JPH0571643B2 - - Google Patents
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- Publication number
- JPH0571643B2 JPH0571643B2 JP58248753A JP24875383A JPH0571643B2 JP H0571643 B2 JPH0571643 B2 JP H0571643B2 JP 58248753 A JP58248753 A JP 58248753A JP 24875383 A JP24875383 A JP 24875383A JP H0571643 B2 JPH0571643 B2 JP H0571643B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- gas
- oxygen ratio
- ratio
- 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.)
- Expired - Lifetime
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- Powder Metallurgy (AREA)
Description
【発明の詳細な説明】
(イ) 産業上の利用分野
本発明は、爆発性ガスを使用する真空焼結炉等
の熱処理炉における安全装置に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to a safety device in a heat treatment furnace such as a vacuum sintering furnace that uses explosive gas.
(ロ) 従来技術
例えば、超硬合金の焼結には、近年、その雰囲
気ガスとしてH2、CO、CH4、C3H8等の爆発性を
有するガスを使用する方法が提案され、普及しつ
つある。ところが、この焼結作業は通常真空焼結
炉内で適当な減圧状態の下に実施されるため、万
一炉内に突発的なリークやシール劣化等に起因す
る不慮のリークを発生すると、前記爆発性ガスに
空気(酸素)が混入されて爆発事故を発生するお
それがある。このため、この種の爆発性ガスを使
用する焼結方法では、真空焼結炉の安全対策を確
立することが最大の技術的課題となつている。ま
た、真空焼結炉以外の爆発性ガスを使用する熱処
理炉においても、同様に安全性を確実に保証する
ものが求められている。(b) Prior art For example, in recent years, methods of using explosive gases such as H 2 , CO, CH 4 , and C 3 H 8 as the atmospheric gas have been proposed and become popular for sintering cemented carbide. It is being done. However, since this sintering work is normally carried out in a vacuum sintering furnace under a suitable reduced pressure condition, if an unexpected leak occurs in the furnace due to a sudden leak or seal deterioration, the above-mentioned Air (oxygen) may be mixed with the explosive gas, causing an explosion. Therefore, in sintering methods that use this type of explosive gas, the biggest technical challenge is to establish safety measures for the vacuum sintering furnace. Furthermore, heat treatment furnaces that use explosive gases other than vacuum sintering furnaces are also required to ensure safety in the same way.
(ハ) 目的
本発明は、かかる事情に着目してなされたもの
で、爆発性ガスを使用する熱処理炉において、リ
ーク発生等に起因して炉内ガスの酸素比率に異常
を起こしても、直ちにこれを感知し、かつ即座に
適切な安全処理を自動的に講ずることができるよ
うにした安全装置を提供することを目的とする。(C) Purpose The present invention has been made in view of this situation, and even if an abnormality occurs in the oxygen ratio of the gas in the furnace due to leakage, etc. in a heat treatment furnace that uses explosive gas, the present invention can be used to immediately It is an object of the present invention to provide a safety device that can sense this and automatically take appropriate safety measures immediately.
(ニ) 構成
すなわち、本発明は上記の目的を達成するため
に、熱処理炉内の爆発性ガスの酸素比率を検出す
る酸素比率検出手段と、この酸素比率検出手段か
らの酸素比率情報を受信しているとともに、炉内
ガスの酸素比率が操業条件に応じて設定される爆
発限界比率又はその近傍の比率に達すると危険信
号を出力するように構成された制御手段と、この
制御手段からの危険信号を入力して炉内ガスの酸
素比率を調整する酸素比率調整手段とを具備して
なり、該酸素比率調整手段が、炉内に不活性ガス
を選択的に供給し得るガス供給路が接続されるガ
ス貯留器と、熱処理炉に連通して炉内の雰囲気ガ
スを大気中に放出する放出路に介設される電磁バ
ルブとからなる炉内パージ機構であることを特徴
とするものである。(d) Configuration That is, in order to achieve the above object, the present invention includes an oxygen ratio detection means for detecting the oxygen ratio of explosive gas in a heat treatment furnace, and receives oxygen ratio information from the oxygen ratio detection means. In addition, there is a control means configured to output a danger signal when the oxygen ratio of the gas in the furnace reaches the explosion limit ratio set according to the operating conditions or a ratio in the vicinity thereof, and a control means configured to output a danger signal. an oxygen ratio adjustment means for adjusting the oxygen ratio of the gas in the furnace by inputting a signal, and the oxygen ratio adjustment means is connected to a gas supply path that can selectively supply an inert gas into the furnace. and an electromagnetic valve interposed in a discharge path that communicates with the heat treatment furnace and releases the atmospheric gas in the furnace into the atmosphere. .
(ホ) 実施例
以下、本発明の一実施例を図面を参照して説明
する。(e) Embodiment Hereinafter, an embodiment of the present invention will be described with reference to the drawings.
第1図は、本発明に係る安全装置のシステムを
示し、熱処理炉特にこの場合真空焼結炉1は、ガ
ス導入路aにバルブ2を介し図示されていないガ
ス供給装置と連通されているとともに、ガス排気
路bにバルブ3を介設して真空ポンプ4と連通さ
れている。そして、真空炉1には、炉内に減圧状
態で封入される爆発性ガス中の酸素比率を検出す
るための酸素比率検出手段の1つとしてO2セン
サ5が付設されている。このO2センサ5は、そ
の検出結果を電気信号に変換する変換器6を経由
して酸素比率情報を制御手段7に送信している。 FIG. 1 shows a safety device system according to the present invention, in which a heat treatment furnace, particularly a vacuum sintering furnace 1 in this case, is communicated with a gas supply device (not shown) through a valve 2 in a gas introduction path a. , a gas exhaust path b is connected to a vacuum pump 4 through a valve 3. The vacuum furnace 1 is provided with an O 2 sensor 5 as one of the oxygen ratio detection means for detecting the oxygen ratio in the explosive gas sealed in the furnace under reduced pressure. The O 2 sensor 5 transmits oxygen ratio information to the control means 7 via a converter 6 that converts the detection result into an electrical signal.
制御手段7は、これらの情報を受信していると
ともに、使用ガスの種類や炉容積などの必要な諸
条件を入力して、真空炉1の操業条件に応じて設
定されるところの爆発限界比率をその記憶部分に
記憶している。ここに、爆発限界比率とは各種の
爆発性ガスが化学量論的に固有にもつ爆発可能と
なる酸素比率の上限又は下限の比率をいう。例え
ば、H2ガスの場合では、H25〜75%(空気との
混合比)の割分の範囲で爆発可能で、H2ガス又
は酸素量に過不足があると爆発できない。したが
つて、この場合には爆発限界比率として上記割合
から算出される比率、又はより安全性を増す目的
でその近傍のある一定のセツト比率が記憶され
る。なお酸素量が上限界比率を越えることは通常
予想されないから、下限界比率のみで十分である
が、必要ならばその上限界比率を記憶させておい
てもよい。そして、制御手段7は、その演算部分
で前記酸素比率情報と爆発限界比率とを比較演算
し、酸素比率情報により伝達される炉内爆発性ガ
スの酸素比率が爆発下限界比率またはその近傍の
セツト比率にまで上昇した場合にはその出力部分
より危険信号Oを、次に述べる酸素比率調整手段
に出力するように構成されている。 The control means 7 receives this information, inputs necessary conditions such as the type of gas used and the furnace volume, and sets the explosion limit ratio, which is set according to the operating conditions of the vacuum furnace 1. is stored in its memory. The term "explosive limit ratio" as used herein refers to the upper or lower limit of the stoichiometrically inherent oxygen ratio of various explosive gases at which they can explode. For example, in the case of H 2 gas, it is possible to explode within the range of 5% to 75% H 2 (mixing ratio with air), but it cannot explode if there is an excess or deficiency in the amount of H 2 gas or oxygen. Therefore, in this case, the ratio calculated from the above ratio as the explosion limit ratio, or a certain set ratio in the vicinity thereof, is stored for the purpose of further increasing safety. Note that since it is normally not expected that the oxygen amount exceeds the upper limit ratio, only the lower limit ratio is sufficient, but the upper limit ratio may be stored if necessary. Then, the control means 7 compares and calculates the oxygen ratio information and the explosion limit ratio in its calculation section, and determines whether the oxygen ratio of the in-furnace explosive gas transmitted by the oxygen ratio information is at or near the lower explosion limit ratio. When the oxygen ratio rises to the oxygen ratio, the output section outputs a danger signal O to the oxygen ratio adjustment means described below.
酸素比率調整手段は、炉内に不活性ガスを供給
するガス供給路cに電磁バルブ9を介設して真空
炉1に連通されるガス貯留器8と、真空炉1の雰
囲気ガスを大気中に放出する放出路dに介設した
電磁バルブ10とによつて構成される炉内パージ
機構からなる。すなわち、この炉内パージ機構
は、前記危険Oが供給炉c側の電磁バルブ9と放
出路d側の電磁バルブ10とに同時に入力されて
両バルブ9,10が開成されると、供給路cから
はガス貯留器8に貯留された高圧のN2やCO2等
の不活性ガスを炉内に導入する一方、放出路dか
ら炉内ガスを外気へ駆遂して、炉内ガス中の酸素
比率を瞬時に低下するものである。 The oxygen ratio adjusting means includes a gas reservoir 8 which is connected to the vacuum furnace 1 by interposing an electromagnetic valve 9 in a gas supply path c that supplies an inert gas into the furnace, and a gas reservoir 8 which is connected to the vacuum furnace 1 by supplying an inert gas into the furnace. It consists of an in-furnace purge mechanism comprised of a solenoid valve 10 interposed in a discharge path d for discharging air. That is, in this in-furnace purge mechanism, when the dangerous O is simultaneously input to the solenoid valve 9 on the supply furnace c side and the solenoid valve 10 on the discharge path d side and both valves 9 and 10 are opened, the supply path c Inert gas such as high-pressure N 2 and CO 2 stored in the gas storage device 8 is introduced into the furnace from 1, while the gas in the furnace is discharged to the outside air from the discharge path d, and the gas in the furnace is This instantly lowers the oxygen ratio.
次に、上記構成を具備する安全装置の作動につ
いて説明する。 Next, the operation of the safety device having the above configuration will be explained.
前記制御手段7は、O2センサ5からの酸素比
率情報を受信しているとともに、リーク発生等に
より炉内ガス中の酸素比率の異常な増加をその演
算部分で検出したならば、前述の如く、その出力
部分より危険信号Oを出力して、即座に適切な安
全処置を講ずることになる。これを第2図につい
て具体的に説明すると、真空炉1が減圧制御状態
においてリーク等を発生し、漏入空気が炉内ガス
と混合してその酸素比率が図示矢印Oupのように
下限界比率近傍のセツト圧力にまで上昇したとす
ると、前記制御手段7はその出力部分から前記パ
ーズ機構の電磁バルブ9,10に危険信号Oを出
力する。すると、バルブ9が開成されて炉内にガ
ス貯留器8から不活性ガスが送り込まれる一方、
同時にバルブ10が開成された放出路dからは炉
内の爆発性ガスが外部に放出され、炉内ガス中の
酸素比率は、図示矢印Odownのように急速に低
下される。つまりこのシステムでは爆発性ガス中
の酸素比率が一定以上になると、炉内を不活性ガ
スで急激に置換し爆発の危険を除去するものであ
る。 The control means 7 receives the oxygen ratio information from the O 2 sensor 5, and if its calculation part detects an abnormal increase in the oxygen ratio in the furnace gas due to the occurrence of a leak, etc. , the danger signal O will be output from the output part, and appropriate safety measures will be taken immediately. To explain this in detail with reference to Fig. 2, when the vacuum furnace 1 generates a leak etc. in the depressurization control state, the leaked air mixes with the gas in the furnace, and the oxygen ratio rises to the lower limit ratio as indicated by the arrow Oup in the diagram. If the pressure rises to a nearby set pressure, the control means 7 outputs a danger signal O from its output portion to the electromagnetic valves 9, 10 of the parsing mechanism. Then, the valve 9 is opened and inert gas is sent into the furnace from the gas reservoir 8, while
At the same time, the explosive gas in the furnace is released from the discharge path d where the valve 10 is opened, and the oxygen ratio in the gas in the furnace is rapidly reduced as indicated by the arrow Odown in the figure. In other words, in this system, when the oxygen ratio in the explosive gas exceeds a certain level, the inside of the furnace is rapidly replaced with inert gas to eliminate the risk of explosion.
このように、この安全装置では、仮にリーク発
生等の異常をきたしても炉内の爆発性ガスが化学
的に爆発し得ない一定の酸素比率範囲に保持する
ものであるから、爆発事故のおそれがなく安全性
が確保できる。 In this way, with this safety device, even if an abnormality such as a leak occurs, the explosive gas in the reactor is kept within a certain oxygen ratio range where it cannot chemically explode, thereby reducing the risk of an explosion accident. Safety can be ensured.
なお、本発明の安全装置で使用する酸素比率検
出手段には、種々の原理によるセンサ類、分析装
置等を適用できるが、近時の分析技術の進歩によ
り減圧下においても酸素量(比率)を検出するこ
とは容易になし得る。また、制御手段7は必要な
情報処理機能及び指令出力機を具備するものであ
れば、その内部システムの構成は自由である。 Although sensors and analyzers based on various principles can be applied to the oxygen ratio detection means used in the safety device of the present invention, recent advances in analysis technology have made it possible to detect the oxygen amount (ratio) even under reduced pressure. It can be easily detected. Furthermore, the internal system configuration of the control means 7 is free as long as it has the necessary information processing function and command output device.
また、前記実施例では、酸素比率調整手段とし
て炉内パージ機構を採用する場合を述べたが、こ
れに限定されるものではない。例えば、真空炉1
の前記ガス導入路aと排気路bに位置するバルブ
2,3に危険信号を入力してバルブを各々開成す
るようにし、ガス導入路aから爆発性ガスを補給
しつつ真空ポンプ4で炉内の圧力を下げ炉内ガス
中の酸素比率を調整するようにすることも可能で
ある。 Further, in the above embodiment, a case has been described in which an in-furnace purge mechanism is employed as the oxygen ratio adjusting means, but the present invention is not limited to this. For example, vacuum furnace 1
A danger signal is input to the valves 2 and 3 located in the gas introduction path a and the exhaust path b to open the valves, and while explosive gas is supplied from the gas introduction path a, the vacuum pump 4 is used to vacuum the inside of the furnace. It is also possible to lower the pressure and adjust the oxygen ratio in the furnace gas.
なお、以上の説明では爆発性ガスを減圧下で雰
囲気ガスとして用いる真空熱処理炉の場合を例に
述べたが、本発明の安全装置はこれ以外の大気炉
あるいは加圧炉形式勢の熱処理炉についても同様
に適用される。 In the above explanation, the case of a vacuum heat treatment furnace that uses an explosive gas as the atmospheric gas under reduced pressure has been described as an example, but the safety device of the present invention can also be applied to other atmospheric furnace or pressurized furnace type heat treatment furnaces. The same applies.
(ヘ) 効果
以上のように、本発明の安全装置は酸素比率検
出手段と、制御手段と、酸素比率調整手段とを所
定の結合状態の下に具備し、熱処理炉の爆発性ガ
スが常に一定の爆発不能な酸素比率範囲に保持さ
れるようにしたものであるから、熱処理炉に何等
かの原因で空気が混入するようなことがあつて
も、爆発事故の危険は未然に防止される。したが
つて、叙述の真空焼結炉をはじめとして、爆発性
ガスを使用する熱処理方法等の広汎な実施も可能
となる。(f) Effects As described above, the safety device of the present invention includes an oxygen ratio detection means, a control means, and an oxygen ratio adjustment means in a predetermined combination state, so that the explosive gas in the heat treatment furnace is always kept constant. Since the oxygen ratio is maintained within a non-explosive range, even if air were to get mixed into the heat treatment furnace for some reason, the risk of an explosion would be prevented. Therefore, it becomes possible to implement a wide range of heat treatment methods, including the vacuum sintering furnace described above, as well as heat treatment methods that use explosive gas.
第1図本発明の実施例を示すシステム説明図で
ある。第2図は実施例システムの作動態様は一例
を示す説明図である。
1……真空炉、2,3……バルブ、4……真空
ポンプ、5……O2センサ、6……変換器、7…
…制御手段、8……ガス貯留器、9,10……電
磁バルブ、a……ガス導入路、b……ガス排出
路、c……ガス供給路、d……ガス放出路、O…
…危険信号。
FIG. 1 is a system explanatory diagram showing an embodiment of the present invention. FIG. 2 is an explanatory diagram showing an example of the operating mode of the embodiment system. 1... Vacuum furnace, 2, 3... Valve, 4... Vacuum pump, 5... O 2 sensor, 6... Converter, 7...
...Control means, 8...Gas reservoir, 9, 10...Solenoid valve, a...Gas introduction path, b...Gas discharge path, c...Gas supply path, d...Gas discharge path, O...
…Danger signal.
Claims (1)
る酸素比率検出手段と、この酸素比率検出手段か
らの酸素比率情報を受信しているとともに、炉内
ガスの酸素比率が操業条件に応じて設定される爆
発限界比率又はその近傍の比率に達すると危険信
号を出力するように構成された制御手段と、この
制御手段からの危険信号を入力して炉内ガスの酸
素比率を調整する酸素比率調整手段とを具備して
なり、該酸素比率調整手段が、炉内に不活性ガス
を選択的に供給し得るガス供給路が接続されるガ
ス貯留器と、熱処理炉に連通して炉内の雰囲気ガ
スを大気中に放出する放出路に介設される電磁バ
ルブとからなる炉内パージ機構であることを特徴
とする熱処理炉における安全装置。1 Oxygen ratio detection means for detecting the oxygen ratio of the explosive gas in the heat treatment furnace, receiving oxygen ratio information from this oxygen ratio detection means, and setting the oxygen ratio of the gas in the furnace according to operating conditions. a control means configured to output a danger signal when the explosion limit ratio reached or a ratio in the vicinity thereof; and an oxygen ratio adjustment that adjusts the oxygen ratio of the gas in the furnace by inputting the danger signal from the control means. a gas reservoir connected to a gas supply path capable of selectively supplying an inert gas into the furnace; and a gas reservoir connected to the heat treatment furnace to control the atmosphere in the furnace. A safety device for a heat treatment furnace, characterized in that it is an in-furnace purge mechanism consisting of an electromagnetic valve interposed in a discharge path that discharges gas into the atmosphere.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24875383A JPS60138004A (en) | 1983-12-26 | 1983-12-26 | Safety equipment in heat treatment furnaces |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24875383A JPS60138004A (en) | 1983-12-26 | 1983-12-26 | Safety equipment in heat treatment furnaces |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60138004A JPS60138004A (en) | 1985-07-22 |
| JPH0571643B2 true JPH0571643B2 (en) | 1993-10-07 |
Family
ID=17182857
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24875383A Granted JPS60138004A (en) | 1983-12-26 | 1983-12-26 | Safety equipment in heat treatment furnaces |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60138004A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0273915A (en) * | 1988-09-07 | 1990-03-13 | Mitsui High Tec Inc | Bright annealing method for metal material |
| JPH04103725A (en) * | 1990-08-22 | 1992-04-06 | Nippon Steel Corp | Oxygen-free quenching device for continuous annealing furnace |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5544144U (en) * | 1978-09-18 | 1980-03-22 | ||
| DE3211247A1 (en) * | 1982-03-26 | 1983-10-06 | Riedhammer Ludwig Gmbh | Process for reducing the oxygen content of the atmosphere of a continuous annealing furnace, and annealing furnace to perform this process |
-
1983
- 1983-12-26 JP JP24875383A patent/JPS60138004A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60138004A (en) | 1985-07-22 |
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