は同一減圧室内で焼結工程、降温工
程、熱処理工程を連続して行つているので従来方
法に比較して焼結から熱処理迄の生産時間を著し
く短縮することができた。第2図は本発明方法に
よるヒートサイクル図、第3図は従来方法(例え
ば特公昭45−13210号公報)によるヒートサイク
ル図であるが両者を比較すると第3表に示す如く
本発明方法の生産時間が約50分であるのに対し従
来方法(例えば特公昭45−13210号公報)の生産
時間は330〜810分である。
[Table] Furthermore, since the present invention performs the sintering process, temperature cooling process, and heat treatment process continuously in the same vacuum chamber, the production time from sintering to heat treatment can be significantly shortened compared to conventional methods. . Fig. 2 is a heat cycle diagram according to the method of the present invention, and Fig. 3 is a heat cycle diagram according to the conventional method (for example, Japanese Patent Publication No. 13210/1982). Comparing the two, the production of the method according to the present invention is shown in Table 3. The production time is about 50 minutes, whereas the production time of the conventional method (for example, Japanese Patent Publication No. 13210/1983) is 330 to 810 minutes.

【表】 更に又本発明方法は減圧室内で加熱するので常
圧で加熱するのと比較して熱伝導よりも熱放射で
加熱される度合いが強いのでむらなく加熱できる
熱歪が少く、焼結処理後の精度を著しく高めるこ
とができる。
[Table] Furthermore, since the method of the present invention is heated in a reduced pressure chamber, compared to heating under normal pressure, the degree of heating is stronger by thermal radiation than by thermal conduction. The accuracy after processing can be significantly improved.

【表】 第4表はCu粉2%、Gr粉0.5%、Ni粉2%、残
りFe粉の粉体を5ton/cm2で押圧成形した120φの
歯車を本発明方法で焼結、熱処理した場合の寸法
精度の比較表である。 (効 果) 本発明によると1気圧よりも低い所定の圧力に
減圧された減圧室内にて所定温度に加熱して焼結
を行う第1工程と、該減圧室内にて所定温度迄降
下させる第2工程と、更に該減圧室内にて油中熱
処理を行う第3工程と、油中熱処理した製品を油
中においたまま常圧に戻し含油させる第4工程と
よりなることを特徴としているので真空破壊前に
製品を油に入れ、油焼入れするとともに真空を破
壊する際に、圧力が上るのを利用して含油を行な
い焼入れ処理と含油処理の各工程を同時に処理
し、全工程を短縮化できるという効果を有し、仕
切壁を摺動して区割室内で常圧に戻せば減圧室の
真空度を殆ど下げることがないので、次回の減圧
工程を能率よく行うことができる。
[Table] Table 4 shows a 120φ gear made by press molding powders of 2% Cu powder, 0.5% Gr powder, 2% Ni powder, and the rest Fe powder at 5ton/ cm2 , and sintered and heat treated using the method of the present invention. This is a comparison table of dimensional accuracy in the following cases. (Effects) According to the present invention, the first step is to perform sintering by heating to a predetermined temperature in a vacuum chamber reduced to a predetermined pressure lower than 1 atm, and the second step is to lower the temperature to a predetermined temperature in the vacuum chamber. It is characterized by two steps, a third step of performing heat treatment in oil in the vacuum chamber, and a fourth step of returning the heat-treated product to normal pressure while remaining in oil and impregnating it with oil. Before destruction, the product is placed in oil, oil quenched, and when the vacuum is broken, oil impregnation takes advantage of the increased pressure, allowing the quenching and oil impregnation processes to be performed simultaneously, shortening the entire process. With this effect, if the partition wall is slid to return the pressure within the compartment to normal pressure, the degree of vacuum in the decompression chamber will hardly be lowered, so the next depressurization process can be carried out efficiently.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明方法を実施する装置の一実施例
正断面図、第2図は本発明方法のヒートサイクル
を示す図、第3図は従来方法のヒートサイクルを
示す図である。 3……減圧室、4……真空ポンプ、8……加熱
空間、9……搬送コンベアー、10……焼入れ
槽。
FIG. 1 is a front sectional view of an embodiment of an apparatus for carrying out the method of the present invention, FIG. 2 is a diagram showing a heat cycle of the method of the present invention, and FIG. 3 is a diagram showing a heat cycle of a conventional method. 3... Decompression chamber, 4... Vacuum pump, 8... Heating space, 9... Transfer conveyor, 10... Quenching tank.

Claims (1)

【特許請求の範囲】[Claims] 1 気圧よりも低い所定の圧力に減圧された減圧
室内にて所定温度に加熱して焼結を行う第1工程
と、該減圧室内にて所定温度迄降下させる第2工
程と、更に該減圧室内にて油中熱処理を行う第3
工程と、油中熱処理した製品を油中においたまま
常圧に戻し含油させる第4工程とよりなる焼結体
の製造方法。
1 A first step of heating and sintering to a predetermined temperature in a reduced pressure chamber that has been reduced to a predetermined pressure lower than atmospheric pressure, a second step of lowering the temperature to a predetermined temperature in the reduced pressure chamber, and a second step of sintering the material in the reduced pressure chamber. The third step is heat treatment in oil.
and a fourth step of returning the heat-treated product in oil to normal pressure and impregnating it with oil.
JP13471877A 1977-11-11 1977-11-11 Preparation of sintered product Granted JPS5468706A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13471877A JPS5468706A (en) 1977-11-11 1977-11-11 Preparation of sintered product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13471877A JPS5468706A (en) 1977-11-11 1977-11-11 Preparation of sintered product

Publications (2)

Publication Number Publication Date
JPS5468706A JPS5468706A (en) 1979-06-02
JPS6124441B2 true JPS6124441B2 (en) 1986-06-11

Family

ID=15134966

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13471877A Granted JPS5468706A (en) 1977-11-11 1977-11-11 Preparation of sintered product

Country Status (1)

Country Link
JP (1) JPS5468706A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5845304A (en) * 1981-09-11 1983-03-16 Sumitomo Electric Ind Ltd Continuous vacuum sintering furnace

Also Published As

Publication number Publication date
JPS5468706A (en) 1979-06-02

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