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JP2916686B2 - Gas supply device for cooling of vacuum heating furnace - Google Patents
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JP2916686B2 - Gas supply device for cooling of vacuum heating furnace - Google Patents

Gas supply device for cooling of vacuum heating furnace

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Publication number
JP2916686B2
JP2916686B2 JP8053989A JP8053989A JP2916686B2 JP 2916686 B2 JP2916686 B2 JP 2916686B2 JP 8053989 A JP8053989 A JP 8053989A JP 8053989 A JP8053989 A JP 8053989A JP 2916686 B2 JP2916686 B2 JP 2916686B2
Authority
JP
Japan
Prior art keywords
gas
vacuum heating
cooling
heating furnace
furnace
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 - Lifetime
Application number
JP8053989A
Other languages
Japanese (ja)
Other versions
JPH02259010A (en
Inventor
通 田中
紀行 島内
保雄 日向野
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.)
Taiyo Nippon Sanso Corp
Original Assignee
Nippon Sanso Corp
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 Nippon Sanso Corp filed Critical Nippon Sanso Corp
Priority to JP8053989A priority Critical patent/JP2916686B2/en
Publication of JPH02259010A publication Critical patent/JPH02259010A/en
Application granted granted Critical
Publication of JP2916686B2 publication Critical patent/JP2916686B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Heat Treatments In General, Especially Conveying And Cooling (AREA)
  • Furnace Details (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は真空加熱炉の冷却用気体供給装置に関し、詳
しくは、金属を真空炉内で真空加熱処理した後、炉内温
度を所定温度に降下させるために使用する冷却用気体を
供給する装置に関するものである。
Description: TECHNICAL FIELD The present invention relates to a gas supply device for cooling a vacuum heating furnace. More specifically, the present invention relates to a method for heating a metal in a vacuum furnace and then heating the metal to a predetermined temperature. The present invention relates to a device for supplying a cooling gas used for lowering.

〔従来の技術〕[Conventional technology]

金属の熱処理、例えば焼き入れ,溶体化処理,焼鈍
し,焼き戻し,ろう付け等は、被処理金属の酸化を避け
るために真空加熱炉を使用して減圧下で加熱処理してい
る。そして処理後の炉内の温度を所定温度にまで降下さ
せるため、冷却媒体として被処理金属の酸化や汚染する
のを避けるよう水素,ヘリウム、窒素、アルゴン等の気
体を真空加熱炉内に供給して行っている。この冷却用気
体は冷却を速めるため通常加圧充填される。そして炉内
が所定温度に降下すると冷却用の前記気体は、加熱処理
した金属より脱気する種々の不純成分が含まれるため、
炉より排出して通常は大気に放散している。
Heat treatment of the metal, for example, quenching, solution treatment, annealing, tempering, brazing, etc., is performed under reduced pressure using a vacuum heating furnace in order to avoid oxidation of the metal to be treated. Then, in order to lower the temperature inside the furnace after the treatment to a predetermined temperature, a gas such as hydrogen, helium, nitrogen or argon is supplied into the vacuum heating furnace as a cooling medium so as to avoid oxidation and contamination of the metal to be treated. Have gone. This cooling gas is usually filled under pressure to speed the cooling. And when the inside of the furnace drops to a predetermined temperature, the cooling gas contains various impurity components that are deaerated from the heat-treated metal,
It is discharged from the furnace and is normally released to the atmosphere.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

しかしながら、上記した冷却用の気体は何れも高価な
気体であり、しかも冷却を速めるために前記した通り高
い圧力に加圧して使用することよりその使用量は極めて
多量となり、その結果処理費用がかさむこととなる。そ
れ故、特にヘリウムの如き高価な気体は金属の冷却用気
体として極めて効果的であることが理解し得ていても、
経済的にその使用意欲を阻害していた。
However, the above-mentioned cooling gas is an expensive gas, and the amount of the gas used is extremely large when used under high pressure as described above in order to speed up the cooling, resulting in an increase in processing cost. It will be. Therefore, even though expensive gases such as helium in particular can be understood to be very effective as cooling gases for metals,
It was economically impeding its willingness to use.

本発明は、上記した現状に鑑み、真空加熱炉の冷却に
使用した後の不純成分を含む排出気体を大気に放散する
ことなく、これを回収して再利用することを図り、高価
な前記各々の気体をより安価に利用し得るようにした真
空加熱炉の冷却用気体の供給装置を提供することを目的
としている。
In view of the above situation, the present invention aims to collect and reuse exhaust gas containing impurity components after being used for cooling the vacuum heating furnace without dispersing the exhaust gas to the atmosphere, It is an object of the present invention to provide a cooling gas supply device for a vacuum heating furnace that can use the gas at a lower cost.

〔課題を解決するための手段〕[Means for solving the problem]

上記目的を達成するために、本発明の真空加熱炉の冷
却用気体の供給装置は、第1の構成として、炉内を加熱
する加熱器と炉内を真空排気する排気手段を有する真空
排気系統とを付設してなる真空加熱炉に冷却用気体を供
給する装置であって、前記真空加熱炉と冷却用気体を貯
蔵した貯槽とを連結した管路よりなる気体供給系統と、
該気体供給系統の管路に両端が連結した管路に、吐出口
を前記気体供給系統の気体の流れと対向する方向に開口
させて配置した圧縮機を設けてなる気体回収系統と、一
端を前記気体回収系統の圧縮機の吐出口側管路に、他端
を前記気体供給系統の管路の前記気体回収系統の真空加
熱炉側分岐部より真空加熱炉側にそれぞれ連結した供給
気体加圧系統とを備えるとともに、前記気体回収系統の
管路に触媒筒,吸着筒等の気体精製手段を配置したこと
を特徴としている。
In order to achieve the above object, a cooling gas supply device for a vacuum heating furnace according to the present invention has, as a first configuration, a vacuum exhaust system having a heater for heating the inside of a furnace and an exhaust unit for evacuating the inside of the furnace. A gas supply system comprising a pipe connecting the vacuum heating furnace and a storage tank storing the cooling gas, which is a device for supplying a cooling gas to a vacuum heating furnace provided with:
A gas recovery system including a compressor having a discharge port opened and opened in a direction opposite to the flow of gas in the gas supply system, in a pipe connected at both ends to the gas supply system, and one end. Supply gas pressurization connected to the discharge port side of the compressor of the gas recovery system, and the other end connected to the vacuum heating furnace side of the vacuum recovery furnace side branch of the gas recovery system of the gas supply system. And a gas purifying means such as a catalyst tube or an adsorption tube is disposed in a pipeline of the gas recovery system.

また第2の構成は、前記第1の構成と同様に構成され
た気体供給系統と、気体の精製手段を持たない気体回収
系統、及び第1の構成と同様の供給気体加圧系統とを備
えるとともに、前記貯槽と前記気体回収系統に配置した
圧縮機の吸入口側とを連結した管路に触媒筒,吸着筒等
の気体精製手段を配設した回収気体精製系統とを備える
ことを特徴としている。
Further, the second configuration includes a gas supply system configured in the same manner as the first configuration, a gas recovery system having no gas purification unit, and a supply gas pressurization system similar to the first configuration. And a recovery gas purification system provided with gas purification means such as a catalyst tube and an adsorption tube in a pipe connecting the storage tank and the suction port side of the compressor arranged in the gas recovery system. I have.

〔実施例〕〔Example〕

以下、本発明を図面に示す実施例に基づいてさらに詳
細に説明する。
Hereinafter, the present invention will be described in more detail based on embodiments shown in the drawings.

まず、第1図は第1実施例を示すもので、本発明装置
の上記第1の構成を適用した一実施例を示している。
First, FIG. 1 shows the first embodiment, and shows one embodiment in which the first configuration of the device of the present invention is applied.

真空加熱炉1は、真空下で金属の熱処理を行うために
通常用いられているものであって、断熱された炉壁2で
気密に囲繞して形成されており、真空加熱炉1内にはヒ
ーター等の発熱体3と真空加熱炉1内を攪拌するための
攪拌ファン4とが配設されている。また炉壁2には冷却
水管5及び真空加熱炉1内の圧力を測定するための圧力
計6が配置されている。このような真空加熱炉1には炉
壁2を気密に貫通して炉内に連通している真空排気系統
7が、弁8,拡散ポンプ9,回転ポンプ10等を配して設けら
れている。尚、被加熱金属Aは、バスケット11により炉
内に搬出入される。
The vacuum heating furnace 1 is generally used for heat-treating a metal under vacuum, and is formed so as to be airtightly surrounded by insulated furnace walls 2. A heating element 3 such as a heater and a stirring fan 4 for stirring the inside of the vacuum heating furnace 1 are provided. A cooling water pipe 5 and a pressure gauge 6 for measuring the pressure in the vacuum heating furnace 1 are arranged on the furnace wall 2. Such a vacuum heating furnace 1 is provided with a vacuum exhaust system 7 which penetrates the furnace wall 2 in a gas-tight manner and communicates with the inside of the furnace, and is provided with a valve 8, a diffusion pump 9, a rotary pump 10, and the like. . The metal to be heated A is carried into and out of the furnace by the basket 11.

本発明の真空加熱炉の冷却用気体の供給装置は、この
ような構成の真空加熱炉1内で金属を真空下で熱処理し
た後に、炉内を冷却するため炉内に冷却用気体を供給す
るものであって、水素,窒素,ヘリウム,アルゴン等の
気体より選ばれた一つ、あるいは二つ以上の混合気体か
らなる冷却用気体を貯槽12から真空加熱炉1に供給し、
冷却後の冷却用気体を貯槽12に回収するように構成した
ものである。
The cooling gas supply device for a vacuum heating furnace according to the present invention supplies a cooling gas to the furnace for cooling the furnace after heat-treating the metal under vacuum in the vacuum heating furnace 1 having such a configuration. A cooling gas comprising one or a mixture of two or more gases selected from gases such as hydrogen, nitrogen, helium, argon, etc., is supplied from the storage tank 12 to the vacuum heating furnace 1;
The cooling gas after cooling is collected in the storage tank 12.

上記貯槽12は、弁13,弁14,弁15を配した管路16よりな
る気体供給系統17で真空加熱炉1に連結している。尚、
以下の説明においては、この気体供給系統17の気体の流
れをもとにして貯槽12側を上流,真空加熱炉1側を下流
と呼ぶ。
The storage tank 12 is connected to the vacuum heating furnace 1 by a gas supply system 17 including a pipe 16 in which valves 13, 14 and 15 are arranged. still,
In the following description, the storage tank 12 side is referred to as upstream, and the vacuum heating furnace 1 side is referred to as downstream based on the gas flow in the gas supply system 17.

そして前記気体供給系統17には、一端が管路16の弁13
の下流側で弁18を介して分岐するとともに、他端が管路
16の弁14の下流側で弁19を介して分岐し、量端が気体供
給系統17の管路16と連結合流する側管路20が設けられて
いる。該側管路20の前記弁18と弁19との間には、吐出口
が弁18側、即ち吐出口を前記気体供給系統17の気体の流
れと対向する方向に開口させて配置した圧縮機21が設け
られている。さらに該圧縮機21の吐出口側には弁22が設
けられ、弁22と弁18との間には白金触媒やパラジウム触
媒等を充填した触媒筒23と、シリカゲル,アルミナ,ゼ
オライト,モレキュラシーブス等の吸着剤を充填した吸
着筒24とが配置されており、これらの弁19,圧縮機21,弁
22,触媒筒23,吸着筒24,弁18を順に備えた側管路20によ
り気体回収系統25が構成されている。
One end of the gas supply system 17 is connected to the valve 13 of the pipe 16.
Downstream from the valve via a valve 18 and the other end
Downstream of the 16 valves 14, there is provided a side pipe 20 branched via a valve 19 and having a flow end connected to the pipe 16 of the gas supply system 17. A compressor in which a discharge port is disposed between the valve 18 and the valve 19 of the side pipe line 20 with a discharge port opened in a direction facing the flow of gas in the gas supply system 17, that is, a discharge port. 21 are provided. Further, a valve 22 is provided on the discharge port side of the compressor 21, and a catalyst tube 23 filled with a platinum catalyst, a palladium catalyst, or the like, and a silica gel, alumina, zeolite, molecular sieve, etc. And an adsorption cylinder 24 filled with the adsorbent, these valves 19, the compressor 21, the valve
A gas recovery system 25 is constituted by a side pipe line 20 provided with 22, a catalyst tube 23, an adsorption tube 24, and a valve 18 in that order.

尚、触媒筒23及び吸着筒24は複数筒併設して設け、使
用と再生の工程を交互に切り替え操作して運転すると連
続運転上好都合である。
Note that it is convenient for continuous operation if a plurality of catalyst tubes 23 and adsorption tubes 24 are provided in parallel and operated by alternately switching the use and regeneration steps.

さらに、前記気体回収系統25の圧縮機21と弁22との
間、即ち圧縮機21の吐出口側には、管26が分岐してい
る。この管26は、その他端が弁27を介して前記気体供給
系統17の管路16の弁15の下流側、即ち弁15と真空加熱炉
1との間に連結しており、この管26と弁27とで供給気体
加圧系統28を構成している。
Further, a pipe 26 is branched between the compressor 21 and the valve 22 of the gas recovery system 25, that is, on the discharge port side of the compressor 21. The other end of the pipe 26 is connected via a valve 27 to the downstream side of the valve 15 in the line 16 of the gas supply system 17, that is, between the valve 15 and the vacuum heating furnace 1. The supply gas pressurizing system 28 is constituted by the valve 27.

次に、上記実施例装置の運転方法を説明する。 Next, an operation method of the above-described embodiment apparatus will be described.

まず、被処理金属Aをバスケット11に載置して真空加
熱炉1内に収容して密閉した後、回転ポンプ10及び拡散
ポンプ9を作動させるとともに弁8を開き、真空加熱炉
1内を排気して所定の真空度とする。所定の真空度に達
したら加熱器3を作動せしめ、炉1内を真空を保持しな
がら昇温し、被処理金属Aを所望する熱処理に応じた条
件にして熱処理する。尚、この間冷却水管5には冷却水
を流水しておく。そして所望の加熱処理が終了したら、
加熱器3を停止して弁8を閉じるとともに拡散ポンプ9
及び真空回転ポンプ10を停止して真空加熱処理が遮断さ
れる。
First, the metal A to be treated is placed in the basket 11 and housed in the vacuum heating furnace 1 to be sealed. Then, the rotary pump 10 and the diffusion pump 9 are operated and the valve 8 is opened to evacuate the vacuum heating furnace 1. To a predetermined degree of vacuum. When a predetermined degree of vacuum is reached, the heater 3 is operated, the temperature inside the furnace 1 is raised while maintaining the vacuum, and the metal A to be processed is heat-treated under conditions according to the desired heat treatment. During this time, cooling water is supplied to the cooling water pipe 5. And when the desired heat treatment is completed,
The heater 3 is stopped, the valve 8 is closed, and the diffusion pump 9 is closed.
Then, the vacuum rotary pump 10 is stopped to shut off the vacuum heating process.

上記のごとく、所定の真空加熱処理が終了したら、弁
13,弁14,弁15を順次開き(その他の弁は閉)、貯槽12を
真空加熱炉1に連通せしめて、貯槽12に貯蔵してある冷
却用気体を、その圧力差で気体供給系統17により真空加
熱炉1に導入して炉内を冷却する。
As described above, when the predetermined vacuum heating process is completed,
13, the valve 14 and the valve 15 are sequentially opened (the other valves are closed), the storage tank 12 is connected to the vacuum heating furnace 1, and the cooling gas stored in the storage tank 12 is supplied to the gas supply system 17 by the pressure difference. To cool the inside of the furnace by introducing it into the vacuum heating furnace 1.

この冷却用気体は、貯槽12と真空加熱炉1との圧力が
平衡するまで流れるが、真空加熱炉の圧力が所定の圧力
になったら弁13,14,15を閉じ気体の供給を停止する。両
者の圧力は、それぞれに設けられた圧力計6,29により測
定される。そして真空加熱炉1の圧力が貯槽12の圧力と
平衡しても、その圧力が所定の圧力に至らない時には、
弁15を閉じて弁19、弁27を開くとともに圧縮機21を駆動
して、貯槽12の冷却用気体を弁13,弁14,弁19を介して圧
縮機21で吸入し、圧縮した後に弁27を経て供給気体加圧
系統28の管路26より真空加熱炉1に圧送し、炉内が所定
圧力になるまで冷却用気体を加圧充填する。一般に、気
体による冷却は、その圧力が高いほど冷却が速まり処理
作業を効率よく進めることができる。
This cooling gas flows until the pressure in the storage tank 12 and the vacuum heating furnace 1 equilibrates. When the pressure in the vacuum heating furnace reaches a predetermined pressure, the valves 13, 14, and 15 are closed to stop the gas supply. Both pressures are measured by pressure gauges 6, 29 provided respectively. Even if the pressure of the vacuum heating furnace 1 is balanced with the pressure of the storage tank 12, when the pressure does not reach the predetermined pressure,
The valve 15 is closed, the valves 19 and 27 are opened, and the compressor 21 is driven, and the cooling gas in the storage tank 12 is sucked by the compressor 21 through the valves 13, the valves 14 and the valve 19, and is compressed. The gas is supplied to the vacuum heating furnace 1 through a pipe 26 of a supply gas pressurizing system 28 via a gas supply line 27, and is filled with cooling gas under pressure until the inside of the furnace reaches a predetermined pressure. In general, in gas cooling, the higher the pressure, the faster the cooling and the more efficient the processing operation.

このようにして真空加熱炉1に冷却用気体が所定圧力
にまで加圧充填されたら、弁27,弁19を閉じるとともに
圧縮機21を停止し、冷却用気体の真空加熱炉1への供給
を止める。そして攪拌ファン4を駆動し、炉内を攪拌し
て冷却を促進する。また冷却の進行とともに炉内圧力は
降下してくるが、この時は適宜弁13,弁14,弁19,弁27を
開くとともに圧縮機21を駆動して、貯槽12より供給気体
加圧系統28を使用して逐次冷却用気体を真空加熱炉1に
加圧補充するとよい。
When the cooling gas is pressurized and filled to a predetermined pressure in the vacuum heating furnace 1 in this manner, the valves 27 and 19 are closed, the compressor 21 is stopped, and the supply of the cooling gas to the vacuum heating furnace 1 is performed. stop. Then, the stirring fan 4 is driven to stir the inside of the furnace to promote cooling. In addition, the pressure in the furnace decreases with the progress of cooling, but at this time, the valves 13, 14, 14, 19, and 27 are opened as appropriate, and the compressor 21 is driven to supply the pressurized gas pressurized system 28 from the storage tank 12. The cooling gas may be successively pressurized and supplied to the vacuum heating furnace 1 by using.

かくして真空加熱炉1内の温度が所望する温度(例え
ば処理金属を搬出作業することができる温度)にまで降
下したら攪拌ファン4を停止する。そして真空加熱炉1
の圧力が貯槽12の圧力より高い間は、弁27,弁22,弁18,
弁13を開き、真空加熱炉1内の気体を供給気体加圧系統
28及び気体回収系統25の触媒筒23、吸着筒24を介して貯
槽12に回収する。次いで真空加熱炉1内と貯槽12内の圧
力が平衡したら、弁27を閉じ、弁15,弁19を開くととも
に圧縮機21を駆動する。そして真空加熱炉1内の冷却用
気体を気体回収系統25を経て貯槽12に回収する。この気
体回収系統25を通って回収される冷却用気体は、真空加
熱炉1での冷却に使用された結果、酸素,水分,その他
の不純成分が含まれているが、これら不純物等は気体の
精製手段である触媒筒23,吸着筒24を通過して除去さ
れ、精製された高純度の気体として貯槽12に回収され
る。
When the temperature in the vacuum heating furnace 1 drops to a desired temperature (for example, a temperature at which the processing metal can be carried out), the stirring fan 4 is stopped. And vacuum heating furnace 1
While the pressure of the storage tank 12 is higher than the pressure of the storage tank 12, the valve 27, the valve 22, the valve 18,
Open the valve 13 and supply gas in the vacuum heating furnace 1 to the gas pressurizing system
The gas is collected in the storage tank 12 through the catalyst tube 23 and the adsorption tube 24 of the gas recovery system 25 and the gas recovery system 25. Next, when the pressures in the vacuum heating furnace 1 and the storage tank 12 are balanced, the valve 27 is closed, the valves 15 and 19 are opened, and the compressor 21 is driven. Then, the cooling gas in the vacuum heating furnace 1 is recovered in the storage tank 12 via the gas recovery system 25. The cooling gas recovered through the gas recovery system 25 contains oxygen, moisture, and other impurity components as a result of being used for cooling in the vacuum heating furnace 1. The gas is removed by passing through the catalyst tube 23 and the adsorption tube 24, which are purification means, and is recovered in the storage tank 12 as purified high-purity gas.

また、気体回収系統25の圧縮機21の吸入側の管路20の
弁19を挟んで弁30,弁31を有する、側管路32を設け、該
側管路32に真空ポンプ33を配設し、弁19を閉じて弁30,
弁31を開き、真空ポンプ33と圧縮機21と共働させること
により、真空加熱炉1内を減圧状態(例えば10Torr)に
するまで気体を回収することができ、回収効率を向上さ
せることができる。また、各管路の適所に加熱手段や冷
却手段等、適宜な補助機器を配置して回収や精製等の効
率の向上を図ることもできる。
In addition, a side pipe 32 having valves 30 and 31 with a valve 19 of a pipe 20 on the suction side of the compressor 21 of the gas recovery system 25 is provided, and a vacuum pump 33 is provided in the side pipe 32. And close valve 19 to close valve 30,
By opening the valve 31 and cooperating with the vacuum pump 33 and the compressor 21, the gas can be collected until the inside of the vacuum heating furnace 1 is reduced in pressure (for example, 10 Torr), and the collection efficiency can be improved. . In addition, it is also possible to arrange appropriate auxiliary equipment such as a heating means and a cooling means at an appropriate position in each pipeline to improve the efficiency of recovery and purification.

尚、冷却用気体として窒素,ヘリウム,アルゴンを使
用する場合には、これらに水素を適当量、約4%以下、
好ましくは0.1〜1%含有せしめて用いると、真空加熱
炉1での冷却のための熱伝達を促進せしめたり、処理金
属より脱ガスする酸素や処理系統で漏入してくる酸素を
反応によって水に変化させて除去できるので金属熱処理
上好都合である。
When nitrogen, helium, or argon is used as a cooling gas, an appropriate amount of hydrogen is added to these gases, about 4% or less.
When used in an amount of preferably 0.1 to 1%, heat transfer for cooling in the vacuum heating furnace 1 is promoted, and oxygen degassed from the treated metal or oxygen leaked in the treatment system is subjected to water reaction. This is convenient for metal heat treatment because it can be removed by changing to.

以上のようにして、貯槽12には不純物を除去した冷却
用気体が回収されて貯えられ、この冷却用気体は次の金
属の加熱処理の冷却用に使用される。このように本実施
例によれば、冷却用気体を繰り返し使用することがで
き、気体のコストの低減を図れ、高価なヘリウム等を使
用することも可能となる。また、冷却用気体が繰り返し
の使用で消失して回収量が減少した場合は、貯槽12に付
設したボンベ34等の別途のガス源より適宜貯槽12に補充
すればよい。
As described above, the cooling gas from which impurities have been removed is collected and stored in the storage tank 12, and this cooling gas is used for cooling the next metal heat treatment. As described above, according to this embodiment, the cooling gas can be repeatedly used, the cost of the gas can be reduced, and expensive helium or the like can be used. Further, when the cooling gas disappears due to repeated use and the recovery amount decreases, the storage tank 12 may be appropriately refilled from a separate gas source such as a cylinder 34 attached to the storage tank 12.

次に第2図は、本発明の第2の構成を適用した第2実
施例を示すものである。尚、前記第1図に示した第1実
施例と同一要素のものには同一符号を付してその詳細な
説明を省略する。
Next, FIG. 2 shows a second embodiment to which the second configuration of the present invention is applied. The same elements as those in the first embodiment shown in FIG. 1 are denoted by the same reference numerals, and detailed description thereof will be omitted.

本実施例は、前記第1実施例において気体回収系統25
に設けられていた触媒筒23及び吸着筒24等の気体精製手
段を別の系統に独立させたものである。即ち、貯槽12
と、前記気体回収系統25の圧縮機21の吸入口側にある弁
19とを、弁40,弁41を介して管路42で連結し、該管路42
の弁40と弁41との間に触媒筒23及び吸着筒24を配置して
回収気体精製系統43を構成したものである。
This embodiment is different from the first embodiment in that the gas recovery system 25
The gas purification means, such as the catalyst tube 23 and the adsorption tube 24, provided in the system is made independent of another system. That is, the storage tank 12
And a valve on the suction port side of the compressor 21 of the gas recovery system 25
19 through a valve 40, a valve 41 and a pipe 42, and the pipe 42
The catalyst cylinder 23 and the adsorption cylinder 24 are arranged between the valve 40 and the valve 41 to constitute a recovered gas purification system 43.

そして、本実施例では、前記第1実施例と同様の操作
で真空加熱炉1に冷却用気体を供給し、冷却後の真空加
熱炉1からの冷却用気体を、まず弁27,弁22,弁18,弁13
を開いて真空加熱炉1内の圧力が貯槽12の圧力と平衡に
なる迄供給気体加圧系統28及び気体回収系統25を介して
貯槽12に回収し、次いで平衡に達したら、弁27を閉じ、
弁15、弁19を開くとともに、圧縮機21を駆動して気体回
収系統25を介して冷却用気体を回収する。この場合、回
収される気体は、不純物を含有したまま貯槽12に回収さ
れる。なお真空加熱炉1内の気体をより一層回収しよう
とする場合には、前記第1実施例と同様に、気体回収系
統25の圧縮機21の吸入口側に真空ポンプ33を配した側管
路32を設け、真空ポンプ33を圧縮機21と共働させればよ
い。
In the present embodiment, a cooling gas is supplied to the vacuum heating furnace 1 by the same operation as in the first embodiment, and the cooling gas from the vacuum heating furnace 1 after cooling is first supplied to the valve 27, the valve 22, Valve 18, Valve 13
To recover the gas in the storage tank 12 via the supply gas pressurizing system 28 and the gas recovery system 25 until the pressure in the vacuum heating furnace 1 becomes equilibrium with the pressure in the storage tank 12. Then, when the equilibrium is reached, the valve 27 is closed. ,
The valves 15 and 19 are opened, and the compressor 21 is driven to recover the cooling gas via the gas recovery system 25. In this case, the recovered gas is recovered in the storage tank 12 while containing the impurities. When the gas in the vacuum heating furnace 1 is to be further recovered, a side pipe in which a vacuum pump 33 is disposed on the suction port side of the compressor 21 of the gas recovery system 25 as in the first embodiment. 32 may be provided, and the vacuum pump 33 may cooperate with the compressor 21.

真空加熱炉1からの冷却用気体の回収が終了したら、
弁15を閉じ、弁40,弁41を開とし、圧縮機21により貯槽1
2に回収した不純物を含む気体を回収気体精製系統43か
ら気体回収系統25を経て貯槽12へと循環させる。この循
環により気体中の不純物が触媒筒23及び吸着筒24で順次
除去され、貯槽12内の気体は高純度に精製される。そし
て所望の純度に達したら前記弁40,弁41,弁19,弁22,弁1
8,弁13を閉じるとともに圧縮機21を停止する。これによ
り、貯槽12には不純物を含まない高純度の気体が冷却用
気体として貯えられる。
When the recovery of the cooling gas from the vacuum heating furnace 1 is completed,
The valve 15 is closed, the valves 40 and 41 are opened, and the storage tank 1 is opened by the compressor 21.
The gas containing impurities collected in 2 is circulated from the recovered gas purification system 43 to the storage tank 12 via the gas recovery system 25. By this circulation, impurities in the gas are sequentially removed by the catalyst tube 23 and the adsorption tube 24, and the gas in the storage tank 12 is purified to high purity. When the desired purity is reached, the valves 40, 41, 19, 22, and 1
8, The valve 21 is closed and the compressor 21 is stopped. Thus, high-purity gas containing no impurities is stored in the storage tank 12 as a cooling gas.

また、触媒筒23,吸着筒24は、第1実施例と同様それ
ぞれ複数箇設けて使用と再生の工程を交互に切り替えて
使用すると、連続した長期の運転ができて好都合であ
る。
When a plurality of catalyst cylinders 23 and adsorption cylinders 24 are provided in the same manner as in the first embodiment and the use and regeneration steps are alternately used, a continuous long-term operation can be advantageously performed.

この様に第2実施例では第1実施例のように回収と同
時に冷却に使用した後の気体に含まれている不純物を除
去して回収は出来ないが、回収した後に回収気体精製系
統43,気体回収系統25,貯槽12と繰り返し循環して精製し
得るので、第1実施例より高純度に精製した気体を得る
ことができ、貯槽12に回収貯えられる。この結果、以後
の真空加熱炉1の冷却用として処理金属を汚染すること
なく極めて効果的に使用することができる。
As described above, in the second embodiment, the impurities contained in the gas used for cooling at the same time as the recovery cannot be removed and the recovery cannot be performed as in the first embodiment, but after the recovery, the recovered gas purification system 43, Since the gas can be purified by repeatedly circulating through the gas recovery system 25 and the storage tank 12, a gas purified to a higher purity than in the first embodiment can be obtained and collected and stored in the storage tank 12. As a result, it can be used extremely effectively for cooling the vacuum heating furnace 1 without contaminating the treated metal.

尚、上記両実施例における各弁は、三方弁等を用いて
弁の数を減らすこともできる。また、冷却用気体として
は、前述のごとく各種気体を用いることができるが、特
に、冷却用気体としてヘリウムを用いることにより、窒
素より優れた冷却速度が得られるとともに、水素のよう
な爆発の危険がないので、安心して加圧状態で使用で
き、冷却速度の向上、冷却時間の短縮、焼入れ硬度の向
上等他の気体以上の作用効果を得られる。
The number of valves in each of the above embodiments can be reduced by using a three-way valve or the like. As the cooling gas, various gases can be used as described above. In particular, by using helium as the cooling gas, a cooling rate superior to that of nitrogen can be obtained, and there is a danger of explosion such as hydrogen. Since there is no gas, it can be used in a pressurized state with peace of mind, and it is possible to obtain the effect of improving the cooling rate, shortening the cooling time, improving the quenching hardness, and the like, which are higher than other gases.

〔発明の効果〕 以上説明したように、本発明は、請求項1によれば、
真空加熱炉と冷却用気体を貯蔵した貯槽とを連結した気
体供給系統に、吐出口を前記気体供給系統の気体の流れ
と対向する方向に開口させて配置した圧縮機及び気体精
製手段を設けた気体回収系統の両端を連結し、供給気体
加圧系統の一端を気体回収系統の圧縮機の吐出口側に、
他端を気体供給系統の気体回収系統の真空加熱炉側分岐
部より真空加熱炉側にそれぞれ連結し、請求項2によれ
ば、請求項1の気体供給系統、気体回収系統及び供給気
体加圧系統の連結構成に加えて、貯槽と気体回収系統の
圧縮機の吸入口側とに気体精製手段を設けた回収気体精
製系統を連結したから、気体の加圧供給や加圧回収及び
精製を単一の圧縮機で行うことができるので、装置が簡
略となり装置価格が安価であり、また運転も容易でかつ
運転費用も低減化する等多くの利点がある。
[Effects of the Invention] As described above, according to the present invention,
A gas supply system connecting a vacuum heating furnace and a storage tank storing a cooling gas was provided with a compressor and a gas purifying means arranged with a discharge port opened in a direction opposite to a gas flow of the gas supply system. Connect both ends of the gas recovery system, connect one end of the supply gas pressurization system to the discharge port side of the compressor of the gas recovery system,
The other end is connected to the vacuum heating furnace side from the vacuum heating furnace side branch of the gas recovery system of the gas supply system, and according to claim 2, the gas supply system, the gas recovery system and the supply gas pressurization of claim 1 In addition to the connection of the system, a recovery gas purification system provided with gas purification means is connected to the storage tank and the suction port side of the compressor of the gas recovery system. Since the operation can be performed by one compressor, there are many advantages such as simplification of the apparatus, low cost of the apparatus, easy operation and reduction of the operation cost.

また、本発明は、真空加熱炉に付設した真空排気系統
とは全く別系統の気体供給系統に気体回収系統を連結し
たから、炉内で発生した不純成分の殆どは真空排気系統
から排出でき、回収気体への混入が少なく、しかも、回
収気体に混入した不純成分は、請求項1の発明にあって
は、回収と同時に気体精製手段にて除去できるから、操
作が簡単で、かつ回収後直ちに回収した気体を冷却用に
使用することができて作業上極めて便利である。さら
に、請求項2の発明にあっては、精製する気体を回収気
体精製系統に循環するようにして気体精製手段に繰り返
し通すことができるので、不純物の除去がより一層促進
されて極めて高純度に精製された気体が回収できる。こ
の結果以後の熱処理金属の冷却に使用した際の金属の酸
化等の変性を防止し、その気体特有の効果を発揮するこ
ととなる。
Further, according to the present invention, since the gas recovery system is connected to a completely separate gas supply system from the vacuum exhaust system attached to the vacuum heating furnace, most of the impurity components generated in the furnace can be exhausted from the vacuum exhaust system, In the invention of claim 1, since the contamination with the recovered gas is small, and the impurity components mixed into the recovered gas can be removed by the gas purification means simultaneously with the recovery, the operation is simple and immediately after the recovery. The recovered gas can be used for cooling, which is extremely convenient in operation. Further, in the invention of claim 2, since the gas to be purified can be repeatedly passed through the gas purification means so as to be circulated to the recovery gas purification system, the removal of impurities is further promoted and the purity is extremely high. Purified gas can be recovered. As a result, denaturation such as oxidation of the metal when used for cooling the subsequently heat-treated metal is prevented, and the effect peculiar to the gas is exerted.

しかも、本発明は、冷却に使用した後の気体を回収し
て、これを繰り返し冷却用に再使用することができるの
で、ヘリウムやアルゴン等の特に高価な気体を金属の熱
処理に於ける冷却用として使用することを可能とする。
この結果これら気体の使用によって熱処理金属の品質の
向上が図れる。しかも安価に冷却処理をすることができ
る。
In addition, the present invention can recover gas after use for cooling and reuse it for cooling repeatedly, so that particularly expensive gas such as helium or argon can be used for cooling in heat treatment of metal. It can be used as
As a result, the quality of the heat-treated metal can be improved by using these gases. Moreover, the cooling process can be performed at low cost.

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

第1図は本発明の第1実施例を説明する系統図、第2図
は第2実施例を説明する系統図である。 1…真空加熱炉、12…貯槽、17…気体供給系統、21…圧
縮機、23…触媒筒、24…吸着筒、25…気体回収系統、28
…供給気体加圧系統、43…回収気体精製系統
FIG. 1 is a system diagram illustrating a first embodiment of the present invention, and FIG. 2 is a system diagram illustrating a second embodiment. DESCRIPTION OF SYMBOLS 1 ... Vacuum heating furnace, 12 ... Storage tank, 17 ... Gas supply system, 21 ... Compressor, 23 ... Catalyst cylinder, 24 ... Adsorption cylinder, 25 ... Gas recovery system, 28
… Supply gas pressurization system, 43… Recovery gas purification system

フロントページの続き (72)発明者 日向野 保雄 東京都大田区久が原5丁目33番10号 ウ エキガス科学株式会社内 (56)参考文献 特開 昭63−310915(JP,A) 特開 昭57−41318(JP,A) 特開 昭61−73825(JP,A) 実開 昭56−5998(JP,U) (58)調査した分野(Int.Cl.6,DB名) C21D 1/00,1/773 B22F 3/10 F27B 5/04,9/04,14/04 F27D 7/06,15/02 Continuation of the front page (72) Inventor Yasuo Hinata 5-33-10 Kugahara, Ota-ku, Tokyo Inside Uekigas Science Co., Ltd. (56) References JP-A-63-310915 (JP, A) JP-A-57-41318 (JP, A) JP-A-61-73825 (JP, A) JP-A-56-5998 (JP, U) (58) Fields investigated (Int. Cl. 6 , DB name) C21D 1 / 00,1 / 773 B22F 3/10 F27B 5 / 04,9 / 04,14 / 04 F27D 7 / 06,15 / 02

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】炉内を加熱する加熱器と炉内を真空排気す
る排気手段を有する真空排気系統とを付設してなる真空
加熱炉に冷却用気体に供給する装置であって、前記真空
加熱炉と冷却用気体を貯蔵した貯槽とを連結した管路よ
りなる気体供給系統と、該気体供給系統の管路に両端が
連結した管路に、吐出口を前記気体供給系統の気体の流
れと対向する方向に開口させて配置した圧縮機を設けて
なる気体回収系統と、一端を前記気体回収系統の圧縮機
の吐出口側管路に、他端を前記気体供給系統の管路の前
記気体回収系統の真空加熱炉側分岐部より真空加熱路側
にそれぞれ連結した供給気体加圧系統とを備えるととも
に、前記気体回収系統の管路に触媒筒,吸着筒等の気体
精製手段を配設したことを特徴とする真空加熱炉の冷却
用気体供給装置。
An apparatus for supplying a cooling gas to a vacuum heating furnace provided with a heater for heating the inside of the furnace and a vacuum exhaust system having an exhaust means for evacuating the inside of the furnace, wherein the vacuum heating A gas supply system consisting of a pipe connecting a furnace and a storage tank storing a cooling gas, and a pipe connected at both ends to a pipe of the gas supply system, a discharge port having a gas flow of the gas supply system. A gas recovery system provided with a compressor arranged to be opened in the opposite direction, one end of the gas recovery system having a discharge port side pipeline of the compressor, and the other end of the gas supply system pipeline. A supply gas pressurization system connected to a vacuum heating path side from a vacuum heating furnace side branch of the recovery system, and gas purification means such as a catalyst tube and an adsorption tube are provided in a line of the gas recovery system. A gas supply device for cooling a vacuum heating furnace.
【請求項2】炉内を加熱する加熱器と炉内を真空排気す
る排気手段を有する真空排気系統とを付設してなる真空
加熱炉に冷却用気体を供給する装置であって、前記真空
加熱炉と冷却用気体を貯蔵した貯槽とを連結した管路よ
りなる気体供給系統と、該気体供給系統の管路に両端が
連結した管路に、吐出口を前記気体供給系統の気体の流
れと対向する方向に開口させて配置した圧縮機を設けて
なる気体回収系統と、一端を前記気体回収系統の圧縮機
の吐出口側管路に、他端を前記気体供給系統の管路の前
記気体回収系統の真空加熱炉側分岐部より真空加熱炉側
にそれぞれ連結した供給気体加圧系統と、前記貯槽と前
記気体回収系統に配置した圧縮機の吸入口側とを連結し
た管路に触媒筒,吸着筒等の気体精製手段を配設した回
収気体精製系統とを備えることを特徴とする真空加熱炉
の冷却用気体供給装置。
2. An apparatus for supplying a cooling gas to a vacuum heating furnace provided with a heater for heating the inside of the furnace and an evacuation system having an evacuation unit for evacuating the inside of the furnace, wherein the vacuum heating A gas supply system consisting of a pipe connecting a furnace and a storage tank storing a cooling gas, and a pipe connected at both ends to a pipe of the gas supply system, a discharge port having a gas flow of the gas supply system. A gas recovery system provided with a compressor arranged to be opened in the opposite direction, one end of the gas recovery system having a discharge port side pipeline of the compressor, and the other end of the gas supply system pipeline. A catalyst tube is connected to a pipe connecting the supply gas pressurization system connected to the vacuum heating furnace side from the vacuum heating furnace side branch of the recovery system, and the suction port side of the compressor arranged in the storage tank and the gas recovery system. Gas recovery system equipped with gas purification means, Cooling gas supply device of a vacuum heating furnace, characterized in that it comprises.
JP8053989A 1989-03-31 1989-03-31 Gas supply device for cooling of vacuum heating furnace Expired - Lifetime JP2916686B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8053989A JP2916686B2 (en) 1989-03-31 1989-03-31 Gas supply device for cooling of vacuum heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8053989A JP2916686B2 (en) 1989-03-31 1989-03-31 Gas supply device for cooling of vacuum heating furnace

Publications (2)

Publication Number Publication Date
JPH02259010A JPH02259010A (en) 1990-10-19
JP2916686B2 true JP2916686B2 (en) 1999-07-05

Family

ID=13721158

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8053989A Expired - Lifetime JP2916686B2 (en) 1989-03-31 1989-03-31 Gas supply device for cooling of vacuum heating furnace

Country Status (1)

Country Link
JP (1) JP2916686B2 (en)

Also Published As

Publication number Publication date
JPH02259010A (en) 1990-10-19

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