JPS5952705B2 - Vacuum carburizing method - Google Patents
Vacuum carburizing methodInfo
- Publication number
- JPS5952705B2 JPS5952705B2 JP13496278A JP13496278A JPS5952705B2 JP S5952705 B2 JPS5952705 B2 JP S5952705B2 JP 13496278 A JP13496278 A JP 13496278A JP 13496278 A JP13496278 A JP 13496278A JP S5952705 B2 JPS5952705 B2 JP S5952705B2
- Authority
- JP
- Japan
- Prior art keywords
- carburizing
- furnace
- gas
- vacuum
- period
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C8/06—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C8/06—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases
- C23C8/08—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases only one element being applied
- C23C8/20—Carburising
- C23C8/22—Carburising of ferrous surfaces
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C8/80—After-treatment
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Solid-Phase Diffusion Into Metallic Material Surfaces (AREA)
Description
【発明の詳細な説明】
この発明は真空浸炭法、特に炉内で有機浸炭スの分解に
伴つて発生する炭素を利用して金属材を浸炭処理する方
法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a vacuum carburizing method, particularly to a method for carburizing metal materials using carbon generated as organic carburizing gas is decomposed in a furnace.
メタンガス(CH4)、プロタン、ブタン等の有機ガス
を炉内で熱分解してこの炉内に置かれた金属部材を浸炭
処理する場合従来では次のような方法がとられている。
すなわち、被浸炭処理物を真空炉内に配置して加熱する
一方、有機液体を(場合によつてはこのガスをさらに熱
分解したもの)炉内に滴下供給しガス化させて炉内を浸
炭温度に保持しながら浸炭処理を行なう方法で、この場
合浸炭量を制御するためには炉内のガスを採取して赤外
線分析器で功−ホンポテンシャルを測定し、炉内のカー
ボンポテンシャルが所定の値に保持されるように有機液
体の供給量を調整することにより行なつている。しかし
、このような方法では、被処理物の形状、被処理物どう
しの接触部、あるいは被処理物の孔部等の部分のガスは
、停溜しがちとなるので従つて新たに外部から供給され
てくるガスとの置換も充分には行なわれない。BACKGROUND ART When pyrolyzing organic gases such as methane gas (CH4), propane, butane, etc. in a furnace and carburizing metal members placed in the furnace, the following method has conventionally been used.
In other words, the material to be carburized is placed in a vacuum furnace and heated, while an organic liquid (in some cases, this gas is further thermally decomposed) is dripped into the furnace and gasified to carburize the inside of the furnace. This is a method of carburizing while maintaining the temperature. In this case, in order to control the amount of carburization, the gas in the furnace is sampled and the carbon potential is measured with an infrared analyzer, and the carbon potential in the furnace is determined to be at a specified level. This is done by adjusting the amount of organic liquid supplied to maintain the same value. However, in this method, the gas tends to accumulate in the shape of the objects to be treated, the contact areas between the objects, or the holes in the objects, so it is necessary to newly supply the gas from the outside. Replacement with the incoming gas is also not sufficient.
そのために、カーボンポテンシャルの値が所定の値に保
持されるのは、ガスの交換がうまく行なわれる部分だけ
となり、炉内に配置されたすべての被処理物に対して目
標とする浸炭処理をほどこすことが困難であつた。この
発明は、このような問題点を解決した新規な真空浸炭方
法を提供しようとするところにあり、その要部とすると
ころは、真空排気された炉内に供給される浸炭ガスの分
解に伴つて生ずる炭素によつて浸炭反応させて金属部材
を浸炭処理すクる方法において、上記炉内に新鮮な浸炭
ガスを充填する行程、浸炭ガスの分解に伴う炉内ガス圧
力の変化を検出する行程、検出された炉内ガス圧力が所
定値以上になつたとき、炉内を一坦真空排気する行程の
一連の行程を繰返し行うようにしたと5ころにある。Therefore, the carbon potential value is maintained at a predetermined value only in areas where gas exchange is successful, and the targeted carburizing treatment is applied to all the workpieces placed in the furnace. It was difficult to rub. The purpose of this invention is to provide a new vacuum carburizing method that solves these problems. In a method of carburizing a metal member by causing a carburizing reaction with the carbon generated by the carburizing process, a step of filling the above-mentioned furnace with fresh carburizing gas, and a step of detecting a change in the gas pressure in the furnace as the carburizing gas is decomposed. 5. When the detected gas pressure in the furnace exceeds a predetermined value, a series of steps for uniformly evacuating the inside of the furnace is repeatedly performed.
次にこの発明を1実例の要部説明図である第1図および
炉内における浸炭処理の時間的経過を説明するための第
2図に基ずいてさらに詳述する。Next, the present invention will be further described in detail based on FIG. 1, which is a diagram illustrating the main parts of one example, and FIG. 2, which illustrates the time course of carburizing treatment in a furnace.
第1図において、1は真空炉、2は加熱炉、3は被処理
物、4は加熱ヒータ、5は加熱ヒータ4の制御部、6は
浸炭ガス溜部、7は真空排気係、8は冷却ガス溜部、9
,10,11は開閉弁および12は焼入れ用の油溜部、
13は加熱炉2内の圧力を検出する圧力検出器である。
第2図において、折れ線mは加熱炉2内の温度の経時変
化を示すものであり、上に行くほど温度が高くなること
を示している。In FIG. 1, 1 is a vacuum furnace, 2 is a heating furnace, 3 is a workpiece, 4 is a heater, 5 is a control unit for the heater 4, 6 is a carburizing gas reservoir, 7 is a vacuum pumping section, and 8 is a Cooling gas reservoir, 9
, 10, 11 are on-off valves; 12 is an oil reservoir for quenching;
13 is a pressure detector that detects the pressure inside the heating furnace 2.
In FIG. 2, a polygonal line m indicates a change in temperature within the heating furnace 2 over time, and indicates that the temperature increases as it goes upward.
折れ線nは加熱炉2内の真空度の経時変化を示すもので
あり、折れ線nが下に行くほど真空度が高くなることを
示している。期間T,,t,,t。はそれぞれ実際に浸
炭が行なわれている時間を示している。区間A−Gは浸
炭処理の各段階を示すもので、区間Aは真空炉1の排気
期間、区間Bは被処理物3を浸炭温度まで到達するよう
に加熱する加熱期間、区間Cは主に浸炭処理中である浸
炭期間、区間Dは拡散処理中である拡散期間、区間Eは
冷却期間、区間Fは被処理物3の再加熱期間、区間Gは
焼入れのための油冷却期間である。まず、被処理物3が
真空炉1内の加熱炉2の中に配置されると開閉弁10が
開かれて真空排気系7によつて真空炉1および加熱炉2
内を真空排気する(第2図の排気期間Aに相当する)。A polygonal line n indicates a change over time in the degree of vacuum within the heating furnace 2, and indicates that the lower the polygonal line n goes, the higher the degree of vacuum becomes. Period T,,t,,t. Each indicates the time during which carburizing is actually performed. Sections A to G indicate each stage of the carburizing process. Section A is the evacuation period of the vacuum furnace 1, section B is the heating period for heating the workpiece 3 to reach the carburizing temperature, and section C is mainly the The carburizing period is the carburizing process, section D is the diffusion period during the diffusion process, section E is the cooling period, section F is the reheating period of the workpiece 3, and section G is the oil cooling period for quenching. First, when the workpiece 3 is placed in the heating furnace 2 in the vacuum furnace 1, the on-off valve 10 is opened and the vacuum exhaust system 7 pumps the vacuum furnace 1 and the heating furnace 2.
The inside is evacuated (corresponding to the evacuation period A in FIG. 2).
この排気が終了すると、被処理物3が、まず加熱ヒータ
4によつて加熱され、制御部5によつて被処理物3の温
度はT,に保持される(第2図の加熱期間Bに相当する
)。そして次に開閉弁9が開かれて浸炭ガス(本実施例
ではメタンガス)が浸炭ガス溜部6から加熱炉2内に充
填されはじめ加熱炉2内ガス圧力がP,になると浸炭ガ
スの充填が停止され、浸炭反応が開始される。浸炭反応
が進むと、メタンガスの分解(CH.→C+2H,)し
たもののうち炭素ガスは反応で消費されるが、水素ガス
は残留するために、反応の進行に伴つて加熱炉2内の圧
力は徐々に上昇(いいかえれば真空度が低下)してくる
。圧力が上昇するということは反応に必要なメタンガス
が不足することであり、加熱炉2内の圧力がP,に達す
ると、開閉弁10を開いて加熱炉2内を真空排気し(浸
炭処理はもちろんいつたん停止する)してしまい、改め
て新鮮なメタンガスを再度ガス圧力P,になるまで充填
した後さきほどと同様に浸炭反応を繰返す(第2図の浸
炭期間に相当する)。この繰返し回数は被処理物3の種
類、量および浸炭の程度に応じて決定される。実際の正
味の浸炭時間は加熱炉2内のガス圧力がP,とP。の間
にある区間(第2図でいうと期間T,,t,,t,)を
合せた期間となる。浸炭(反応)が終了すると再度開閉
弁10を開いて、真空排気して、真空中で被処理物3の
表面炭素濃度の拡散処理を一定時間行い(第2図の拡散
期間Dに相当する)。その後加熱炉2の加熱を停止せし
めて被処理物3を変態点以下の、温度まで冷却し結晶粒
の微細化を行う(第2図の冷却期間Eに相当する)。最
後に再度被処理物3を再加熱して、真空炉1中に取り出
すとともにこの真空炉1中に窒素ガスを導びき入れ、被
処理物を油溜部12に投入して焼入れする。以上詳述し
たようにこの発明は炉内のメタンガスをある圧力範囲(
あるカーボンポテンシヤルの範囲)だけを繰返し使用す
ることによつて、処理物表面積に関係なく一定のカーボ
ンポテンシヤル範囲内での浸炭処理が行えると同時に使
用ずみのガスはいつたん排気され新たなガスが隅々まで
供給されるので被処理物どうしの接触部あるいは被処理
物の孔部を均一に浸炭することができる。When this evacuation ends, the workpiece 3 is first heated by the heater 4, and the temperature of the workpiece 3 is maintained at T by the control unit 5 (during the heating period B in FIG. Equivalent to). Then, the on-off valve 9 is opened and carburizing gas (methane gas in this embodiment) starts to be filled into the heating furnace 2 from the carburizing gas reservoir 6. When the gas pressure inside the heating furnace 2 reaches P, the carburizing gas is filled. The carburizing reaction is started. As the carburizing reaction progresses, carbon gas among the decomposed methane gas (CH.→C+2H,) is consumed in the reaction, but hydrogen gas remains, so as the reaction progresses, the pressure inside the heating furnace 2 decreases. It gradually rises (in other words, the degree of vacuum decreases). An increase in pressure means a shortage of methane gas necessary for the reaction, and when the pressure inside the heating furnace 2 reaches P, the on-off valve 10 is opened to evacuate the inside of the heating furnace 2 (the carburizing process is Of course, the carburizing reaction is repeated in the same way as before (corresponding to the carburizing period in Figure 2) after filling with fresh methane gas until the gas pressure reaches P. The number of repetitions is determined depending on the type and amount of the object 3 to be treated and the degree of carburization. The actual net carburizing time is determined by the gas pressure in the heating furnace 2 being P and P. This period is the sum of the sections between the two (periods T,, t,, t, in FIG. 2). When the carburization (reaction) is completed, the on-off valve 10 is opened again, the vacuum is evacuated, and the surface carbon concentration of the object to be treated 3 is diffused for a certain period of time in a vacuum (corresponding to the diffusion period D in Fig. 2). . Thereafter, the heating of the heating furnace 2 is stopped and the workpiece 3 is cooled to a temperature below the transformation point to refine the crystal grains (corresponding to the cooling period E in FIG. 2). Finally, the workpiece 3 is reheated and taken out into the vacuum furnace 1, nitrogen gas is introduced into the vacuum furnace 1, and the workpiece is put into the oil reservoir 12 and hardened. As described in detail above, this invention allows methane gas in the furnace to be controlled within a certain pressure range (
By repeatedly using only a certain carbon potential range), carburizing can be carried out within a certain carbon potential range regardless of the surface area of the workpiece, and at the same time, the used gas is exhausted and new gas is introduced into the corner. Since the carburizing agent is supplied up to each point, it is possible to uniformly carburize the contact areas between the objects to be treated or the pores of the objects to be treated.
さらに従来のようにガス中の炭素濃度を検出して逐時ガ
スを供給する浸炭炉では、炉内のカーボンポテンシヤル
を一定に保つために雰囲気攪拌装置を炉内に設ける必要
があつたがこの発明においては不要である。このように
この発明の効果は顕著であり被処理物の浸炭処理の精度
を著しく向上させることができる。Furthermore, in conventional carburizing furnaces that detect the carbon concentration in the gas and supply gas at any time, it is necessary to install an atmosphere stirring device in the furnace in order to keep the carbon potential in the furnace constant. It is not necessary in . As described above, the effects of the present invention are remarkable, and the accuracy of carburizing treatment of objects to be treated can be significantly improved.
第1図はこの発明の1実施例の要部説明図、第2図は炉
内における浸炭処理の時間的経過を説明するための図で
ある。
1 ・・・・・・真空炉、2 ・・・・・・加熱炉、3
・・・・・・被処理物、4 ・・・・・・加熱ヒータ
、5 ・・・・・・制御部、6 ・・・・・・浸炭ガス
溜部、7・・・・・・真空排気系、8・・・・・・冷却
ガス溜部、9,10,11・・・・・・開閉弁、12・
・・・・・油溜部。FIG. 1 is an explanatory diagram of a main part of an embodiment of the present invention, and FIG. 2 is a diagram for explaining the time course of carburizing treatment in a furnace. 1 ... Vacuum furnace, 2 ... Heating furnace, 3
...Product to be treated, 4 ...Heating heater, 5 ...Control section, 6 ...Carburizing gas reservoir, 7 ...Vacuum Exhaust system, 8...Cooling gas reservoir, 9, 10, 11... Opening/closing valve, 12.
...Oil sump.
Claims (1)
伴つて生ずる炭素によつて浸炭反応を起こせ金属部材を
浸炭処理する浸炭方法において、つぎの(1)〜(3)
の行程を順次繰返し行うようにしたことを特徴とする真
空浸炭方法。 (1)炉内に新鮮な浸炭ガスを充填する行程。 (2)浸炭ガスの分解に伴う炉内ガス圧力の変化検出す
る行程。(3)検出された炉内ガス圧力が所定値以上に
なたとき、炉内を一坦真空排気する行程。[Scope of Claims] 1. A carburizing method for carburizing a metal member by causing a carburizing reaction with carbon generated as a result of the decomposition of carburizing gas supplied into an evacuated furnace, comprising the following (1) to ( 3)
A vacuum carburizing method characterized by sequentially repeating the following steps. (1) Filling the furnace with fresh carburizing gas. (2) A process to detect changes in gas pressure in the furnace due to decomposition of carburizing gas. (3) When the detected gas pressure in the furnace exceeds a predetermined value, the inside of the furnace is evacuated.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13496278A JPS5952705B2 (en) | 1978-10-31 | 1978-10-31 | Vacuum carburizing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13496278A JPS5952705B2 (en) | 1978-10-31 | 1978-10-31 | Vacuum carburizing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5562159A JPS5562159A (en) | 1980-05-10 |
| JPS5952705B2 true JPS5952705B2 (en) | 1984-12-21 |
Family
ID=15140644
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13496278A Expired JPS5952705B2 (en) | 1978-10-31 | 1978-10-31 | Vacuum carburizing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5952705B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012007240A (en) * | 2011-07-19 | 2012-01-12 | Ihi Corp | Method and device for controlling quality of vacuum carburization, and vacuum carburizing furnace |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58126975A (en) * | 1982-01-22 | 1983-07-28 | Komatsu Ltd | Carburizing method by vacuum carburizing furnace |
| DE10152204B4 (en) * | 2001-10-23 | 2004-01-22 | Schwäbische Härtetechnik Ulm GmbH | Device and method for measuring and / or regulating the carburizing atmosphere in a vacuum carburizing plant |
-
1978
- 1978-10-31 JP JP13496278A patent/JPS5952705B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012007240A (en) * | 2011-07-19 | 2012-01-12 | Ihi Corp | Method and device for controlling quality of vacuum carburization, and vacuum carburizing furnace |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5562159A (en) | 1980-05-10 |
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