JPH0552485A - Vacuum heating furnace and vacuum heating method - Google Patents

Vacuum heating furnace and vacuum heating method

Info

Publication number
JPH0552485A
JPH0552485A JP3242638A JP24263891A JPH0552485A JP H0552485 A JPH0552485 A JP H0552485A JP 3242638 A JP3242638 A JP 3242638A JP 24263891 A JP24263891 A JP 24263891A JP H0552485 A JPH0552485 A JP H0552485A
Authority
JP
Japan
Prior art keywords
furnace shell
vacuum
water
furnace
heating
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
Application number
JP3242638A
Other languages
Japanese (ja)
Other versions
JP3163676B2 (en
Inventor
Shinobu Inuzuka
忍 犬塚
Yoichi Nakanishi
洋一 中西
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.)
Daido Steel Co Ltd
Original Assignee
Daido Steel 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 Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP24263891A priority Critical patent/JP3163676B2/en
Publication of JPH0552485A publication Critical patent/JPH0552485A/en
Application granted granted Critical
Publication of JP3163676B2 publication Critical patent/JP3163676B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Landscapes

  • Muffle Furnaces And Rotary Kilns (AREA)
  • Furnace Details (AREA)
  • Powder Metallurgy (AREA)

Abstract

PURPOSE:To prevent the generation of preclusion against the increasing of the degree of vacuum due to the evaporation of adhered water by a method wherein the adhesion of water to the internal surface of a furnace shell due to the condensation of water vapor is prevented by keeping the temperature of the furnace shell through a temperature keeping means when the furnace shell is evacuated and a work to be treated is heated. CONSTITUTION:A vacuum device 17 is operated and the inside of a furnace shell 2 is evacuated while a heater 12 is excited and the heating of a work 31 to be treated is started. Heat medium, such as hot-water or the like, is conducted through a water-cooled jacket, for example, as the temperature keeping means for the furnace shell 2, which keeps the furnace shell at a predetermined temperature, whereby the internal surface of the furnace shell is retained at a temperature precluding the condensation of water vapor even when the water vapor, generated from the work 31 to be treated, has arrived at the vicinity of the same. According to this method, water vapor, evaporated from the work 31 in accordance with the heating of the same, is discharged out of the furnace shell 2 through a discharging pipeline 18 without being condensed whereby the water vapor is removed as condensed water by a condenser 19 before arriving at the vacuum device 17. Accordingly, moisture will never arrive at the vacuum device 17 and the deterioration of the vacuum device 11 can be prevented.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は真空加熱炉及び真空加熱
方法に関し、特に加熱によって水分が蒸発する処理品の
加熱に好適な真空加熱炉及び真空加熱方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vacuum heating furnace and a vacuum heating method, and more particularly to a vacuum heating furnace and a vacuum heating method suitable for heating a processed product whose moisture is evaporated by heating.

【0002】[0002]

【従来の技術】上記のような処理品を真空状態で加熱す
る場合、処理品を炉内に入れ炉内を真空排気すると共に
処理品を加熱する。この場合、加熱に伴い処理品から水
分が蒸発する。その蒸気は炉殻の内面付近に到達すると
凝縮し、炉殻内面に水が付着する。この水は、真空排気
に伴なう炉内の減圧や処理品の加熱に伴なう余熱によっ
て蒸発し減少する。
2. Description of the Related Art When a processed product as described above is heated in a vacuum state, the processed product is placed in a furnace, the inside of the furnace is evacuated, and the processed product is heated. In this case, water is evaporated from the treated product as it is heated. When the steam reaches near the inner surface of the furnace shell, it condenses and water adheres to the inner surface of the furnace shell. This water is evaporated and reduced due to the decompression in the furnace due to the vacuum exhaust and the residual heat accompanying the heating of the processed product.

【0003】[0003]

【発明が解決しようとする課題】しかし上記のように内
面に付着した水の蒸発の場合、蒸発に伴ない熱を奪うの
で水の温度が下がり(場合によっては凍結する)、蒸発
速度が遅くて全てが蒸発するのに長時間を要する。とこ
ろで上記のように処理品の水分が蒸発したり炉殻内面に
付着した水が蒸発する間は、炉内の真空度はそれらの蒸
発による蒸気圧で規制され、良い真空度にならない。従
って、上記のように内面に付着した水の蒸発に長時間を
要すると、処理品からの蒸発が済んでしまっても上記内
面に付着した水が蒸発してしまうまでは炉内を所定の高
真空度まで上昇させることが困難で、処理品の所定の高
真空度の状態での加熱の開始が非常に遅れてしまう問題
点があった。
However, in the case of evaporation of the water adhering to the inner surface as described above, the temperature of the water is lowered (freezing in some cases) because the heat is removed along with the evaporation, and the evaporation rate is slow. It takes a long time for everything to evaporate. By the way, while the water content of the treated product evaporates or the water adhering to the inner surface of the furnace shell evaporates as described above, the degree of vacuum in the furnace is regulated by the vapor pressure due to the evaporation, and a good degree of vacuum cannot be obtained. Therefore, if it takes a long time to evaporate the water adhering to the inner surface as described above, even if the water adhering to the inner surface evaporates even if evaporation from the treated product is completed, There is a problem that it is difficult to raise the degree of vacuum to a high degree, and the start of heating of the processed product in a state of a predetermined high degree of vacuum is extremely delayed.

【0004】また処理品を真空状態で加熱する場合に、
炉殻内に前の処理品の処理の工程で生じた水が溜まって
いると、その水の蒸発による蒸気圧によって炉殻内の真
空度が規制され、良い真空度にならないという問題点が
あった。
When the processed product is heated in a vacuum state,
If water generated in the process of treating the previous treated product is accumulated in the furnace shell, the vapor pressure due to the evaporation of the water regulates the vacuum degree in the furnace shell, and there is a problem that a good vacuum degree cannot be obtained. It was

【0005】本願発明は上記従来技術の問題点(技術的
課題)を解決する為になされたもので、炉殻内面付近で
蒸気が凝縮して炉殻内面に水が付着することを防止でき
るようにして、所定の真空状態での処理品の加熱を迅速
に開始できるようにした真空加熱装置、及び、炉殻内の
水を予め排出して、良好な真空度の状態での加熱を行い
得るようにした真空加熱方法を提供することを目的とし
ている。
The present invention has been made to solve the above-mentioned problems (technical problems) of the prior art, and it is possible to prevent steam from condensing and water adhering to the inner surface of the furnace shell near the inner surface of the furnace shell. Then, the vacuum heating device that can quickly start the heating of the processed product in a predetermined vacuum state, and the water in the furnace shell can be discharged in advance to perform the heating in the state of a good vacuum degree. It is an object of the present invention to provide such a vacuum heating method.

【0006】[0006]

【課題を解決するための手段】上記目的を達成する為
に、本願発明における真空加熱炉は、内部を真空排気す
る為の真空装置が付設されている炉殻内に、炉殻の内部
に存置された処理品を加熱する為の加熱手段が備えられ
ている真空加熱炉において、上記炉殻の内面を、上記処
理品から生じて炉殻の内面付近に到達した蒸気の凝縮を
阻止する温度に保持する保温手段を備えたものである。
In order to achieve the above object, a vacuum heating furnace according to the present invention is installed inside a furnace shell provided with a vacuum device for evacuating the inside. In a vacuum heating furnace provided with heating means for heating the treated product, the inner surface of the furnace shell is set to a temperature at which condensation of vapor generated from the treated product and reaching the vicinity of the inner surface of the furnace shell is prevented. It is provided with a heat retaining means for holding.

【0007】又本願発明における真空加熱方法は、真空
装置が付設された炉殻内に処理品を存置させ、炉殻内を
真空排気し、処理品を加熱する真空加熱方法において、
上記炉殻内を真空排気するに当っては、炉殻内に溜まっ
た水を炉殻外に排出すると共に、炉殻内を真空排気する
ものである。
The vacuum heating method according to the present invention is a vacuum heating method in which a processed product is placed in a furnace shell provided with a vacuum device, the furnace shell is evacuated, and the processed product is heated.
When the inside of the furnace shell is evacuated, the water accumulated in the furnace shell is discharged to the outside of the furnace shell and the inside of the furnace shell is evacuated.

【0008】[0008]

【作用】真空加熱炉による処理品の加熱の場合、処理品
は炉殻内に存置され、炉殻内が真空排気されると共に処
理品の加熱が開始される。加熱によって処理品から水分
が蒸発すると、その蒸気は真空排気に伴ない炉殻外に排
出される。この場合、上記蒸気が炉殻の内面付近に到達
しても、その内面は蒸気の凝縮を阻止する温度に保たれ
ている為、その蒸気が凝縮して水が炉殻内面に付着する
ことはない。処理品からの水分の蒸発が終了すると炉内
真空度は所定の高真空度まで上昇され、その状態で処理
品の加熱が行なわれる。
When the processed product is heated by the vacuum heating furnace, the processed product is left in the furnace shell, the inside of the furnace shell is evacuated, and the heating of the processed product is started. When the water vaporizes from the treated product due to heating, the vapor is exhausted to the outside of the furnace shell along with vacuum evacuation. In this case, even if the steam reaches the vicinity of the inner surface of the furnace shell, the inner surface is kept at a temperature that prevents condensation of the steam, so that the steam is condensed and water does not adhere to the inner surface of the furnace shell. Absent. When the evaporation of water from the treated product is completed, the degree of vacuum in the furnace is raised to a predetermined high degree of vacuum, and the treated product is heated in that state.

【0009】[0009]

【実施例】以下本願の実施例を示す図面について説明す
る。図1、2において、1は真空加熱炉の一例としてバ
ッチ式の真空炉を示す。2は該真空における炉殻で、円
筒状の本体3と、その本体3の一方の端に連結した冷却
設備包囲壁3aと、それとは反対側の出入口に設けた扉4
とから構成してある。これらは何れも例えば水冷ジャケ
ットで構成される。5は断熱壁で、本体6とその本体6
の出入口に設けた扉7及びそれとは反対の側に設けられ
た扉8とから構成され、その内側の空間が熱処理室とな
っている。扉8は処理品の加熱時に閉ざされ冷却時に開
かれる。10は熱処理室内に設けられた載置台で、その上
側の空間が処理品の存置空間11となっている。12は上記
存置空間11の周囲に配設された加熱手段で、一例として
電熱ヒータが用いられ、断熱壁に取付けてある。尚13は
必要に応じて備えられるマッフルで、処理品の熱処理時
例えば脱ワックス、脱ガス時に発生する有害ガスによる
炉殻構成物質の汚染、破損の防止、或いは存置空間11で
の温度分布の良好化の為のものである。次に炉殻2の排
水構造を説明する。14は集水部で、炉殻2の本体3にお
いて最も低い位置に設けてある。15は集水部14の底壁に
設けた排水口で、ドレンバルブ16が付設してある。
Embodiments of the present invention will be described below with reference to the drawings. 1 and 2, reference numeral 1 denotes a batch type vacuum furnace as an example of the vacuum heating furnace. Reference numeral 2 denotes a furnace shell in the vacuum, which is a cylindrical main body 3, a cooling equipment surrounding wall 3a connected to one end of the main body 3, and a door 4 provided at an entrance on the opposite side.
It consists of and. Each of these is composed of, for example, a water cooling jacket. Reference numeral 5 is a heat insulating wall, and the main body 6 and the main body 6
The door is provided with a door 7 and a door 8 provided on the opposite side to the door 7, and the space inside is a heat treatment chamber. The door 8 is closed when the processed product is heated and opened when cooled. Reference numeral 10 is a mounting table provided in the heat treatment chamber, and the space above the mounting table is a storage space 11 for the processed product. Reference numeral 12 is a heating means arranged around the existing space 11, and an electric heater is used as an example, and is attached to the heat insulating wall. In addition, 13 is a muffle provided as necessary, for example, dewaxing during heat treatment of the processed product, prevention of contamination and damage of furnace shell constituents by harmful gas generated during degassing, or good temperature distribution in the storage space 11. It is for the purpose of conversion. Next, the drainage structure of the furnace shell 2 will be described. Reference numeral 14 denotes a water collecting portion, which is provided at the lowest position in the main body 3 of the furnace shell 2. Reference numeral 15 denotes a drain port provided on the bottom wall of the water collecting section 14, to which a drain valve 16 is attached.

【0010】次に図2に示される17は真空装置で、炉殻
2の内部を真空排気する為のものであり、油回転ポンプ
その他周知の真空ポンプが用いられる。18は炉殻2の内
部と真空装置17とを繋ぐ排気用管路であり、途中には凝
縮器19(例えば冷凍器)が介設してある。上記油回転ポ
ンプとして作動油の油水分離器を備えるものを用いる場
合は、上記凝縮器19は省略しても良い。尚図示はしない
が炉殻2には処理品の熱処理に応じた熱処理用のガス
(例えば水素、反応性ガス)を送入する為の図示外のガ
ス供給手段が接続してある。
Next, 17 shown in FIG. 2 is a vacuum device for evacuating the inside of the furnace shell 2, and an oil rotary pump or other well-known vacuum pump is used. Reference numeral 18 denotes an exhaust pipe line that connects the inside of the furnace shell 2 and the vacuum device 17, and a condenser 19 (for example, a refrigerator) is provided in the middle thereof. The condenser 19 may be omitted when an oil rotary pump equipped with a hydraulic oil separator is used as the oil rotary pump. Although not shown, the furnace shell 2 is connected to a gas supply means (not shown) for feeding a heat treatment gas (for example, hydrogen or a reactive gas) according to the heat treatment of the processed product.

【0011】次に再び図1において、21は処理品の周知
の冷却構造を示し、以下これについて説明する。22はク
ーラ、23は循環用のファンで、ファンモータ24によって
運転されるようになっている。25はモータカバーで、真
空保持用のものである。
Next, referring again to FIG. 1, reference numeral 21 denotes a known cooling structure for the processed product, which will be described below. 22 is a cooler, and 23 is a circulation fan, which is driven by a fan motor 24. 25 is a motor cover for holding a vacuum.

【0012】次に上記真空炉を用いた処理品の処理を説
明する。扉4,7が開けられ、処理品31が載置台10の上
に乗せられる。次に扉4,7が閉じられ、真空装置17が
作動されて炉殻2内が真空排気されると共に、ヒータ12
への通電によってそれが発熱され、処理品31の加熱が開
始される。又炉殻2にはそれを所定温度に保温する保温
手段の一例として、水冷ジャケットに温水等の熱媒体が
流され、炉殻2の内面が、その付近に蒸気(次に述べる
ように処理品31から生ずる蒸気)が到達してもその蒸気
の凝縮を阻止する温度に保持される。その温度は蒸気圧
により異なるが例えば数10度である。
Next, processing of a processed product using the above vacuum furnace will be described. The doors 4 and 7 are opened, and the processed product 31 is placed on the mounting table 10. Next, the doors 4 and 7 are closed, the vacuum device 17 is operated to evacuate the furnace shell 2, and the heater 12
It is heated by the energization to, and heating of the processed product 31 is started. Further, as an example of a heat retaining means for keeping the furnace shell 2 at a predetermined temperature, a heat medium such as hot water is flown through a water cooling jacket, and the inner surface of the furnace shell 2 is vaporized in the vicinity thereof (processed product as described below). The vapor generated from 31) is held at a temperature that prevents the vapor from condensing even when it arrives. The temperature is, for example, several tens of degrees although it depends on the vapor pressure.

【0013】上記のように加熱を開始した場合、処理品
31が加熱により水分が蒸発するものであると、加熱に伴
い処理品31から水分が蒸発する。その蒸気は上記真空排
気にともない排気用管路18を通って炉殻2外に排出され
る。この場合上記蒸気の一部が断熱壁5を通り抜けて炉
殻2の付近に到達しても、炉殻2は上記のような温度に
保持されている為、その蒸気は凝縮することはなく、上
記真空排気によって炉殻2外に排出される。炉殻2外に
排出された蒸気は真空装置17に至る前に凝縮器19によっ
て凝縮され水として除去される。従って、真空装置17へ
水分が至ることはなく、真空装置17の劣化が未然に防止
される。
When heating is started as described above, treated products
When 31 is a material whose water content is evaporated by heating, the water content is evaporated from the treated product 31 as it is heated. The steam is discharged to the outside of the furnace shell 2 through the exhaust pipe line 18 in association with the vacuum exhaust. In this case, even if a part of the steam passes through the heat insulating wall 5 and reaches the vicinity of the furnace shell 2, since the furnace shell 2 is maintained at the temperature as described above, the steam does not condense, It is discharged to the outside of the furnace shell 2 by the vacuum exhaust. The steam discharged to the outside of the furnace shell 2 is condensed by the condenser 19 and removed as water before reaching the vacuum device 17. Therefore, moisture does not reach the vacuum device 17, and the deterioration of the vacuum device 17 is prevented.

【0014】上記処理品31からの蒸気の発生が終わると
炉殻2内の真空度は所定の高真空度まで上昇し、その状
態において処理品31の所定の加熱が行われる。
When the generation of steam from the processed product 31 is finished, the degree of vacuum in the furnace shell 2 rises to a predetermined high vacuum level, and the processed product 31 is heated in a predetermined state in this state.

【0015】上記のようにして処理品31に所定の加熱が
施されたならば、ヒータ12への通電が停止され、冷却用
のガスが炉殻2内に導入され、クーラ22やファン23が周
知のように運転されて、処理品31の冷却が行われる。そ
して冷却が終了すると、扉4,7が開かれて処理を終え
た処理品31が取り出される。
When the processed article 31 is heated to a predetermined level as described above, the heater 12 is de-energized, the cooling gas is introduced into the furnace shell 2, and the cooler 22 and the fan 23 are turned on. It is operated in a known manner to cool the processed product 31. When the cooling is completed, the doors 4 and 7 are opened and the processed product 31 that has been processed is taken out.

【0016】次に上記のように処理品31から水分の蒸発
する処理の数例を示せば、次の通りである。水アトマイ
ズにより製造した酸化された合金鋼粉末の水素還元処
理、表層が酸化した金属の還元性ガスによる還元処理、
粉末に付着した水分の乾燥処理等である。
Next, some examples of the process of evaporating the water from the processed product 31 as described above are as follows. Hydrogen reduction treatment of oxidized alloy steel powder produced by water atomization, reduction treatment of metal whose surface layer is oxidized by reducing gas,
This is, for example, a drying process of water adhering to the powder.

【0017】次に炉殻2の保温手段の他の例を説明す
る。その一つは、炉殻2の外側又は内側に保温手段とし
て加熱ヒータを付設し、それによって炉殻2の内面を上
記の様に保温する方法である。他の一つは、炉殻2が水
冷構造でない場合、炉殻2の外側を保温手段としての断
熱材で覆う方法である。更に他の一つは、断熱壁5の断
熱性を小さくしておき、ヒータ12から発せられた後断熱
壁5の外に漏れ、炉殻2の内面に至る熱を保温手段とし
て利用する方法である。
Next, another example of the heat retaining means for the furnace shell 2 will be described. One of them is a method in which a heater is attached to the outside or inside of the furnace shell 2 as a heat-retaining means, so that the inner surface of the furnace shell 2 is kept warm as described above. The other is a method of covering the outside of the furnace shell 2 with a heat insulating material as a heat retaining means when the furnace shell 2 does not have a water cooling structure. Still another is a method in which the heat insulating property of the heat insulating wall 5 is kept small, and the heat emitted from the heater 12 to the outside of the heat insulating wall 5 and reaching the inner surface of the furnace shell 2 is used as a heat insulating means. is there.

【0018】次に熱処理の他の例として、加熱に伴って
処理品から生ずる蒸気が炉殻2の内面付近で凝縮し、炉
殻内面に水が付着するままの状態で処理が行われる場合
がある。この場合には、前の処理品の処理が終わって次
の処理品の処理を開始しようとする場合、次のようにす
ると良い。炉殻2が図1、2から明らかなように円筒構
造をしておりその最低部に集水部14が設けてある為、上
記炉殻2の内面に付着する水は重力によって自然に集水
部14に集まっている。従って前の処理品の処理が終了し
た段階でドレンバルブ16を開いてその水を排水口15から
炉殻2外に排出する。その後バルブ16を閉じ、次の処理
品31の装入、真空排気、ヒータ12による加熱を開始す
る。尚上記水の排出は、次の処理品31の装入の後に行っ
ても良い。又排水口15に水の強制排出手段例えば排水ポ
ンプを接続した場合には、上記水の排出は前の処理品の
処理過程或いは次の処理品の処理の為の真空排気を開始
した後に行っても良い。
Next, as another example of the heat treatment, there is a case where the steam generated from the treated product by heating is condensed near the inner surface of the furnace shell 2 and the treatment is carried out in a state where water is attached to the inner surface of the furnace shell 2. is there. In this case, when the processing of the previous processed product is finished and the processing of the next processed product is to be started, the following may be performed. Since the furnace shell 2 has a cylindrical structure as is clear from FIGS. 1 and 2 and the water collecting portion 14 is provided at the lowest portion thereof, water attached to the inner surface of the furnace shell 2 is naturally collected by gravity. Gathered in part 14. Therefore, when the treatment of the previous treated product is completed, the drain valve 16 is opened and the water is discharged from the drainage port 15 to the outside of the furnace shell 2. After that, the valve 16 is closed, and the charging of the next processed product 31, the vacuum exhaust, and the heating by the heater 12 are started. The water may be discharged after charging the next treated product 31. Further, when a forced discharge means of water, for example, a drain pump is connected to the drain port 15, the water is discharged after starting the vacuum exhaust for the treatment process of the previous treated product or the treatment of the next treated product. Is also good.

【0019】次に図3は本願の異なる実施例を示すもの
で、真空加熱炉の他の例として連続式の真空炉を示すも
のである。真空炉1eは、前室33と、主処理室34と、冷却
室35とから構成されている。前室33は処理品を受け入れ
る為の入口36を有し、そこには開閉装置38によって操作
される扉37が備わっている。前室33と主処理室34との間
及び主処理室34と冷却室35との間は夫々隔壁39で仕切ら
れている。各隔壁39には処理品通過用の開口部が設けら
れ、それらの開口部には開閉装置41で操作される扉40が
備わっている。主処理室34には前実施例で示した如き保
温手段と、排水構造とを備えてある。上記前室33及び主
処理室34にはそれぞれ個別の真空装置が接続してある。
冷却室35は出口42を有し、そこには開閉装置44によって
操作される扉43が備わっている。冷却室35には冷却用の
ガスを送入する為の図示外のガス供給手段が接続してあ
る。45は前室33、主処理室34、冷却室35を通して設けら
れた搬送手段で、例えばローラが利用してある。
Next, FIG. 3 shows a different embodiment of the present invention, showing a continuous vacuum furnace as another example of the vacuum heating furnace. The vacuum furnace 1e includes a front chamber 33, a main processing chamber 34, and a cooling chamber 35. The antechamber 33 has an inlet 36 for receiving a processed product, and a door 37 operated by an opening / closing device 38 is provided therein. The front chamber 33 and the main processing chamber 34 and the main processing chamber 34 and the cooling chamber 35 are partitioned by partition walls 39, respectively. Each partition 39 is provided with an opening for passing a processed product, and each opening is provided with a door 40 operated by an opening / closing device 41. The main processing chamber 34 is provided with the heat retaining means as shown in the previous embodiment and the drainage structure. Separate vacuum devices are connected to the front chamber 33 and the main processing chamber 34, respectively.
The cooling chamber 35 has an outlet 42, which is provided with a door 43 operated by an opening / closing device 44. The cooling chamber 35 is connected to a gas supply means (not shown) for feeding a cooling gas. Reference numeral 45 denotes a transfer means provided through the front chamber 33, the main processing chamber 34, and the cooling chamber 35, which is, for example, a roller.

【0020】上記のような真空炉1eは例えば粉末金属成
形品の焼結の為に用いられる。処理品31eは先ず前室33
内に入れられ、周知の前処理が行われる。次にその処理
品31eは主処理室34内に入れられ、そこで真空状態にお
いて主たる加熱処理が行われる。この場合、処理品31e
から生ずる蒸気は前実施例と同様にして凝縮が防止され
る。主処理室34で所定の加熱処理が終わると処理品31e
は冷却室35に入れられ、そこで通常の低い温度まで冷却
され、その後出口42から送出される。尚上記真空炉1eに
おいては、前室33と冷却室35の両方又はその一方にも、
前実施例で示した如き保温手段と、排水構造との両方又
は何れか一方を備えても良い。そうすることによって、
主処理室34から蒸気がそれらの部屋に流れ込んでも、そ
れらの部屋の炉殻への水の付着を防止したり、各々の部
屋に溜まった水を排出することが出来る。なお、機能上
前図のものと同一又は均等構成と考えられる部分には、
前図と同一の符号にアルファベットのeを付して重複す
る説明を省略した。
The vacuum furnace 1e as described above is used, for example, for sintering a powder metal molded product. First, the processed product 31e is in the front chamber 33.
It is placed inside and a well-known pretreatment is performed. Next, the processed product 31e is put into the main processing chamber 34, where the main heat treatment is performed in a vacuum state. In this case, processed product 31e
The vapor generated from this is prevented from condensing as in the previous embodiment. When the prescribed heat treatment is completed in the main processing chamber 34, the processed product 31e
Is placed in a cooling chamber 35, where it is cooled to a normal low temperature and then delivered from outlet 42. In the vacuum furnace 1e, both the front chamber 33 and the cooling chamber 35, or one of them,
Both or either of the heat retaining means as shown in the previous embodiment and the drainage structure may be provided. By doing so,
Even if steam flows from the main processing chamber 34 into those chambers, it is possible to prevent water from adhering to the furnace shells of those chambers and to discharge the water accumulated in each chamber. It should be noted that, in terms of function, parts considered to be the same as or equivalent to those in the previous figure
The same reference numerals as in the previous figure are appended with the letter e, and the duplicate description is omitted.

【0021】[0021]

【発明の効果】以上のように本願発明にあっては、処理
品31を加熱する場合、真空状態のもとでその加熱を行な
い得るは勿論のこと、
As described above, according to the present invention, when the processed product 31 is heated, it goes without saying that it can be heated under a vacuum condition.

【0022】上記の如き真空状態での加熱を開始する場
合、加熱に伴い処理品31から水分が蒸発しその蒸気が炉
殻2の内面付近に到達しても、炉殻2の内面はその蒸気
の凝縮を阻止する温度に保たれるから、上記蒸気は、凝
縮することなく、真空排気に伴なって速やかに炉殻外に
排出されてしまう特長がある。このことは、処理品31か
らの水分の蒸発が終わればその直後から炉内の真空度を
真空排気による所定の高真空度に向けて上昇させ得るこ
とであり、前記従来技術の如く炉殻内面に凝縮した水が
蒸発してしまうまでの長時間のあいだ真空度の上昇が蒸
気圧によって規制されていたものに比べ、短時間で所定
の高真空度の状態での加熱を開始できる利点がある。
When heating in the vacuum state as described above is started, even if moisture evaporates from the treated product 31 due to heating and the steam reaches the vicinity of the inner surface of the furnace shell 2, the inner surface of the furnace shell 2 still retains the steam. Since the temperature is maintained at a temperature at which the condensation of the above is prevented, the vapor has a feature that it is not condensed and is promptly discharged to the outside of the furnace shell upon evacuation. This means that immediately after the evaporation of water from the treated product 31 is finished, the degree of vacuum in the furnace can be increased toward a predetermined high degree of vacuum by vacuum evacuation. There is an advantage that heating in a predetermined high vacuum state can be started in a short time compared to the one in which the increase of the vacuum degree was regulated by the vapor pressure for a long time until the condensed water was evaporated. ..

【0023】更に本願発明の方法によれば、真空状態で
の処理品の加熱の開始の場合、例えば前の処理品の処理
の工程で生じた水が炉殻2の内部に溜まっていても、そ
の水を排出して真空排気を行うから、前記従来技術の如
く溜まった水の蒸発による真空度の規制は元々生ずるこ
とはなく、良好な真空度の状態での処理品の加熱を行い
得る効果がある。
Further, according to the method of the present invention, when the heating of the processed product in the vacuum state is started, for example, even if the water generated in the process of the previous processed product is accumulated inside the furnace shell 2, Since the water is discharged and evacuated, the degree of vacuum is not restricted by evaporation of the accumulated water as in the prior art, and the processed product can be heated in a good degree of vacuum. There is.

【図面の簡単な説明】[Brief description of drawings]

【図1】真空炉の略示縦断面図。FIG. 1 is a schematic vertical sectional view of a vacuum furnace.

【図2】図1におけるII−II線断面図。FIG. 2 is a sectional view taken along line II-II in FIG.

【図3】異なる真空炉の例を示す略示縦断面図。FIG. 3 is a schematic vertical sectional view showing an example of a different vacuum furnace.

【符号の説明】[Explanation of symbols]

2 炉殻 12 加熱手段 17 真空装置 31 処理品 2 Furnace shell 12 Heating means 17 Vacuum equipment 31 Processed product

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 内部を真空排気する為の真空装置が付設
されている炉殻内に、炉殻の内部に存置された処理品を
加熱する為の加熱手段が備えられている真空加熱炉にお
いて、上記炉殻の内面を、上記処理品から生じて炉殻の
内面付近に到達した蒸気の凝縮を阻止する温度に保持す
る保温手段を備えたことを特徴とする真空加熱炉。
1. A vacuum heating furnace in which a heating means for heating a processed product existing inside the furnace shell is provided in the furnace shell provided with a vacuum device for evacuating the inside. A vacuum heating furnace provided with a heat retaining means for holding the inner surface of the furnace shell at a temperature that prevents condensation of vapor generated from the treated product and reaching near the inner surface of the furnace shell.
【請求項2】 真空装置が付設された炉殻内に処理品を
存置させ、炉殻内を真空排気し、処理品を加熱する真空
加熱方法において、上記炉殻内を真空排気するに当って
は、炉殻内に溜まった水を炉殻外に排出すると共に、炉
殻内を真空排気することを特徴とする真空加熱方法。
2. A vacuum heating method in which a processed product is placed in a furnace shell provided with a vacuum device, the furnace shell is evacuated, and the processed product is heated, in which the furnace shell is evacuated. Is a vacuum heating method characterized in that the water accumulated in the furnace shell is discharged to the outside of the furnace shell and the furnace shell is evacuated.
JP24263891A 1991-08-27 1991-08-27 Vacuum heating method Expired - Fee Related JP3163676B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24263891A JP3163676B2 (en) 1991-08-27 1991-08-27 Vacuum heating method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24263891A JP3163676B2 (en) 1991-08-27 1991-08-27 Vacuum heating method

Publications (2)

Publication Number Publication Date
JPH0552485A true JPH0552485A (en) 1993-03-02
JP3163676B2 JP3163676B2 (en) 2001-05-08

Family

ID=17092030

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24263891A Expired - Fee Related JP3163676B2 (en) 1991-08-27 1991-08-27 Vacuum heating method

Country Status (1)

Country Link
JP (1) JP3163676B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009113621A1 (en) * 2008-03-12 2009-09-17 株式会社Ihi Single chamber vacuum heat treating furnace and method of preventing oxidation of article to be treated in single chamber vacuum heat treating furnace
WO2013032301A2 (en) * 2011-08-31 2013-03-07 Lg Innotek Co., Ltd. Reaction container and vacuum heat treatment apparatus having the same
CN105333741A (en) * 2015-11-09 2016-02-17 云南钛业股份有限公司 Method for rapid pumping out
CN107002159A (en) * 2015-04-02 2017-08-01 株式会社Ihi Annealing device
CN110530543A (en) * 2019-07-23 2019-12-03 上海卫星装备研究所 Closure assembly is heated in vacuum degassing suitable for aerospace product

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009113621A1 (en) * 2008-03-12 2009-09-17 株式会社Ihi Single chamber vacuum heat treating furnace and method of preventing oxidation of article to be treated in single chamber vacuum heat treating furnace
JP2009216344A (en) * 2008-03-12 2009-09-24 Ihi Corp Single chamber type vacuum heat treatment furnace and oxidation preventing method for treatment item in single chamber type vacuum heat treatment furnace
WO2013032301A2 (en) * 2011-08-31 2013-03-07 Lg Innotek Co., Ltd. Reaction container and vacuum heat treatment apparatus having the same
WO2013032301A3 (en) * 2011-08-31 2013-05-10 Lg Innotek Co., Ltd. Reaction container and vacuum heat treatment apparatus having the same
CN107002159A (en) * 2015-04-02 2017-08-01 株式会社Ihi Annealing device
CN105333741A (en) * 2015-11-09 2016-02-17 云南钛业股份有限公司 Method for rapid pumping out
CN110530543A (en) * 2019-07-23 2019-12-03 上海卫星装备研究所 Closure assembly is heated in vacuum degassing suitable for aerospace product

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