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JP2001081543A - Vacuum carburizing method - Google Patents

Vacuum carburizing method

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Publication number
JP2001081543A
JP2001081543A JP26019299A JP26019299A JP2001081543A JP 2001081543 A JP2001081543 A JP 2001081543A JP 26019299 A JP26019299 A JP 26019299A JP 26019299 A JP26019299 A JP 26019299A JP 2001081543 A JP2001081543 A JP 2001081543A
Authority
JP
Japan
Prior art keywords
carburizing
amount
gas
laser
carburization
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.)
Pending
Application number
JP26019299A
Other languages
Japanese (ja)
Inventor
Yutaka Takeda
豊 武田
Hitoshi Ota
均 太田
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.)
Chugai Ro Co Ltd
Original Assignee
Chugai Ro 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 Chugai Ro Co Ltd filed Critical Chugai Ro Co Ltd
Priority to JP26019299A priority Critical patent/JP2001081543A/en
Publication of JP2001081543A publication Critical patent/JP2001081543A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To prevent a generation of soot even in the case where hydrocarbon gas of >=2 carbon atoms is adopted and to carry out uniform carburizing treatment. SOLUTION: Hydrocarbon gas is introduced into a heating chamber, and carburizing treatment is performed under reduced pressure. In this vacuum carburizing method, hydrocarbon gas of prescribed amount is introduced for a prescribed time at the beginning of carburizing. The amount of subsequent introduction of the hydrocarbon gas is gradually decreased according to the predetermined pattern to carry out carburizing or is continuously controlled on the basis of the set amount of transmission of laser in the heating chamber.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は真空浸炭方法、具体
的には、真空炉中に炭化水素系ガスを直接供給して、被
処理材表面に浸炭を行い、引き続き真空下で熱処理する
方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vacuum carburizing method, and more specifically, to a method of directly supplying a hydrocarbon-based gas into a vacuum furnace to carburize a surface of a material to be treated, and subsequently performing a heat treatment under vacuum. Things.

【0002】[0002]

【従来の技術】真空浸炭は、被処理材を真空中で浸炭温
度まで加熱し、均熱状態に達した時点でメタン(C
4)、プロパン(C38)、プロピレン(C36)、エチレ
ン(C24)或いはアセチレン(C22)等の浸炭性ガス
(炭化水素系ガス)を炉内に直接供給し、所定時間保持し
て浸炭を行い、引き続き真空下で所定時間保持して拡散
処理するものであるが、結晶粒粗大化の虞がある被処理
材については結晶粒度微細化の目的で拡散処理後にA1
変態以下に冷却した後、再加熱を行って焼き入れが行わ
れる。
2. Description of the Related Art Vacuum carburizing involves heating a material to be treated to a carburizing temperature in a vacuum and, when a uniform temperature is reached, methane (C).
H 4), propane (C 3 H 8), propylene (C 3 H 6), ethylene (C 2 H 4) or acetylene (C 2 H 2) carburizing gas such as
(Carbon-based gas) is directly supplied into the furnace, carburized by holding for a predetermined time, and then diffusion is performed by holding for a predetermined time under vacuum. For the material, after diffusion treatment for the purpose of reducing the crystal grain size, A 1
After cooling below the transformation, reheating is performed and quenching is performed.

【0003】このように、真空浸炭では生の炭化水素系
ガスを用いてAcm線上で行う飽和浸炭であることから、
他の浸炭方法のように浸炭雰囲気の炭素ポテンシャルを
制御して表面炭素濃度を調節する方法を採用することが
できない。そのため、真空浸炭では浸炭時間と拡散時間
とを管理することにより所望の表面炭素量と浸炭硬化深
さを得るようにしている。この場合、被処理材の単位表
面積当りの浸炭に必要な炭素量は、理論的に算出できる
が、浸炭の初期と後半とでは所要炭素量が異なる。
As described above, vacuum carburization is a saturated carburization performed on an Acm line using a raw hydrocarbon gas.
A method of controlling the carbon potential of the carburizing atmosphere to adjust the surface carbon concentration as in other carburizing methods cannot be adopted. Therefore, in vacuum carburization, a desired amount of surface carbon and a desired carburized hardening depth are obtained by controlling the carburizing time and the diffusion time. In this case, the amount of carbon required for carburizing per unit surface area of the material to be treated can be theoretically calculated, but the required amount of carbon differs between the initial stage and the latter half of carburizing.

【0004】ちなみに、真空浸炭における炭素吸収の進
行を調べるため、例えば、浸炭温度1000℃、有効浸
炭深さ1.0mmの場合を想定して、真空浸炭における炭
素吸収量を測定したところ、図3に示す結果が得られ
た。なお、図3には、浸炭開始から5分までは1分毎
に、以後は5分毎に計測した値をプロットしてある。図
3に示す結果から、浸炭開始後の1分間で全浸炭必要炭
素量の約20%の炭素量が、また浸炭開始後の5分間で
全浸炭必要炭素量の約40%の炭素量が吸収されること
が判る。
Incidentally, in order to examine the progress of carbon absorption in vacuum carburization, the amount of carbon absorption in vacuum carburization was measured assuming, for example, a case of 1000 ° C. and an effective carburization depth of 1.0 mm. The result shown in FIG. Note that FIG. 3 plots values measured every 1 minute from the start of carburization to 5 minutes and thereafter every 5 minutes. From the results shown in FIG. 3, the carbon content of about 20% of the total carburization required in 1 minute after the start of carburization and the carbon content of about 40% of the total carburization required in 5 minutes after the start of carburization were absorbed. It turns out that it is done.

【0005】ところで、実操業では、理論必要炭素量に
基づき算出した炭化水素ガス量を供給量にすると浸炭の
バラツキが避けられないことから、安定した浸炭層を得
るため理論必要炭素量の2〜3倍の浸炭性ガス(炭化水
素ガス)を供給して浸炭処理が行われることと、前述し
たように処理中の雰囲気の炭素ポテンシャルを制御でき
ないこととが相俟って、炉内のスーティングが避けられ
ず、被処理材表面に煤が付着して光輝状態を維持できな
いという問題がある。
In actual operation, if the amount of hydrocarbon gas calculated based on the theoretically required amount of carbon is used as the supply amount, variations in carburizing cannot be avoided. The carburizing process is performed by supplying three times the carburizing gas (hydrocarbon gas), and the carbon potential of the atmosphere during the process cannot be controlled as described above, so that the sooting in the furnace is performed. However, there is a problem that the soot adheres to the surface of the material to be treated and the glittering state cannot be maintained.

【0006】この問題を解決する方法として、特公昭5
8−48626号公報により、処理(浸炭)室の一部に開
口を設け、この開口から排出される雰囲気中の煤煙の発
生による光線路の遮断を発光器・受光器により検知し
て、煤煙発生を検知した時点で炭化水素の供給を停止
し、煤煙の消滅による光線路の遮断解除後、再び一定量
の炭化水素ガスを供給するようにし、煤煙の発生及び消
滅を利用して間欠的に浸炭性ガスの供給を制御する方法
が提案されている。
As a method for solving this problem, Japanese Patent Publication No. Sho 5
According to Japanese Patent Application Laid-Open No. 8-48626, an opening is provided in a part of a processing (carburizing) chamber, and interruption of an optical line due to generation of soot in the atmosphere discharged from the opening is detected by a light emitting device and a light receiving device to generate soot. At the point of detection, the supply of hydrocarbons is stopped, and after releasing the cutoff of the optical line due to the disappearance of soot, a certain amount of hydrocarbon gas is supplied again, and intermittent carburization is performed using the generation and disappearance of soot. A method for controlling the supply of a reactive gas has been proposed.

【0007】[0007]

【発明が解決しようとする課題】しかしながら、前記方
法では煤煙発生の有無を浸炭処理室から抽出されるサン
プリングガスにより検知するため、制御遅れが避けられ
ず、しかも、浸炭性ガスの供給停止を煤煙発生検知時点
としているため、煤煙が断続的に発生する状態で浸炭す
ることになり、被処理材表面に煤が付着することを完全
に防止できないという問題がある。
However, in the above method, since the presence or absence of soot generation is detected by the sampling gas extracted from the carburizing chamber, a control delay is inevitable, and the supply of carburizing gas is stopped when the soot is stopped. Since the point of occurrence is detected, carburization occurs in a state in which soot is generated intermittently, and there is a problem that soot cannot be completely prevented from adhering to the surface of the material to be treated.

【0008】また、前記方法では、浸炭性ガスとしてメ
タンガス(CH4)を採用した場合、熱分解時の連鎖反応
の律速段階となるメチルラジカル生成反応が遅いため、
煤煙による光線路の遮断を検知して炭化水素の供給を停
止させても制御遅れによる悪影響は比較的少ないが、浸
炭性ガスとして、例えば、プロパンガス(C38)などの
炭素数2以上の炭化水素系ガスを用いた場合、1000
゜C程度の高温下では分解速度が前記メタン基生成反応に
比べて数千倍と極めて速いため、多量の煤が発生するこ
とから、制御遅れは致命的な欠陥となり、被処理材表面
への煤の付着防止や均一な浸炭処理を行うことができな
いという問題がある。
In the above method, when methane gas (CH 4 ) is used as the carburizing gas, a methyl radical generation reaction, which is a rate-determining step of a chain reaction during thermal decomposition, is slow.
Even if the supply of hydrocarbons is stopped by detecting the interruption of the optical line due to soot, the adverse effect due to the control delay is relatively small, but as a carburizing gas, for example, a carbon number of 2 or more such as propane gas (C 3 H 8 ) When a hydrocarbon-based gas of
At a high temperature of about ゜ C, the decomposition rate is several thousand times faster than the methane group generation reaction, and a large amount of soot is generated. There is a problem that prevention of soot adhesion and uniform carburizing cannot be performed.

【0009】従って、本発明は、炭素数2以上の炭化水
素系ガスを採用した場合でも、煤の発生を防止し、均一
な浸炭処理を行うことができるようにすることを目的と
するものであり、下記の知見に基づいて為されたもので
ある。
Accordingly, an object of the present invention is to prevent the generation of soot and perform a uniform carburizing treatment even when a hydrocarbon-based gas having 2 or more carbon atoms is employed. Yes, based on the following findings.

【0010】即ち、図3に示す結果から、真空浸炭で
は、浸炭の初期には浸炭性ガスの送入量を多くする必要
があるが、浸炭の後期には浸炭性ガスの送入量を少なく
しても良いことが判る。
That is, from the results shown in FIG. 3, in the case of vacuum carburization, it is necessary to increase the amount of carburizing gas to be introduced at the beginning of carburizing, but to reduce the amount of carburizing gas to be introduced at the latter stage of carburizing. It turns out that you may do it.

【0011】また、前述したように、浸炭の初期と浸炭
の後期とでは鋼材など被処理材が吸収する炭素量を異に
することから、真空浸炭における雰囲気中の炭素原子量
は変動するとの観点に基づき、浸炭期に一定量の浸炭性
ガスを送入しながら雰囲気のレーザー透過量を測定した
ところ、図4に示す結果が得られ、同図から浸炭初期に
おけるレーザー透過量はほぼ一定であるが、時間の経過
とともにレーザー透過量は減衰することが明らかとなっ
た。このことは、浸炭の初期を除いて鋼材が吸収する炭
素量以上の浸炭性ガスが存在すること、すなわち、鋼材
に吸収されない炭素原子が存在していることを意味し、
また、雰囲気中の炭素原子量と雰囲気のレーザー透過量
とは相関関係を有するを意味する。
Further, as described above, since the amount of carbon absorbed by the material to be treated such as steel is different between the initial stage of carburizing and the latter stage of carburizing, the carbon atom amount in the atmosphere in vacuum carburizing varies. When the laser transmission amount of the atmosphere was measured while supplying a constant amount of carburizing gas during the carburizing period, the result shown in FIG. 4 was obtained. From the figure, the laser transmission amount in the initial stage of carburizing was almost constant. It was found that the amount of laser transmission attenuated over time. This means that except for the initial stage of carburizing, the presence of a carburizing gas equal to or greater than the amount of carbon absorbed by the steel material, that is, the presence of carbon atoms that are not absorbed by the steel material,
Further, it means that the amount of carbon atoms in the atmosphere and the laser transmission amount in the atmosphere have a correlation.

【0012】[0012]

【課題を解決するための手段】本発明は、前記課題を解
決するための手段として、加熱室内に炭化水素系ガスを
送入して減圧下で浸炭処理する真空浸炭方法において、
浸炭開始時に所定量の炭化水素系ガスを一定時間送入
し、その後の浸炭期における炭化水素系ガスの送入量を
漸減させて浸炭するようにしたものである。
According to the present invention, there is provided a vacuum carburizing method for feeding a hydrocarbon-based gas into a heating chamber and performing carburizing treatment under reduced pressure as means for solving the above-mentioned problems.
At the start of carburization, a predetermined amount of hydrocarbon-based gas is supplied for a certain period of time, and then the amount of hydrocarbon-based gas supplied during the carburization period is gradually reduced to perform carburization.

【0013】また、他の観点からみれば、本発明は、加
熱室内に炭化水素系ガスを送入して減圧下で浸炭処理す
る真空浸炭方法において、浸炭開始時に所定量の炭化水
素系ガスを送入し、その後の浸炭期における炭化水素系
ガスの送入量を前記加熱室内におけるレーザーの設定透
過量に基づき制御するようにしたものである。
From another viewpoint, the present invention relates to a vacuum carburizing method in which a hydrocarbon-based gas is fed into a heating chamber and carburized under reduced pressure. The amount of the hydrocarbon-based gas to be supplied during the subsequent carburizing period is controlled based on the set transmission amount of the laser in the heating chamber.

【0014】好ましい実施態様においては、前記レーザ
ーの設定透過量は、浸炭開始時におけるレーザー透過量
より5〜10%減衰した時点のレーザー透過量に設定さ
れる。これは、設定透過量が5%未満の減衰量では、遊
離炭素原子の濃度が低すぎて浸炭に時間を要し、また、
10%を超える減衰量では、遊離炭素原子の濃度が高く
なり過ぎて、その濃度増加と共に煤が徐々に発生するよ
うになるからである。
In a preferred embodiment, the set transmission amount of the laser is set to a laser transmission amount at the time when the laser transmission amount is attenuated by 5 to 10% from the laser transmission amount at the start of carburizing. This is because, when the set permeation amount is less than 5%, the concentration of free carbon atoms is too low and carburization takes time, and
If the amount of attenuation exceeds 10%, the concentration of free carbon atoms becomes too high, soot is gradually generated as the concentration increases.

【0015】前記炭化水素系ガスとしては、メタン(C
4)、プロパン(C38)、プロピレン(C36)、エチレ
ン(C24)或いはアセチレン(C22)等の公知の浸炭性
ガスを採用できるが、処理時間の短縮化のためには炭素
数2以上の炭化水素系ガスを単独で又は二種以上を組み
合わせて使用するのが好ましい。
As the hydrocarbon-based gas, methane (C
H 4 ), propane (C 3 H 8 ), propylene (C 3 H 6 ), ethylene (C 2 H 4 ), or a known carburizing gas such as acetylene (C 2 H 2 ) can be used. For shortening, it is preferable to use a hydrocarbon gas having 2 or more carbon atoms alone or in combination of two or more.

【0016】一般に、真空浸炭の処理過程は、昇温期、
浸炭期及び拡散期に分けられるが、前記浸炭期及び拡散
期の温度は、通常、800〜1200゜Cの範囲内の温度
で被処理材に応じて適宜設定される。また、浸炭期の圧
力は、通常、6.7KPa以下、好ましくは0.013〜1.
3KPaの圧力下で行われる。
In general, the process of vacuum carburization is performed during a heating period,
The temperature is divided into a carburization period and a diffusion period, and the temperature during the carburization period and the diffusion period is usually set appropriately at a temperature in the range of 800 to 1200 ° C. depending on the material to be treated. The pressure during the carburization period is usually 6.7 KPa or less, preferably 0.013 to 1.0.
It is performed under a pressure of 3 KPa.

【0017】また、浸炭雰囲気中の遊離炭素原子の濃度
を検出するため、単色性で指向性に優れ、炉内雰囲気中
に放出された遊離炭素原子の影響を受けやすいレーザー
が採用される。このレーザーを浸炭雰囲気に放射し、こ
れを透過したレーザーの量を検出するため、レーザー光
源及びレーザー光受光器が採用され、これらは対向して
炉壁部に配設される。
In order to detect the concentration of free carbon atoms in the carburizing atmosphere, a laser which is monochromatic, has excellent directivity, and is easily affected by free carbon atoms emitted into the furnace atmosphere is employed. In order to radiate this laser into a carburizing atmosphere and detect the amount of laser transmitted therethrough, a laser light source and a laser light receiver are employed, which are disposed on the furnace wall so as to face each other.

【0018】[0018]

【発明の実施の形態】本発明方法は、例えば、図1に示
す構造の真空浸炭炉を用いて実施することができる。図
において、真空浸炭炉を構成する炉本体1は、その上部
に炉内ガスを撹拌する循環ファン2を備え、炉壁部3に
浸炭性ガス供給口4及びガス排気口7がそれぞれ形成さ
れている。また、前記炉本体1内の加熱室5は前記浸炭
性ガス供給口4に接続された浸炭性ガス供給ライン6を
介して浸炭性ガス供給源(図示せず)に接続されると共
に、前記ガス排気口7に接続された真空排気系ライン8
を介して真空排気装置(図示せず)に接続されている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The method of the present invention can be carried out, for example, using a vacuum carburizing furnace having a structure shown in FIG. In the drawing, a furnace body 1 constituting a vacuum carburizing furnace is provided with a circulation fan 2 for stirring gas inside the furnace at an upper part thereof, and a carburizing gas supply port 4 and a gas exhaust port 7 are formed in a furnace wall 3 respectively. I have. The heating chamber 5 in the furnace main body 1 is connected to a carburizing gas supply source (not shown) through a carburizing gas supply line 6 connected to the carburizing gas supply port 4. Evacuation system line 8 connected to exhaust port 7
Is connected to a vacuum evacuation device (not shown).

【0019】前記炉本体1の炉壁部3には加熱室5を挟
んでレーザー投光器9とレーザー受光器10が対向して
配置され、これらは変換器11と共に炉内雰囲気のレー
ザー透過量を検出するレーザー透過量検出手段を構成
し、レーザー投光器9から放射されたレーザービーム
は、炉内の加熱室5を経て対向するレーザー受光器10
に入射し、その透過量はレーザー受光器10及び変換器
11によりレーザー透過量に対応する電気的信号として
検出され、その検出値が制御装置12に入力される。
A laser projector 9 and a laser receiver 10 are disposed on the furnace wall 3 of the furnace body 1 with the heating chamber 5 interposed therebetween, and they detect the amount of laser transmission in the furnace atmosphere together with the converter 11. The laser beam emitted from the laser projector 9 is transmitted through the heating chamber 5 in the furnace.
And the transmission amount is detected as an electrical signal corresponding to the laser transmission amount by the laser receiver 10 and the converter 11, and the detected value is input to the control device 12.

【0020】前記制御装置12は、炉内雰囲気のレーザ
ー透過量を透過量検出手段により検出された検出値に基
づき、図2に示すように、レーザー透過量が設定透過量
に維持されるように、浸炭性ガス供給ライン6に配設さ
れた流量制御器13、例えば、マスフローメータあるい
はコントロールモータバルブを制御して、加熱室5内に
供給する浸炭性ガス量を漸減させるようにしてある。
The controller 12 controls the laser transmission amount in the furnace atmosphere based on the detection value detected by the transmission amount detection means so that the laser transmission amount is maintained at the set transmission amount as shown in FIG. The amount of carburizing gas supplied into the heating chamber 5 is gradually reduced by controlling a flow rate controller 13 provided in the carburizing gas supply line 6, for example, a mass flow meter or a control motor valve.

【0021】実施に際しては、まず、真空排気装置によ
り前記炉本体1内を0.013KPa程度の真空に排気
し、次いで材料を真空中で浸炭処理温度、例えば、10
00゜Cまで加熱する。均熱に達した後、浸炭性ガス供給
口4から浸炭性ガス、例えば、プロパンガス30体積%
とプロピレンガス70体積%とからなる混合ガスを炉内
に送入し、浸炭が行われる。
In practice, the inside of the furnace main body 1 is first evacuated to a vacuum of about 0.013 KPa by a vacuum evacuation device, and then the material is carburized at a temperature of, for example, 10% in a vacuum.
Heat to 00 ° C. After reaching soaking, the carburizing gas supply port 4 feeds a carburizing gas, for example, 30% by volume of propane gas.
And a mixed gas of 70% by volume of propylene gas are fed into the furnace to perform carburization.

【0022】浸炭性ガス送入と同時に、レーザー投光器
9からレーザーが加熱室5内に放射され、加熱室5内を
透過してレーザー受光器10に到達し、そこで透過量が
検出される。この透過量は変換器11により電気的信号
に変換され、浸炭開始時のレーザー透過量として制御装
置12に入力され、当該レーザー透過量に基づいて浸炭
期の設定透過量が設定される。この設定透過量は、浸炭
開始時点におけるレーザー透過量を100%とし、その
透過量から5〜10%、例えば、10%減衰した量のレ
ーザー透過量に設定される。
Simultaneously with the supply of the carburizing gas, a laser is emitted from the laser projector 9 into the heating chamber 5, passes through the heating chamber 5 and reaches the laser receiver 10, where the amount of transmission is detected. This transmission amount is converted into an electric signal by the converter 11 and input to the control device 12 as the laser transmission amount at the start of carburization, and the set transmission amount in the carburizing period is set based on the laser transmission amount. The set transmission amount is set to a laser transmission amount of 5 to 10%, for example, 10% attenuated from the transmission amount, with the laser transmission amount at the start of carburization as 100%.

【0023】炉内に理論必要炭素量の3倍の前記混合ガ
ス(浸炭性ガス)を送入すると、熱分解により炭素原子が
生成して炉内に放出される結果、図2に示すように、加
熱室5内の鋼材部品の全表面が浸炭温度におけるAcm線
の飽和値に達した時点から加熱室5内を透過するレーザ
ーの透過量が低下する。この炉内雰囲気のレーザー透過
量はレーザー受光器10により常時検出され、その検出
値は前記制御装置12により前記設定透過量と比較さ
れ、前記検出値が設定透過量にまで低下すると、前記制
御装置12から信号が出力され、その信号により流量制
御器13が開度を小さくするように制御され、加熱室5
内に供給する浸炭性ガスの送入量が低減される。
When the mixed gas (carburizing gas), which is three times the theoretically required amount of carbon, is fed into the furnace, carbon atoms are generated by thermal decomposition and released into the furnace, as shown in FIG. When the entire surface of the steel part in the heating chamber 5 reaches the saturation value of the Acm line at the carburizing temperature, the transmission amount of the laser transmitted through the heating chamber 5 decreases. The laser transmission amount of the atmosphere in the furnace is constantly detected by the laser light receiver 10, and the detected value is compared with the set transmission amount by the control device 12, and when the detected value decreases to the set transmission amount, the control device A signal is output from the heating chamber 12 and the flow controller 13 is controlled by the signal to reduce the opening.
The amount of carburizing gas supplied to the inside is reduced.

【0024】なお、レーザー透過量の低下開始時間を短
くする、即ち、煤の発生しない範囲でできるだけ多量の
浸炭性ガスを送入することで浸炭ムラを軽減でき、前記
低下開始時点から浸炭期の時間を管理することにより、
浸炭深さをより正確にすることができる。
It is to be noted that the carburizing unevenness can be reduced by shortening the start time of the decrease in the amount of laser transmission, that is, by feeding in as much carburizing gas as possible within a range where soot is not generated. By managing time,
The carburization depth can be made more accurate.

【0025】浸炭性ガスの送入量を低減させた直後は、
被処理材に吸収される炭素原子の量が浸炭性ガスの熱分
解により発生する炭素原子の量よりも多くなるため、レ
ーザー透過量は一時的に増加する傾向を示すが、時間の
経過と共に被処理材が吸収する炭素量が減少するため雰
囲気内の炭素原子量が増大し、炉内雰囲気中のレーザー
透過量が再び低下し始める。この炉内雰囲気中のレーザ
ー透過量が再び設定透過量にまで低下すると、制御装置
12により流量制御器13の開度が更に減少させられる
ため、加熱室5内に供給する浸炭性ガスの送入量が更に
減少し、以後、同様にして加熱室5内に供給する浸炭性
ガス量が連続的に減少させられ、浸炭終了までレーザー
透過量が浸炭開始時のレーザー透過量の90%に維持さ
れる。浸炭が終わると、浸炭性ガスの送入が停止され、
加熱室5内は再び0.13KPa程度の真空にまで排気さ
れ、前記温度に維持して拡散が行われる。
Immediately after the amount of carburizing gas has been reduced,
Since the amount of carbon atoms absorbed by the material to be treated becomes larger than the amount of carbon atoms generated by the thermal decomposition of the carburizing gas, the amount of laser transmission tends to increase temporarily, but the amount of laser transmission tends to increase over time. Since the amount of carbon absorbed by the treatment material decreases, the amount of carbon atoms in the atmosphere increases, and the laser transmission amount in the furnace atmosphere starts to decrease again. When the laser transmission amount in the furnace atmosphere again decreases to the set transmission amount, the opening of the flow controller 13 is further reduced by the control device 12, so that the carburizing gas supplied into the heating chamber 5 is supplied. Thereafter, the amount of carburizing gas supplied into the heating chamber 5 is continuously decreased in the same manner, and the laser transmission amount is maintained at 90% of the laser transmission amount at the start of carburizing until the end of carburizing. You. When carburizing is over, the supply of carburizing gas is stopped,
The inside of the heating chamber 5 is again evacuated to a vacuum of about 0.13 KPa, and diffusion is performed while maintaining the temperature.

【0026】なお、前記実施例においては、加熱室内の
炉内雰囲気を通るレーザー透過量を検出し、その検出値
が設定透過量に維持されるように浸炭性ガスの送入量を
漸減させるように制御しているが、これの代わりに真空
浸炭炉の規模や被処理材のサイズ、量、所望の表面炭素
量、浸炭深さ等に基づいて予め設定した制御パターンに
従って浸炭期における炭化水素系ガスの送入量を漸減さ
せるようにしても良い。
In the above embodiment, the amount of laser transmission through the furnace atmosphere in the heating chamber is detected, and the amount of carburizing gas supplied is gradually reduced so that the detected value is maintained at the set transmission amount. However, instead of this, the hydrocarbon system in the carburizing period according to a control pattern set in advance based on the scale of the vacuum carburizing furnace, the size and amount of the material to be treated, the desired surface carbon amount, the carburizing depth, etc. The gas supply amount may be gradually reduced.

【0027】[0027]

【発明の効果】従って、本発明によれば、浸炭開始時に
所定量の炭化水素系ガスを一定時間送入し、その後の浸
炭期における炭化水素系ガスの送入量を漸減させながら
浸炭するため、炉内に過剰な浸炭性ガスが存在するのを
防止でき、煤の発生を回避できる。
Therefore, according to the present invention, a predetermined amount of hydrocarbon-based gas is supplied for a certain period of time at the start of carburization, and then carburizing is performed while gradually reducing the amount of hydrocarbon-based gas supplied during the carburization period. In addition, it is possible to prevent the presence of excessive carburizing gas in the furnace, and to prevent the generation of soot.

【0028】また、炉内雰囲気のレーザー透過量を炉内
で直接検出し、この検出値に基づき浸炭性ガスの供給量
を制御するため、浸炭性ガスの供給制御遅れがなく、ま
た、浸炭期における炉内雰囲気の炭素原子量を間接的に
把握することとなり、煤の発生を確実に回避できるとと
もに、浸炭性ガスの必要供給量の変動要因である浸炭処
理温度、被処理材の総表面積及び浸炭の経過に関係な
く、煤の発生を防止し、かつ、浸炭ムラを回避する浸炭
性ガスの供給量を維持できる。
Further, since the amount of laser transmission in the furnace atmosphere is directly detected in the furnace and the supply amount of the carburizing gas is controlled based on the detected value, there is no delay in the control of the supply of the carburizing gas. Indirectly grasps the carbon atomic weight in the furnace atmosphere at the time of the above, soot generation can be reliably avoided, and the carburizing temperature, the total surface area and the carburizing Irrespective of the progress of the carburization, it is possible to prevent the generation of soot and maintain the supply amount of the carburizing gas for avoiding the carburizing unevenness.

【0029】更に、浸炭性ガスの供給量を制御する基準
値として、浸炭開始時におけるレーザー透過量より5〜
10%減衰した時点のレーザー透過量を採用しているた
め、浸炭ムラを防止すると同時に、煤の発生を回避でき
る。
Further, the reference value for controlling the supply amount of the carburizing gas is 5 to 5
Since the laser transmission amount at the time of attenuation by 10% is employed, it is possible to prevent carburization unevenness and to avoid soot generation.

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

【図1】 本発明方法に使用する浸炭装置の構成図、FIG. 1 is a configuration diagram of a carburizing apparatus used in the method of the present invention,

【図2】 本発明方法におけるレーザー透過量の制御パ
ターンと浸炭性ガス送入量と関係を示す図
FIG. 2 is a diagram showing a relationship between a control pattern of a laser transmission amount and a carburizing gas supply amount in the method of the present invention.

【図3】 浸炭深さと炭素量との関係を示すグラフFIG. 3 is a graph showing the relationship between carburization depth and carbon content.

【図4】 レーザー透過量と浸炭時間との関係を示すグ
ラフ
FIG. 4 is a graph showing a relationship between a laser transmission amount and a carburizing time.

【符号の説明】[Explanation of symbols]

1…炉本体 2…循環ファン 3…炉壁部 4…浸炭性ガス供給口 5…加熱室 6…浸炭性ガス供給ライン 7…ガス排気口 8…真空排気系ライン 9…レーザー投光器 10…レーザー受光器 11…変換器 12…制御装置 13…流量制御器 DESCRIPTION OF SYMBOLS 1 ... Furnace main body 2 ... Circulation fan 3 ... Furnace wall part 4 ... Carburizing gas supply port 5 ... Heating chamber 6 ... Carburizing gas supply line 7 ... Gas exhaust port 8 ... Vacuum exhaust system line 9 ... Laser projector 10 ... Laser reception Unit 11 ... Converter 12 ... Control device 13 ... Flow controller

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 加熱室内に炭化水素系ガスを送入して減
圧下で浸炭処理する真空浸炭方法において、浸炭開始時
に所定量の炭化水素系ガスを一定時間送入し、その後の
浸炭期における炭化水素系ガスの送入量を漸減させて浸
炭することを特徴とする真空浸炭方法。
In a vacuum carburizing method in which a hydrocarbon-based gas is fed into a heating chamber and carburized under reduced pressure, a predetermined amount of a hydrocarbon-based gas is fed for a certain time at the start of carburization, A vacuum carburizing method characterized by gradually reducing the amount of hydrocarbon-based gas to be fed and carburizing.
【請求項2】 加熱室内に炭化水素系ガスを送入して減
圧下で浸炭処理する真空浸炭方法において、浸炭開始時
に所定量の炭化水素系ガスを送入し、その後の浸炭期に
おける炭化水素系ガスの送入量を前記加熱室内における
レーザーの設定透過量に基づき制御することを特徴とす
る真空浸炭方法。
2. A vacuum carburizing method in which a hydrocarbon-based gas is fed into a heating chamber and carburized under reduced pressure, wherein a predetermined amount of a hydrocarbon-based gas is fed at the start of carburization, and the hydrocarbon in a subsequent carburizing period is introduced. A vacuum carburizing method characterized by controlling an amount of system gas to be supplied based on a set transmission amount of a laser in the heating chamber.
【請求項3】 レーザーの設定透過量が、浸炭開始時に
おけるレーザー透過量より5〜10%減衰した時点のレ
ーザー透過量であることを特徴とする請求項2記載の真
空浸炭方法。
3. The vacuum carburizing method according to claim 2, wherein the set transmission amount of the laser is a laser transmission amount when the laser transmission amount is attenuated by 5 to 10% from the laser transmission amount at the start of carburizing.
JP26019299A 1999-09-14 1999-09-14 Vacuum carburizing method Pending JP2001081543A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
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Publications (1)

Publication Number Publication Date
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Family

ID=17344618

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Country Status (1)

Country Link
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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002365276A (en) * 2001-06-04 2002-12-18 Dowa Mining Co Ltd Method and apparatus for measuring carbon concentration in reduced pressure atmosphere
WO2003048405A1 (en) * 2001-11-30 2003-06-12 Koyo Thermo Systems Co., Ltd. Method and apparatus for vacuum heat treatment
EP1306462A3 (en) * 2001-10-23 2003-10-29 Schwäbische Härtetechnik Ulm GmbH Process and apparatus for measuring and controlling the carburising atmosphere in a vacuum carburising installation
WO2003104516A1 (en) * 2002-06-11 2003-12-18 光洋サーモシステム株式会社 Method of gas carburizing
WO2005003401A1 (en) * 2003-07-03 2005-01-13 Koyo Thermo Systems Co., Ltd. Method for gas carburizing
JP2005350729A (en) * 2004-06-10 2005-12-22 Ishikawajima Harima Heavy Ind Co Ltd Vacuum carburizing method
US7416614B2 (en) 2002-06-11 2008-08-26 Koyo Thermo Systems Co., Ltd. Method of gas carburizing
WO2008102684A1 (en) 2007-02-23 2008-08-28 Ihi Corporation Carburizing apparatus and carburizing method
US8317939B2 (en) 2003-06-12 2012-11-27 Koyo Thermo Systems Co., Ltd. Method of gas carburizing
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Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002365276A (en) * 2001-06-04 2002-12-18 Dowa Mining Co Ltd Method and apparatus for measuring carbon concentration in reduced pressure atmosphere
EP1306462A3 (en) * 2001-10-23 2003-10-29 Schwäbische Härtetechnik Ulm GmbH Process and apparatus for measuring and controlling the carburising atmosphere in a vacuum carburising installation
US7357843B2 (en) 2001-11-30 2008-04-15 Koyo Thermo Systems Co., Ltd. Vacuum heat treating method and apparatus therefor
WO2003048405A1 (en) * 2001-11-30 2003-06-12 Koyo Thermo Systems Co., Ltd. Method and apparatus for vacuum heat treatment
WO2003104516A1 (en) * 2002-06-11 2003-12-18 光洋サーモシステム株式会社 Method of gas carburizing
US7416614B2 (en) 2002-06-11 2008-08-26 Koyo Thermo Systems Co., Ltd. Method of gas carburizing
US8317939B2 (en) 2003-06-12 2012-11-27 Koyo Thermo Systems Co., Ltd. Method of gas carburizing
WO2005003401A1 (en) * 2003-07-03 2005-01-13 Koyo Thermo Systems Co., Ltd. Method for gas carburizing
US7029540B2 (en) 2003-07-03 2006-04-18 Koyo Thermo Systems Co., Ltd. Method of gas carburizing
JP2005350729A (en) * 2004-06-10 2005-12-22 Ishikawajima Harima Heavy Ind Co Ltd Vacuum carburizing method
WO2008102684A1 (en) 2007-02-23 2008-08-28 Ihi Corporation Carburizing apparatus and carburizing method
WO2019182140A1 (en) * 2018-03-22 2019-09-26 日本製鉄株式会社 Vacuum carburization processing method, and method for manufacturing carburized component
JP6583600B1 (en) * 2018-03-22 2019-10-02 日本製鉄株式会社 Vacuum carburizing treatment method and carburized parts manufacturing method
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JPWO2021039911A1 (en) * 2019-08-29 2021-03-04
CN114341392A (en) * 2019-08-29 2022-04-12 日本制铁株式会社 Vacuum carburization method and method for manufacturing carburized component
JP7201092B2 (en) 2019-08-29 2023-01-10 日本製鉄株式会社 Vacuum carburizing treatment method and carburized part manufacturing method
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