JPH0264391A - Vacuum heat treatment furnace - Google Patents
Vacuum heat treatment furnaceInfo
- Publication number
- JPH0264391A JPH0264391A JP21613288A JP21613288A JPH0264391A JP H0264391 A JPH0264391 A JP H0264391A JP 21613288 A JP21613288 A JP 21613288A JP 21613288 A JP21613288 A JP 21613288A JP H0264391 A JPH0264391 A JP H0264391A
- Authority
- JP
- Japan
- Prior art keywords
- tray
- gas
- furnace
- work
- heat treatment
- 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.)
- Granted
Links
- 238000010438 heat treatment Methods 0.000 title claims abstract description 38
- 239000007789 gas Substances 0.000 abstract description 55
- 238000006243 chemical reaction Methods 0.000 abstract description 16
- 239000011810 insulating material Substances 0.000 abstract description 10
- 238000001816 cooling Methods 0.000 abstract description 9
- 239000000112 cooling gas Substances 0.000 abstract description 5
- 238000007599 discharging Methods 0.000 abstract description 4
- 239000012535 impurity Substances 0.000 abstract description 4
- 230000002093 peripheral effect Effects 0.000 abstract description 2
- 238000000034 method Methods 0.000 abstract 1
- 238000007789 sealing Methods 0.000 abstract 1
- 239000000463 material Substances 0.000 description 28
- 239000012495 reaction gas Substances 0.000 description 13
- 239000000126 substance Substances 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000004904 shortening Methods 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 238000010583 slow cooling Methods 0.000 description 1
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、真空状態において処理物の熱処理を行う場合
に、ガスを使用する還元炉、反応炉等の真空熱処理炉に
関するものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a vacuum heat treatment furnace such as a reduction furnace or a reaction furnace that uses gas when heat treating a processed material in a vacuum state.
(従来の技術)
従来の真空熱処理炉の例について、添付図面により説明
すると、第4図は従来の真空熱処理炉の一例を示すもの
で内熱式炉である。ここで、真空熱処理炉は断熱材lの
内張された炉体2と、この炉体2内に配置されたヒータ
3と、同じくこの炉体2内に配置された処理物4を入れ
る為のトレイ5と、炉体2内へ還元あるいは反応ガスを
導入するガス導入系6及び炉体2内の気体を排出する排
気系7等から構成されている。そしてガス導入系6は還
元あるいは反応ガスの詰められたボンベ8がバルブ9、
流量調節弁IOを介して炉体2内のノズル11と接続さ
れている。一方、排気系7はメカニカルブースターポン
プ12と油回転ポンプ13が接続されており炉体2内の
気体を外部に排出する。(Prior Art) An example of a conventional vacuum heat treatment furnace will be explained with reference to the accompanying drawings. FIG. 4 shows an example of a conventional vacuum heat treatment furnace, which is an internal heating type furnace. Here, the vacuum heat treatment furnace includes a furnace body 2 lined with a heat insulating material 1, a heater 3 placed inside this furnace body 2, and a heater 3 placed inside this furnace body 2 for putting the processed material 4 therein. It is comprised of a tray 5, a gas introduction system 6 for introducing reducing or reaction gas into the furnace body 2, an exhaust system 7 for discharging the gas inside the furnace body 2, and the like. In the gas introduction system 6, a cylinder 8 filled with reducing or reaction gas is connected to a valve 9.
It is connected to a nozzle 11 in the furnace body 2 via a flow rate control valve IO. On the other hand, the exhaust system 7 is connected to a mechanical booster pump 12 and an oil rotary pump 13, and discharges the gas inside the furnace body 2 to the outside.
このような構成の熱処理炉において、処理物4をトレイ
5に入れた後、炉内に入れ十分排気系7で排気し、その
後ヒータ3で加熱を開始し、ガス導入系6より還元ある
いは反応ガスを導入する。In the heat treatment furnace configured as described above, the material to be treated 4 is placed in the tray 5, then placed in the furnace and sufficiently exhausted by the exhaust system 7. After that, heating is started by the heater 3, and reduction or reaction gas is supplied from the gas introduction system 6. will be introduced.
この導入されたガスは、図中矢印のように炉内を流れ処
理物4に作用して還元や各種反応(化学等)をした後、
排気系7より炉外へ排出される。This introduced gas flows through the furnace as shown by the arrow in the figure, acts on the treated material 4, undergoes reduction and various reactions (chemical, etc.), and then
It is discharged from the furnace through the exhaust system 7.
第5図は、従来の真空熱処理炉の他の構成例を示すもの
で外熱式炉である。ここで、真空熱処理炉は、断熱材l
と、ヒータ3と、この炉体(レトルト)2内に配置され
た処理物4を入れる為のトレイ5と、炉体(レトルト)
2内へ還元あるいは反応ガスを導入するガス導入系6及
び炉内の気体を排出する排気系7等から構成されている
。そして、ガス導入系6は還元あるいは反応ガスの詰め
られたボンベ8がバルブ9、流量調節弁10を介して炉
内のノズル11と接続されている。一方、排気系7はメ
カニカルブースターポンプ12と油回転ポンプ13が接
続されており炉内の気体を外部に排出する、
このような構成の熱処理炉においても、第4図に示すも
のと同様に、処理物4をトレイ5に入れた後、炉内に入
れ、十分排気系7で排気し、その後ヒータ3で加熱を開
始し、ガス導入系6より還元あるいは反応ガスを導入す
る。この導入されたガスは、図中矢印のように炉内を流
れ処理物4に作用して還元や各種反応(化学等)した後
、排気系7より炉外に排出される。FIG. 5 shows another configuration example of a conventional vacuum heat treatment furnace, which is an external heating type furnace. Here, the vacuum heat treatment furnace uses a heat insulating material l
, a heater 3, a tray 5 for holding the processed material 4 placed in the furnace body (retort) 2, and a furnace body (retort).
It is comprised of a gas introduction system 6 for introducing reducing or reaction gas into the furnace 2, an exhaust system 7 for exhausting the gas inside the furnace, and the like. In the gas introduction system 6, a cylinder 8 filled with reducing or reaction gas is connected to a nozzle 11 in the furnace via a valve 9 and a flow control valve 10. On the other hand, the exhaust system 7 is connected to a mechanical booster pump 12 and an oil rotary pump 13 to exhaust the gas inside the furnace to the outside. In a heat treatment furnace having such a configuration, as shown in FIG. 4, After the material to be treated 4 is placed in the tray 5, it is placed in the furnace and sufficiently exhausted by the exhaust system 7, after which heating is started by the heater 3, and a reducing or reaction gas is introduced from the gas introduction system 6. The introduced gas flows through the furnace as shown by the arrow in the figure, acts on the treated material 4, undergoes reduction and various reactions (chemical, etc.), and is then discharged from the furnace through the exhaust system 7.
(発明が解決しようとする課題)
ところで、上述した従来の真空熱処理炉では以下に述べ
るような欠点を有していた。(Problems to be Solved by the Invention) By the way, the above-mentioned conventional vacuum heat treatment furnace had the following drawbacks.
+11還元あるいは反応のためのガスを炉内全体に亘っ
て流すので、大量のガスが必要となり、消費するガスの
コストが嵩み、ランニングコスト全体が高価なものとな
っていた。+11 Since the gas for reduction or reaction is passed throughout the furnace, a large amount of gas is required, the cost of the gas consumed increases, and the overall running cost becomes expensive.
(2)第4図に示す内熱式の炉にあっては、炉体に使用
する断熱材の飛散が生じ、この飛散した断熱材が処理物
に混入して製品不良を発生させる原因となり問題であっ
た。そこで、断熱材を金属構成とする手段が考えられる
が、高温炉ではMo。(2) In the internal heating type furnace shown in Figure 4, the heat insulating material used in the furnace body scatters, and this scattered heat insulating material mixes into the processed material, causing product defects. Met. Therefore, it is possible to consider a method of making the heat insulating material metal, but Mo is used in high-temperature furnaces.
Ta、 W等の高価な材料を使う必要があるため真空熱
処理炉のイニシャルコストが高くなりすぎる欠点があっ
た。Since it is necessary to use expensive materials such as Ta and W, there is a drawback that the initial cost of the vacuum heat treatment furnace is too high.
(3)第5図に示す外熱式の炉にあっては、断熱材の処
理物への混入という上記欠点を防止するためには有効で
あるが、炉体(レトルト)材に高価な材料を使用しなけ
ればならず、設備のイニシャルコストが高くなるという
欠点があった。また、炉体(レトルト)材についても1
000℃以上では工業的に使用できるものは殆どなく、
温度的な制限があった。さらに、レトルトにひび割れが
発生すると、反応ガスに11□等を使用する場合には非
常に危険であった。(3) The external heating type furnace shown in Figure 5 is effective in preventing the above-mentioned drawback of insulating material being mixed into the processed material, but the furnace body (retort) material is made of expensive materials. had to be used, which had the disadvantage of increasing the initial cost of the equipment. Also, regarding the furnace body (retort) material, 1
There are almost no products that can be used industrially at temperatures above 000°C.
There were temperature restrictions. Furthermore, cracks in the retort would be very dangerous if 11□ or the like was used as the reaction gas.
(4)炉内に還元あるいは反応ガスを流す際に、トレイ
とトレイとの間及びトレイと周囲との間の隙間が一様で
ないためガス流量に差ができ、ガスの大量に流れるトレ
イとそうでないトレイとで反応速度に差ができるという
ことがあった。(4) When flowing reduction or reaction gas into the furnace, the gaps between the trays and between the trays and the surroundings are uneven, resulting in a difference in gas flow rate. There were cases where there was a difference in reaction speed depending on the tray that was not used.
(5)処理の終了後、処理物を冷却する際、処理物が粉
体等である場合、冷却ガスの流速が大きいと飛散してし
まうということがあった。このため、徐冷しなければな
らず、冷却時間に5〜lO時間程度かかり、生産性を著
しく低下させる要因ともなっていた。(5) When cooling the processed material after the completion of the treatment, if the processed material is powder or the like, it may scatter if the flow rate of the cooling gas is high. For this reason, slow cooling was required, and the cooling time took about 5 to 10 hours, which was a factor that significantly reduced productivity.
本発明の目的は、上述した従来の欠点に鑑みてなされた
もので、還元あるいは反応に使用するガスの量を大幅に
減少させることによりランニングコストを低減するとと
もに、処理物に断熱材等の不純物が混入することのない
真空熱処理炉を提供することにある。The purpose of the present invention has been made in view of the above-mentioned drawbacks of the conventional technology.It is an object of the present invention to reduce running costs by significantly reducing the amount of gas used for reduction or reaction, and to reduce impurities such as heat insulating materials in the processed material. The object of the present invention is to provide a vacuum heat treatment furnace that does not contain any contaminants.
(課屈を解決するための手段)
上記目的を達成するために、本発明の真空熱処理炉は、
密封可能なトレイ七、このトレイ内へガスを供給するガ
ス供給機構と、炉内へガスを供給するガス供給機構と、
トレイ内及び炉内からガスを排出するガス排出機構と、
トレイの周囲に配設された加熱機構とを具備しているこ
とを特徴としている。(Means for solving the burden) In order to achieve the above object, the vacuum heat treatment furnace of the present invention has the following features:
a sealable tray 7; a gas supply mechanism that supplies gas into the tray; and a gas supply mechanism that supplies gas into the furnace;
a gas exhaust mechanism that exhausts gas from inside the tray and inside the furnace;
It is characterized by comprising a heating mechanism disposed around the tray.
(作用)
このように、本発明の真空熱処理炉によればトレイを密
封可能とし、トレイの内部と外部に別々のガスを流せる
ようにするとともに、トレイの内部も真空排気できるよ
うに排出機構に接続されているため、トレイ内の処理物
の周囲のみに還元あるいは反応を流して効果的に処理を
行うことができる。また、トレイは密封されているので
、不純物の混入や飛散を防止できる。(Function) As described above, according to the vacuum heat treatment furnace of the present invention, the tray can be sealed, allowing separate gases to flow inside and outside the tray, and the exhaust mechanism is designed so that the inside of the tray can also be evacuated. Because they are connected, reduction or reaction can be carried out only around the object to be processed in the tray, allowing for effective processing. Furthermore, since the tray is sealed, it is possible to prevent impurities from entering or scattering.
(実施例)
以下、本発明の一実施例を添付図面にしたがって説明す
る。(Example) An example of the present invention will be described below with reference to the accompanying drawings.
第1図は本発明の真空)処理炉の一例を示す断面図であ
る。ここで、真空熱処理炉は断熱材20の内張された炉
体21と、この炉体21内に配置されたヒータ22と、
同じくこの炉体21内に配置された処理物23を入れる
為のトレイ24と、不活性ガスを導入するガス導入系2
5と、トレイ内へ還元あるいは反応ガスを導入するガス
導入系26と、炉内及びトレイ内の気体を排出する2系
統の排気系27.27′等から構成されている。そして
、ガス導入系26は還元あるいは反応ガスの詰められた
ボンベ28がバルブ29、流量調節弁30を介してトレ
イ内の吐出口31と接続されている。ガス導入系25は
不活性ガスの詰められたボンベ32がバルブ33、流量
調節弁34を介して炉内のノズル35と接続されている
。FIG. 1 is a sectional view showing an example of a vacuum processing furnace of the present invention. Here, the vacuum heat treatment furnace includes a furnace body 21 lined with a heat insulating material 20, a heater 22 disposed inside this furnace body 21,
Similarly, a tray 24 for holding the processed material 23 placed inside this furnace body 21 and a gas introduction system 2 for introducing an inert gas
5, a gas introduction system 26 for introducing reducing or reaction gas into the tray, and two exhaust systems 27 and 27' for discharging gas from the furnace and the tray. In the gas introduction system 26, a cylinder 28 filled with a reducing or reaction gas is connected to a discharge port 31 in the tray via a valve 29 and a flow control valve 30. In the gas introduction system 25, a cylinder 32 filled with inert gas is connected to a nozzle 35 in the furnace via a valve 33 and a flow control valve 34.
一方、排気系27.27゛ はメカニカルブースターポ
ンプ36.36′ と油回転ポンプ37.37°が直列
に接続されており炉内及びトレイ内の気体を外部へ排出
する。トレイ24.24°はトレイ支柱38a 、 3
8bの上に載置され、それぞれガス導入系26及び排気
系27と連通している。そして、トレイ24の一番上に
は蓋2taが載置され、トレイ24の凹部を閉じて、密
閉する。On the other hand, the exhaust system 27.27' has a mechanical booster pump 36.36' and an oil rotary pump 37.37' connected in series, and exhausts the gas inside the furnace and the tray to the outside. Tray 24.24° is tray support 38a, 3
8b, and communicate with the gas introduction system 26 and exhaust system 27, respectively. Then, a lid 2ta is placed on the top of the tray 24, and the recessed portion of the tray 24 is closed and hermetically sealed.
第2図は、本発明のトレイ24を示す一部切り欠き斜視
図である。トレイ24の一方の側壁にはガス導入系26
に接続されるための空洞24cが穿設されるとともに、
トレイ24の凹部に向かって吐出口31が複数個設けら
れている。また、トレイ24の反対側の側壁には吐出口
31から吐出されたガスを排出するための吐出口24b
が複数個設けられ、排気系27と接続される空洞24d
に連通している。トレイ24は複数個積み重ねることに
より上下の空[24C及び24dが連通してそれぞれガ
ス導入系26、排気系27と接続される。第1図の場合
は、3個のトレイ24を積み重ねた状態を示している。FIG. 2 is a partially cutaway perspective view showing the tray 24 of the present invention. A gas introduction system 26 is installed on one side wall of the tray 24.
A cavity 24c is bored for connection to the
A plurality of discharge ports 31 are provided toward the recessed portion of the tray 24. Further, a discharge port 24b for discharging the gas discharged from the discharge port 31 is provided on the opposite side wall of the tray 24.
A cavity 24d is provided with a plurality of cavities and is connected to the exhaust system 27.
is connected to. By stacking a plurality of trays 24, the upper and lower spaces [24C and 24d] communicate with each other and are connected to a gas introduction system 26 and an exhaust system 27, respectively. In the case of FIG. 1, a state in which three trays 24 are stacked is shown.
このような構成の真空熱処理炉において、炉外で処理物
23をトレイ24の凹部に入れた後、炉内に入れトレイ
支柱上にセットする。次に、2系統の排気系27.27
°で同時にトレイ24及び炉内の排気を行う。排出後、
ヒータ22で加熱しつつ、ガス導入系26により還元あ
るいは反応ガスをトレイ24内に導入する。この導入さ
れたガスは、図中矢印のようにトレイ24内を流れ、処
理物23に作用して還元や各種反応(化学等)した後、
排気系27により炉外へ排出される。この際、ガス導入
系25からも還元あるいは反応ガスを流してもよい。還
元あるいは反応ガスは吐出口31から均一に流れ出るの
で処理物23との反応を均一に行うことができる。つま
り、ガスがトレイ24内で均一に処理物と触れ合うので
、一部の反応が進みすぎたりすることはない。In the vacuum heat treatment furnace configured as described above, the workpiece 23 is placed in the recess of the tray 24 outside the furnace, and then placed inside the furnace and set on the tray support. Next, the two exhaust systems 27.27
At the same time, the tray 24 and the inside of the furnace are evacuated. After discharge,
A reducing or reaction gas is introduced into the tray 24 through a gas introduction system 26 while being heated by a heater 22 . This introduced gas flows within the tray 24 as shown by the arrow in the figure, acts on the processed material 23, undergoes reduction and various reactions (chemical, etc.), and then
The exhaust system 27 exhausts the gas out of the furnace. At this time, the reducing or reaction gas may also be flowed from the gas introduction system 25. Since the reducing or reaction gas uniformly flows out from the discharge port 31, the reaction with the processing material 23 can be performed uniformly. In other words, since the gas uniformly contacts the processed material within the tray 24, some reactions will not proceed too much.
処理の終了後、第3図に示すようにシャッター39を開
き、炉内に設けられた強制冷却機構41によりトレイ2
4の外周面に強制的に冷却ガスを流す。After the processing is completed, the shutter 39 is opened as shown in FIG. 3, and the tray 2 is
Cooling gas is forced to flow on the outer peripheral surface of 4.
この時、トレイ24は密封されているので、冷却ガスに
よりトレイ24内の処理物23が飛散するおそれはない
。At this time, since the tray 24 is sealed, there is no fear that the processing object 23 in the tray 24 will be scattered by the cooling gas.
一般に、還元あるいは反応を行う場合の処理物は表面積
を増し反応面積を増すために小粒や粉末の場合がおおい
。In general, the treated material for reduction or reaction is often in the form of small particles or powder in order to increase the surface area and increase the reaction area.
ここで冷却すべきものは、処理物であるが、熱容量はト
レイ24の方が極端に大きく、トレイ24を冷却すれば
、処理物を容易に冷却できる。このようにして、本実施
例では処理の終了後の冷却時間を大幅に短縮することが
できた。つまり、従来5〜9時間かかっていた冷却時間
を0.5〜1時間にすることができる。したがって、真
空熱処理炉の処理時間を短縮することにより生産性を向
上させることができる。What should be cooled here is the processed material, but the tray 24 has an extremely larger heat capacity, and if the tray 24 is cooled, the processed material can be easily cooled. In this way, in this example, the cooling time after completion of the treatment could be significantly shortened. In other words, the cooling time, which conventionally took 5 to 9 hours, can be reduced to 0.5 to 1 hour. Therefore, productivity can be improved by shortening the processing time of the vacuum heat treatment furnace.
冷却後、トレイ24.24°は炉外へ取り出され、次の
処理工程に備える。After cooling, the tray 24.24° is removed from the furnace and prepared for the next processing step.
(発明の効果)
以上詳細に説明したように、本発明に係る真空熱処理炉
は、反応効率が高〈従来の熱処理炉のように炉全体に還
元ガスあるいは反応ガスを大量に流す必要がないので、
トレイ中を流すガスは微1でよい。したがって、ランニ
ングコストの大幅な低減を図ることができる。(Effects of the Invention) As explained in detail above, the vacuum heat treatment furnace according to the present invention has high reaction efficiency. ,
The amount of gas flowing through the tray can be as small as 1. Therefore, running costs can be significantly reduced.
また、トレイの外周を流すガス量もトレイ内圧力よりト
レイ外圧力を低くして、トレイ内から外へガスが流れて
も支障がないため少量でよい。Further, the amount of gas flowing around the outer circumference of the tray may be small because the pressure outside the tray is lower than the pressure inside the tray, and there is no problem even if the gas flows from the inside of the tray to the outside.
さらに、処理物はトレイ内部に収納されているため加熱
、冷却中でも炉材(主に断熱材)からの不純物の混入の
ない純度の高い製品を製造できる。Furthermore, since the processed material is stored inside the tray, a highly pure product can be manufactured without contaminating impurities from the furnace material (mainly the insulation material) even during heating and cooling.
つまり、外熱式の炉でしか達成できなかった高品質の製
品が内熱式の炉で製造可能となり、真空熱処理炉のイニ
シャルコストの低減を図ることができる。In other words, high-quality products that could only be achieved with an external heating furnace can now be manufactured using an internal heating furnace, and the initial cost of the vacuum heat treatment furnace can be reduced.
さらにまた、外熱式の炉のように炉材に耐高熱性の特殊
材料を使う必要がないため、炉を製造する際のイニシャ
ルコストが高くなることはない。Furthermore, unlike external heating type furnaces, there is no need to use special materials with high heat resistance for the furnace material, so the initial cost of manufacturing the furnace does not increase.
一方、トレイ内に設けたガスの吐出口及び排出口により
トレイ内のガス流を均一にできるので還元等の反応を均
一にすることができる。On the other hand, since the gas flow in the tray can be made uniform by the gas discharge ports and exhaust ports provided in the tray, reactions such as reduction can be made uniform.
また、処理終了後の冷却時間を大幅に短縮することがで
きるため、サイクルタイムの短縮により生産性を向上で
きる。Furthermore, since the cooling time after the processing is completed can be significantly shortened, productivity can be improved by shortening the cycle time.
第1図〜第3図は本発明の一実施例を示すもので、第1
図は本発明の真空熱処理炉の一例を示す断面図、第2図
は真空熱処理炉に配置されるトレイの一部切り欠き斜視
図、第3図は熱処理の終了後のトレイ冷却原理を説明す
るための断面図、第4図は従来の真空熱処理炉の一例を
示す縦断面図、第5図は従来の真空熱処理炉の別の例を
示す縦断面図である。
図中、
20・・・・・・・・断熱材
21・・・・・・・・炉体
22・・・・・・・・ヒータ
23・・・・・・・・処理物
24・・・・・・・・トレイ
25.26 ・・・・ガス導入系
27.27° ・・・・排気系
28・・・・・・・・ボンベ
29.33・・・・・バルブ
30.34・・・・・流量調節弁
31・・・・・・・・吐出口
35・・・・・・・−ノズル
36・・・・・・・・メカニカルブースターポンプ
37・・・・・・・・油回転ポンプ
なお、図中、同一符号は同−又は相当部分を示している
。
第1図
特許出願人 日本真空技術株式会社
第2図
第4I21
第3図
第5図Figures 1 to 3 show one embodiment of the present invention.
The figure is a sectional view showing an example of the vacuum heat treatment furnace of the present invention, Figure 2 is a partially cutaway perspective view of a tray placed in the vacuum heat treatment furnace, and Figure 3 explains the principle of cooling the tray after the heat treatment is completed. 4 is a longitudinal sectional view showing an example of a conventional vacuum heat treatment furnace, and FIG. 5 is a longitudinal sectional view showing another example of a conventional vacuum heat treatment furnace. In the figure, 20...Insulating material 21... Furnace body 22... Heater 23... Processing material 24... ...Tray 25.26 ...Gas introduction system 27.27° ...Exhaust system 28 ...Cylinder 29.33 ...Valve 30.34... ...Flow rate control valve 31...Discharge port 35...-Nozzle 36...Mechanical booster pump 37...Oil rotation Pump In the drawings, the same reference numerals indicate the same or corresponding parts. Figure 1 Patent applicant: Japan Vacuum Technology Co., Ltd. Figure 2 Figure 4I21 Figure 3 Figure 5
Claims (1)
ス供給機構と、炉内へガスを供給するガス供給機構と、
トレイ内及び炉内からガスを排出するガス排出機構と、
トレイの周囲に配設された加熱機構とを具備しているこ
とを特徴とする真空熱処理炉。a sealable tray; a gas supply mechanism that supplies gas into the tray; and a gas supply mechanism that supplies gas into the furnace;
a gas exhaust mechanism that exhausts gas from inside the tray and inside the furnace;
A vacuum heat treatment furnace characterized by comprising a heating mechanism disposed around a tray.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63216132A JP2799172B2 (en) | 1988-08-30 | 1988-08-30 | Vacuum heat treatment furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63216132A JP2799172B2 (en) | 1988-08-30 | 1988-08-30 | Vacuum heat treatment furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0264391A true JPH0264391A (en) | 1990-03-05 |
JP2799172B2 JP2799172B2 (en) | 1998-09-17 |
Family
ID=16683765
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63216132A Expired - Fee Related JP2799172B2 (en) | 1988-08-30 | 1988-08-30 | Vacuum heat treatment furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2799172B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4864696B2 (en) * | 2003-04-23 | 2012-02-01 | ボルボ エアロ コーポレイション | Method and apparatus for reducing contamination of workpieces |
JP2014181882A (en) * | 2013-03-21 | 2014-09-29 | Ngk Insulators Ltd | Heat treatment device |
WO2019131791A1 (en) * | 2017-12-27 | 2019-07-04 | 株式会社米倉製作所 | Infrared baking device and electronic component baking method using same |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101675931B1 (en) * | 2016-02-02 | 2016-11-16 | (주)앤피에스 | Tray, apparatus for processing substrate and method using the same |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61164255U (en) * | 1985-04-01 | 1986-10-11 |
-
1988
- 1988-08-30 JP JP63216132A patent/JP2799172B2/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61164255U (en) * | 1985-04-01 | 1986-10-11 |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4864696B2 (en) * | 2003-04-23 | 2012-02-01 | ボルボ エアロ コーポレイション | Method and apparatus for reducing contamination of workpieces |
JP2014181882A (en) * | 2013-03-21 | 2014-09-29 | Ngk Insulators Ltd | Heat treatment device |
WO2019131791A1 (en) * | 2017-12-27 | 2019-07-04 | 株式会社米倉製作所 | Infrared baking device and electronic component baking method using same |
TWI756503B (en) * | 2017-12-27 | 2022-03-01 | 日商米倉製作所股份有限公司 | Infrared baking device and baking method of electronic part using the same |
Also Published As
Publication number | Publication date |
---|---|
JP2799172B2 (en) | 1998-09-17 |
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