JP2003119558A - Method for vacuum carburizing steel part - Google Patents

Method for vacuum carburizing steel part

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Publication number
JP2003119558A
JP2003119558A JP2001313884A JP2001313884A JP2003119558A JP 2003119558 A JP2003119558 A JP 2003119558A JP 2001313884 A JP2001313884 A JP 2001313884A JP 2001313884 A JP2001313884 A JP 2001313884A JP 2003119558 A JP2003119558 A JP 2003119558A
Authority
JP
Japan
Prior art keywords
carburizing
gas
vacuum
kpa
heating chamber
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
JP2001313884A
Other languages
Japanese (ja)
Inventor
Yoshikazu Shimozato
吉計 下里
Kenichi Tanaka
健一 田中
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 JP2001313884A priority Critical patent/JP2003119558A/en
Publication of JP2003119558A publication Critical patent/JP2003119558A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To reduce consumption of expensive unsaturated hydrocarbon gas, and miniaturize a vacuum exhaust system, along with forming a uniform carburized layer. SOLUTION: In a method for vacuum carburizing steel parts in a reduced pressure, this carburizing method is characterized by carburizing the steel parts in the unsaturated hydrocarbon gas with a first predetermined reduced pressure, and then carburizing them in the saturated hydrocarbon gas with a second predetermined reduced pressure, in the carburizing stage.

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】本発明は鋼材部品の真空浸炭
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 method for vacuum carburizing steel parts.

【0002】[0002]

【従来の技術】従来、鋼材表面の耐摩耗性等の機械的性
質を向上させる表面処理法の一形態として真空浸炭処理
が行われている。この真空浸炭処理は、鋼材部品を真空
中で870〜1000℃の浸炭温度まで加熱し、均熱状
態に達した時点で浸炭ガスを加熱室内に供給すると共
に、加熱室内を前記浸炭処理温度に維持した状態で所定
の減圧下(通常、10〜70KPa)で所定時間保持す
ることにより行うものである。
2. Description of the Related Art Conventionally, vacuum carburizing treatment has been carried out as one form of a surface treatment method for improving mechanical properties such as wear resistance of a steel material surface. In this vacuum carburizing process, steel parts are heated to a carburizing temperature of 870 to 1000 ° C. in a vacuum, and when a soaking state is reached, carburizing gas is supplied into the heating chamber and the heating chamber is maintained at the carburizing temperature. In this state, it is carried out by holding for a predetermined time under a predetermined reduced pressure (usually 10 to 70 KPa).

【0003】この真空浸炭処理においては、例えば、真
空浸炭処理に於ける浸炭時間と鋼材中の炭素濃度プロフ
ァイルを示す図3から判るように、全浸炭量の46%が
浸炭初期の5分間に供給されることから、鋼材部品の全
表面に均一に浸炭層を形成するためには、浸炭初期に鋼
材部品の全表面が浸炭ガスに均一に、かつ、十分に晒さ
れることが重要となる。また、アセチレンガス等の鎖状
不飽和炭化水素を浸炭ガスとして使用する場合は、熱分
解速度が速いため、加熱室内或いは真空排気系において
煤の発生を回避する必要がある。この煤の発生を防止す
るため、特許第2963869号公報にて、浸炭ガスと
してアセチレン系ガスを使用し、1KPa以下の減圧下
で鋼材部品を真空浸炭する方法が提案されている。具体
的には、全浸炭期にアセチレンガスを連続的に供給する
一方、連続的に排気することで炉内圧力を1KPa以下
に維持して浸炭処理するものである。
In this vacuum carburizing process, for example, as can be seen from FIG. 3 showing the carburizing time and the carbon concentration profile in the steel material in the vacuum carburizing process, 46% of the total carburizing amount is supplied within 5 minutes of the initial carburizing process. Therefore, in order to uniformly form the carburized layer on the entire surface of the steel part, it is important that the entire surface of the steel part is uniformly and sufficiently exposed to the carburizing gas at the initial carburization stage. Further, when a chain unsaturated hydrocarbon such as acetylene gas is used as a carburizing gas, the rate of thermal decomposition is high, so it is necessary to avoid soot generation in the heating chamber or the vacuum exhaust system. In order to prevent the generation of soot, Japanese Patent No. 2963869 proposes a method in which an acetylene-based gas is used as a carburizing gas and a steel part is vacuum carburized under a reduced pressure of 1 KPa or less. Specifically, the acetylene gas is continuously supplied during the entire carburizing period, while continuously exhausting the gas to carry out the carburizing treatment while maintaining the furnace pressure at 1 KPa or less.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、この方
法では、全浸炭期における炉内圧を1KPa以下に維持
し、かつ、アセチレンガスの導入が行われるため、煤の
発生は回避できるものの、処理量が大である場合には浸
炭層の均―性が十分でなく、また、アセチレンガスの消
費量が多くなり、さらには、真空排気系が大型化すると
いう問題がある。
However, in this method, the pressure inside the furnace during the entire carburization period is maintained at 1 KPa or less and acetylene gas is introduced, so that the generation of soot can be avoided, but the treatment amount is small. If it is large, there is a problem that the uniformity of the carburized layer is not sufficient, the consumption of acetylene gas is large, and the vacuum exhaust system becomes large.

【0005】従って、本発明は、均一な浸炭層を形成す
るとともに、高価な不飽和炭化水素ガスの消費量の低減
並びに真空排気系の小型化を図ることを課題とするもの
である。
Therefore, it is an object of the present invention to form a uniform carburized layer, reduce consumption of expensive unsaturated hydrocarbon gas, and miniaturize a vacuum exhaust system.

【0006】[0006]

【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、鋼材部品を減圧下で浸炭処理
する真空浸炭方法において、浸炭期に第一所定減圧下の
不飽和炭化水素系ガス下に引続き、第二所定減圧下の飽
和炭化水素系ガス下で浸炭処理するようにしたものであ
る。
Means for Solving the Problems As a means for solving the above problems, the present invention provides a vacuum carburizing method for carburizing steel parts under reduced pressure, wherein an unsaturated hydrocarbon under a first predetermined reduced pressure during a carburizing period. The carburizing process is carried out under a second predetermined reduced pressure of a saturated hydrocarbon gas under a system gas.

【0007】ここで、第一所定減圧下とは不飽和炭化水
素系ガスの熱分解により処理材表面に煤が付着せず、か
つ、浸炭初期における炭素供給量を確実に確保できる真
空度をいい、使用する不飽和炭化水素系ガスの種類によ
って規定され、また、第二所定減圧下とは飽和炭化水素
系ガスの熱分解により処理材表面に煤が付着せず、か
つ、鋼材部品の全体を浸炭ガスで晒すことができる真空
度をいい、使用する飽和炭化水素系ガスの種類によって
規定されるものである。
Here, the term "first predetermined reduced pressure" means a degree of vacuum in which soot does not adhere to the surface of the treated material due to thermal decomposition of the unsaturated hydrocarbon type gas and the carbon supply amount can be reliably secured in the initial carburization stage. Specified by the type of unsaturated hydrocarbon gas used, and under the second predetermined reduced pressure, soot does not adhere to the surface of the treated material due to thermal decomposition of the saturated hydrocarbon gas, and the entire steel part is It refers to the degree of vacuum that can be exposed to carburizing gas, and is defined by the type of saturated hydrocarbon gas used.

【0008】本発明に係る浸炭処理方法では、浸炭期を
初期と後期の二段階に分けて浸炭処理を行うが、浸炭期
初期に使用する浸炭ガスである前記不飽和炭化水素系ガ
スとしては、エチレン、アセチレン等が挙げられ、これ
らは単独で又は混合して使用できる。また、浸炭期後期
に使用する浸炭ガスである前記飽和炭化水素系ガスとし
ては、メタン、エタン、プロパン、ブタンなどが挙げら
れ、これらは単独で又は混合して使用できるが、コスト
的な観点からは、13A都市ガス(CH 88%、C
6%、C 3%、C10 3%)を
使用するのが好適である。
In the carburizing process according to the present invention, the carburizing process is carried out by dividing the carburizing stage into two stages, an initial stage and a latter stage. As the unsaturated hydrocarbon type gas which is the carburizing gas used at the early stage of the carburizing period, Examples thereof include ethylene and acetylene, which can be used alone or in combination. The saturated hydrocarbon-based gas, which is a carburizing gas used in the latter part of the carburizing period, includes methane, ethane, propane, butane, etc. These can be used alone or in a mixture, but from the viewpoint of cost. Is 13A city gas (CH 4 88%, C
2 H 6 6%, C 3 H 8 3%, C 4 H 10 3%) are preferably used.

【0009】本発明の実施態様においては、1.5〜3.
5KPaのアセチレンガス下で浸炭処理を5〜15分間
行い、これに引続き5.0〜8.0KPaの13A都市ガ
ス下で浸炭処理を10〜60分間行なう。
In an embodiment of the present invention, 1.5-3.
Carburizing is carried out under acetylene gas of 5 KPa for 5 to 15 minutes, and subsequently, carburizing is carried out under 13A city gas of 5.0 to 8.0 KPa for 10 to 60 minutes.

【0010】浸炭期初期の圧力を1.5KPa〜3.5K
Paの範囲内に設定したのは、次の理由による。即ち、
浸炭期の初期の圧力設定値が3.5KPa以下では、アセ
チレンガスの熱分解によって生じた煤が処理材表面に付
着することを回避できるが、3.5KPaを超えると、加
熱室内でアセチレンガスの熱分解によって煤が多量に発
生し処理材表面に煤が付着するのを回避するのが困難と
なるためである。また、前記圧力設定値が1.5KPa未
満では均一な浸炭層を得るのに重要な要素である浸炭初
期時におけるアセチレンガスの供給量を確実に確保する
ことができなくなるからである。
The pressure in the early carburizing period is 1.5 KPa to 3.5 K
The reason for setting within the range of Pa is as follows. That is,
When the initial pressure setting value of the carburizing period is 3.5 KPa or less, it is possible to avoid the soot generated by the thermal decomposition of acetylene gas from adhering to the surface of the treated material, but if it exceeds 3.5 KPa, the acetylene gas in the heating chamber This is because it is difficult to avoid that soot is generated in large quantities due to thermal decomposition and soot adheres to the surface of the treated material. Further, if the pressure set value is less than 1.5 KPa, it becomes impossible to reliably secure the supply amount of acetylene gas at the initial carburization, which is an important factor for obtaining a uniform carburized layer.

【0011】また、前記浸炭期後期の圧力を5.0〜8.
0KPaの範囲内に設定したのは、次の理由による。即
ち、浸炭期後期での浸炭処理は、アセチレンガスに比べ
て13A都市ガスの分解速度が著しく遅く、即ち、13
A都市ガスの主成分であるメタンの分解速度がアセチレ
ンガスの1/1000程度と分解し難く、加熱室内の圧
力を高くしても(即ち、加熱室内での滞留時間を長くし
ても)、浸炭ガスの分解に伴う煤の発生は少なく処理材
への煤の付着をも防止できるが、浸炭ガスを処理材表面
に確実に接触させて均一化するためには少なくとも5.
0KPa必要であり、5.0KPa未満では浸炭ムラを生
じ易く、8.0KPaを超えると、煤溜まりを生じ易くな
るからである。
The pressure in the latter half of the carburizing period is 5.0 to 8.
The reason for setting the range within 0 KPa is as follows. That is, in the carburizing treatment in the latter stage of the carburizing period, the decomposition rate of 13A city gas was significantly slower than that of acetylene gas, that is, 13C.
A The decomposition rate of methane, which is the main component of city gas, is about 1/1000 that of acetylene gas, which is difficult to decompose, and even if the pressure in the heating chamber is increased (that is, the residence time in the heating chamber is increased), Soot is not generated due to the decomposition of carburizing gas and soot can be prevented from adhering to the treated material, but at least 5.
This is because 0 KPa is required, and if it is less than 5.0 KPa, carburizing unevenness is likely to occur, and if it exceeds 8.0 KPa, soot accumulation is likely to occur.

【0012】[0012]

【発明の実施の形態】本発明に係る鋼材の真空浸炭処理
方法は、バッチ式真空浸炭炉や連続式真空浸炭炉など任
意の形態でも実施できるが、ここでは図2に示すバッチ
式二室型真空浸炭炉を用い、かつ、浸炭期初期の浸炭ガ
スとしてアセチレンガスを、浸炭期後期の浸炭ガスとし
て13A都市ガスを用いる場合を例に挙げて説明する。
BEST MODE FOR CARRYING OUT THE INVENTION The vacuum carburizing method for steel materials according to the present invention can be carried out in any form such as a batch type vacuum carburizing furnace or a continuous type vacuum carburizing furnace. Here, the batch type two-chamber type shown in FIG. A case where a vacuum carburizing furnace is used and acetylene gas is used as the carburizing gas in the early carburizing period and 13A city gas is used as the carburizing gas in the latter stage of the carburizing period will be described as an example.

【0013】図示の二室型真空浸炭炉は、装入兼抽出室
1と加熱室9とからなり、前記装入兼抽出室1は、ガス
供給ライン2a及びバルブ3aを介して窒素供給源4に
接続される一方、第一排気系ライン5及び第一排気弁6
を介して真空排気系及び排ガス処理系に接続されてい
る。また、前記装入兼抽出室1の一端側には装入兼抽出
ドア7が配設され、その他端側には中間ドア8を介在さ
せて加熱室9が接続されている。前記加熱室9は、ガス
供給ライン2bからバルブ3b、3c、3d及び、ガス
供給ライン2、2c、2dを介して窒素供給源4、アセ
チレンガス供給源10及び13A都市ガス供給源11
に、また、第二排気系ライン12及び第二排気弁13を
介して真空排気系及び排ガス処理系にそれぞれ接続され
ている。なお、送入兼抽出室1はその内部に油焼入槽を
備え、また、前記加熱室9には加熱手段が配設されると
共に、前記装入兼抽出室1と同様に被処理材を移行させ
る移送手段が配設されているが、これらは公知のものと
同じ構成であるので省略する。
The illustrated two-chamber type vacuum carburizing furnace comprises a charging / extracting chamber 1 and a heating chamber 9. The charging / extracting chamber 1 has a nitrogen supply source 4 through a gas supply line 2a and a valve 3a. While being connected to the first exhaust system line 5 and the first exhaust valve 6
Is connected to the vacuum exhaust system and the exhaust gas treatment system via. A charging / extracting door 7 is arranged at one end of the charging / extracting chamber 1, and a heating chamber 9 is connected to the other end thereof with an intermediate door 8 interposed. The heating chamber 9 includes a nitrogen supply source 4, an acetylene gas supply source 10 and a 13A city gas supply source 11 from a gas supply line 2b via valves 3b, 3c, 3d and gas supply lines 2, 2c, 2d.
Further, they are connected to the vacuum exhaust system and the exhaust gas treatment system via the second exhaust system line 12 and the second exhaust valve 13, respectively. It should be noted that the feeding / extracting chamber 1 is provided with an oil quenching tank therein, and the heating chamber 9 is provided with a heating means. A transfer means for transferring is provided, but these are omitted since they have the same structure as known ones.

【0014】前記二室型真空浸炭炉を用いて被処理材で
ある鋼材部品を真空浸炭処理する場合、まず、被処理材
を積載したトレイを装入兼抽出室1に装入し、第一排気
系ライン5及び第二排気系ライン12を介して装入兼抽
出室1及び加熱室9内をそれぞれ真空排気して所定の真
空度(約0.02KPa)にまで減圧した後、装入兼抽出
室1内のトレイに積載された処理材を減圧下の加熱室9
内に位置させる。次いで、窒素供給源4からガス供給ラ
イン2、2bを介して窒素ガスを加熱室9内に導入し、
炉内圧力を所定圧(86.5〜100KPa)まで上昇さ
せ、窒素雰囲気下で炉内温度を浸炭処理温度(870〜
1000℃)に昇温させる。
When vacuum-carburizing a steel material to be treated using the two-chamber type vacuum carburizing furnace, first, a tray loaded with the material to be treated is loaded into the loading / extracting chamber 1, The charging / extracting chamber 1 and the heating chamber 9 are respectively evacuated through the exhaust system line 5 and the second exhaust system line 12 to reduce the pressure to a predetermined vacuum degree (about 0.02 KPa), and then the charging / combining process is also performed. The processing materials loaded on the trays in the extraction chamber 1 are heated under reduced pressure in the heating chamber 9
Located inside. Next, nitrogen gas is introduced into the heating chamber 9 from the nitrogen supply source 4 through the gas supply lines 2 and 2b,
The pressure inside the furnace is raised to a predetermined pressure (86.5 to 100 KPa), and the temperature inside the furnace is set to a carburizing temperature (870 to 870) under a nitrogen atmosphere.
The temperature is raised to 1000 ° C.

【0015】昇温完了後、炉内を前記浸炭温度に所定時
間保持して均熱処理する。この際、均熱処理完了の約2
0分前の時点で加熱室9内を真空排気(約0.02KP
a)して真空下で均熱を行う。均熱完了後、ガス供給ラ
イン2cを介して加熱室9内にアセチレンガスを連続的
に供給し、炉内圧力を1.5KPa〜3.5KPaに維持し
ながら所定時間だけ初期浸炭処理を行い、続いてアセチ
レンガスの供給を停止し、ガス供給ライン2dを介して
加熱室9内に13A都市ガスを連続的に供給し、炉内圧
力を5.0KPa〜8.0KPaに維持しながら所定時間浸
炭処理を行う。その後、13A都市ガスの供給を停止
し、加熱室9内を真空排気(約0.02KPa)した後、
そのままの温度で拡散処理する。この浸炭・拡散処理が
完了すると、加熱室9内及び装入兼抽出室1内に窒素ガ
ス(N2)を所定圧(86.5〜100KPa)まで供給
して窒素雰囲気下で焼入れ温度(約810〜900℃)
に降温保持する。その後、トレイを装入兼抽出室1に移
動させ、油焼入槽内に浸漬させ焼入れを行う。
After the temperature rise is completed, the inside of the furnace is kept at the carburizing temperature for a predetermined time to carry out soaking. At this time, about 2
Evacuation of the heating chamber 9 at 0 minutes before (about 0.02 KP
a) Perform soaking under vacuum. After completion of soaking, acetylene gas is continuously supplied into the heating chamber 9 through the gas supply line 2c, and the initial carburizing treatment is performed for a predetermined time while maintaining the furnace pressure at 1.5 KPa to 3.5 KPa. Then, supply of acetylene gas is stopped, 13A city gas is continuously supplied into the heating chamber 9 through the gas supply line 2d, and carburization is performed for a predetermined time while maintaining the furnace pressure at 5.0 KPa to 8.0 KPa. Perform processing. After that, the supply of the 13A city gas was stopped, and the inside of the heating chamber 9 was evacuated (about 0.02 KPa).
Diffusion treatment is performed at the same temperature. When this carburizing / diffusion treatment is completed, nitrogen gas (N2) is supplied to the heating chamber 9 and the charging / extracting chamber 1 up to a predetermined pressure (86.5 to 100 KPa), and the quenching temperature (about 810 ~ 900 ° C)
Hold the temperature down. Then, the tray is moved to the charging / extracting chamber 1 and immersed in the oil quenching tank for quenching.

【0016】[0016]

【実施例1】S15CK製平板(50mm×500mm×3
mm)80枚と、SCM420製袋穴付丸棒(φ38mm×
70mm)9本を処理材(総面積4.3m2)とし、これら
をトレイ上に積載し、目標有効浸炭深さ0.6mmとし
て、図2に示す下記仕様の二室型真空浸炭炉を用いて図
1に示す真空浸炭ヒートサイクルで真空浸炭焼入れ処理
を行った。 炉型式: 二室型(焼入れ:油) 加熱室容積: 7.8m(有効寸法:1220mm長さ×
760mm巾×710mm高さ) 真空ポンプ: 油回転ポンプ(450m/時) メカニカルブースタ(250m/時)
[Example 1] Flat plate made of S15CK (50 mm x 500 mm x 3
mm) 80 sheets and SCM420 bag-made round bar (φ38 mm x
70 mm) as treatment material (total area 4.3 m 2 ), these are loaded on the tray, the target effective carburizing depth is 0.6 mm, and the two-chamber vacuum carburizing furnace with the following specifications shown in Fig. 2 is used. Vacuum carburizing and quenching treatment was performed by the vacuum carburizing heat cycle shown in FIG. Furnace type: Two-chamber type (quenching: oil) Heating chamber volume: 7.8 m 3 (effective dimension: 1220 mm length x
760mm width x 710mm height) Vacuum pump: Oil rotary pump (450m 3 / hour) Mechanical booster (250m 3 / hour)

【0017】即ち、前記処理材を搭載したトレイを加熱
室9内に配置させた後、86.5〜100KPaの窒素雰
囲気中、加熱室9内温度を浸炭温度930℃にまで昇温
させ、60分間均熱化する。均熱処理完了の約20分前
の時点で0.02KPa(制御値)にまで真空排気し、真
空下で均熱処理を行う。均熱処理完了後、加熱室9内に
浸炭ガスを供給し浸炭温度930℃で25分間浸炭処理
を行うが、浸炭期初期の10分間は、浸炭ガスとしてア
セチレンガスを12L/分で連続供給し、加熱室9内の
圧力を1.5KPa(制御値)に維持しながら浸炭処理を
行い、10分経過後、浸炭ガスの供給を停止し、次い
で、浸炭ガスとして13A都市ガスを55L/分の速度
で供給し、加熱室9内の圧力を6.0KPa(制御値)に
維持しながら引き続き浸炭処理を15分間行う。次い
で、加熱室9内を真空排気して0.02KPa(制御値)
の真空度にした後、同真空度を維持しながら930℃で
42分間拡散処理を行う。拡散処理後、加熱室9内に窒
素ガスを導入して略大気圧のN2雰囲気とし、同雰囲気
中で焼入温度の850℃までに降温させ、同温度で1時
間保持する。拡散処理後、窒素ガスを導入して略大気圧
のN2雰囲気とした装入兼抽出室1内にトレイを移行さ
せて、処理材を120℃の温度の油に入れて油焼入れを
行う。
That is, after the tray on which the treatment material is mounted is placed in the heating chamber 9, the temperature inside the heating chamber 9 is raised to a carburizing temperature of 930 ° C. in a nitrogen atmosphere of 86.5 to 100 KPa, and 60 Heat soak for a minute. Approximately 20 minutes before the completion of soaking, vacuum exhaust is performed to 0.02 KPa (control value), and soaking is performed under vacuum. After completion of soaking, carburizing gas is supplied into the heating chamber 9 to perform carburizing treatment at a carburizing temperature of 930 ° C. for 25 minutes. During the initial carburizing period of 10 minutes, acetylene gas is continuously supplied at 12 L / min as carburizing gas, Carburizing treatment is performed while maintaining the pressure in the heating chamber 9 at 1.5 KPa (control value), and after 10 minutes, supply of carburizing gas is stopped, and then 13A city gas is supplied as carburizing gas at a rate of 55 L / min. And the pressure in the heating chamber 9 is maintained at 6.0 KPa (control value), and the carburizing treatment is continued for 15 minutes. Next, the inside of the heating chamber 9 is evacuated to 0.02 KPa (control value).
After the vacuum degree is set to 1, the diffusion process is performed at 930 ° C. for 42 minutes while maintaining the same vacuum degree. After the diffusion treatment, nitrogen gas is introduced into the heating chamber 9 to create a N2 atmosphere at approximately atmospheric pressure, the temperature is lowered to the quenching temperature of 850 ° C. in the same atmosphere, and the temperature is maintained for 1 hour. After the diffusion treatment, the tray is moved to the inside of the charging / extracting chamber 1 in which nitrogen gas is introduced and the atmosphere is N2 atmosphere, and the treated material is put into oil at a temperature of 120 ° C. for oil quenching.

【0018】得られた処理材の有効浸炭深さは0.55
〜0.60mmで袋穴奥までほぼ均一な浸炭層が形成され
ており、処理材表面に煤の付着やトラップ部への煤の溜
まりは認められず、良好な結果が得られた。
The effective carburized depth of the obtained treated material is 0.55.
A substantially uniform carburized layer was formed up to the inside of the bag hole at a depth of up to 0.60 mm, and soot was not attached to the surface of the treated material and soot was not accumulated in the trap portion, and good results were obtained.

【0019】[0019]

【実施例2】S15CK製平板(50mm×500mm×3
mm)80枚と、SCM420製袋穴付丸棒(φ38mm×
70mm)9本を処理材(総面積4.3m2)とし、これら
をトレイ上に積載し、目標有効浸炭深さ0.9mmとして
下記条件下で実施例1と同様にして真空浸炭焼入れ処理
を行った。なお、本実施例では、浸炭期後期の処理を更
に二段階に分け浸炭ガス供給量を二段階に変えて行っ
た。
[Example 2] Flat plate made of S15CK (50 mm x 500 mm x 3
mm) 80 sheets and SCM420 bag-made round bar (φ38 mm x
70 mm) as treatment material (total area 4.3 m 2 ), these are loaded on a tray, and the target effective carburizing depth is 0.9 mm, and vacuum carburizing and quenching treatment is performed under the following conditions in the same manner as in Example 1. went. In this example, the treatment in the latter stage of the carburizing period was divided into two stages and the carburizing gas supply amount was changed to two stages.

【0020】浸炭処理: 浸炭温度:930℃ 浸炭時間:60分 浸炭ガス: 浸炭期初期:アセチレンガス 浸炭期後期:13A都市ガス ガス供給量: 浸炭期初期: 12L/分 ×10分 浸炭期後期A: 55L/分 ×15分 浸炭期後期B: 40L/分 ×35分 加熱室9内圧力: 浸炭期初期: 1.5KPa(制御値) 浸炭期後期A: 6.5KPa(制御値) 浸炭期後期B: 6.5KPa(制御値) 拡散処理: 拡散温度: 930℃ 拡散時間: 150分間 加熱室圧力: 0.02KPa(制御値) 焼入れ処理: 焼入れ温度:840℃ 焼入れ液: 油(温度:120℃) 得られた処理材の有効浸炭深さは0.85〜0.93mmで
袋穴奥までほぼ均一な浸炭層が形成されており、処理材
表面に煤の付着やトラップ部への煤の溜まりは認められ
ず、良好な結果が得られた。
Carburizing treatment: Carburizing temperature: 930 ° C. Carburizing time: 60 minutes Carburizing gas: Early carburizing period: Acetylene gas late carburizing period: 13A City gas gas supply: Early carburizing period: 12 L / min x 10 minutes Carburizing period late A: 55 L / min x 15 min late carburizing period B: 40 L / min x 35 min Pressure inside heating chamber 9: early carburizing period: 1.5 KPa (control value) late carburizing period A: 6.5 KPa (control value) late carburizing period B : 6.5KPa (control value) Diffusion treatment: Diffusion temperature: 930 ° C Diffusion time: 150 minutes Heating chamber pressure: 0.02KPa (control value) Quenching treatment: Quenching temperature: 840 ° C Quenching liquid: Oil (temperature: 120 ° C) The obtained carburized material has an effective carburizing depth of 0.85 to 0.93 mm and a carburized layer is formed almost evenly up to the inside of the bag hole. Soot does not adhere to the surface of the treated material or soot is trapped in the trap part. No good results were obtained It was.

【0021】[0021]

【実施例3】SCM420製ハイポイトギヤを処理材と
し、これをトレイ上に30個積載(全表面積:4m2
し、目標有効浸炭深さ0.8mmとして下記条件下で実施
例1と同様にして真空浸炭焼入れ処理を行った。
[Embodiment 3] A hypothetical gear made of SCM420 was used as a treating material, and 30 pieces of this were loaded on the tray (total surface area: 4 m 2 ).
Then, vacuum carburizing and quenching treatment was carried out in the same manner as in Example 1 under the following conditions with a target effective carburizing depth of 0.8 mm.

【0022】浸炭処理: 浸炭温度:950℃ 浸炭時間:22分 浸炭ガス: 浸炭期初期:アセチレンガス 浸炭期後期:13A都市ガス ガス供給量: 浸炭期初期: 12L/分 ×10分 浸炭期後期: 50L/分 ×22分 加熱室内圧力: 浸炭期初期: 1.5KPa(制御値) 浸炭期後期: 6.5KPa(制御値) 拡散処理: 拡散温度: 950℃ 拡散時間: 92分間 加熱室圧力: 0.02KPa(制御値) 焼入れ処理: 焼入れ温度:850℃ 焼入れ液: 油(温度:100℃) 得られた処理材の有効浸炭深さは0.76〜0.84mmで
均一な浸炭層が形成されており、処理材表面に煤の付着
やトラップ部への煤の溜まりは認められず、良好な結果
が得られた。
Carburizing treatment: Carburizing temperature: 950 ° C Carburizing time: 22 minutes Carburizing gas: Early carburizing period: Acetylene gas late carburizing period: 13A City gas supply: Carburizing period early: 12L / min × 10 minutes Carburizing period late: 50L / Min × 22 minutes Heating chamber pressure: Early carburizing period: 1.5 KPa (control value) Late carburizing period: 6.5 KPa (control value) Diffusion treatment: Diffusion temperature: 950 ° C Diffusion time: 92 minutes Heating chamber pressure: 0.1 02KPa (Control value) Quenching treatment: Quenching temperature: 850 ° C Quenching liquid: Oil (Temperature: 100 ° C) The obtained treated material has an effective carburizing depth of 0.76 to 0.84 mm and a uniform carburized layer is formed. Therefore, no soot was attached to the surface of the treated material and soot was not accumulated in the trap portion, and good results were obtained.

【0023】[0023]

【発明の効果】以上の説明から明らかなように、本発明
は、初期の浸炭期は、不飽和炭化水素系ガス(例えば、
アセチレンガス)で、後期の浸炭期は飽和炭化水素系ガ
ス(例えば、13A都市ガス)で浸炭処理を行うため、
処理材表面に煤が付着することを回避して、均一な浸炭
層を形成することができ、しかも、アセチレンガス等の
高価な不飽和炭化水素系ガスの消費量を低減でき、真空
排気装置の小型化をも図ることができる。
As is apparent from the above description, the present invention is characterized in that during the initial carburizing period, unsaturated hydrocarbon gas (for example,
Acetylene gas), in the latter carburizing period, the carburizing process is performed with saturated hydrocarbon gas (for example, 13A city gas).
Soot can be prevented from adhering to the surface of the treated material and a uniform carburized layer can be formed. Furthermore, the consumption of expensive unsaturated hydrocarbon-based gas such as acetylene gas can be reduced and It can also be downsized.

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

【図1】 本発明方法における真空浸炭ヒートサイクル
の一例を示す図
FIG. 1 is a diagram showing an example of a vacuum carburizing heat cycle in the method of the present invention.

【図2】 本発明に使用する真空浸炭炉のブロック図FIG. 2 is a block diagram of a vacuum carburizing furnace used in the present invention.

【図3】 浸炭時間と鋼材中の炭素濃度プロファイルを
示すグラフ
FIG. 3 is a graph showing carburizing time and carbon concentration profile in steel

【符号の説明】[Explanation of symbols]

1…装入兼抽出室 2…ガス供給ライン 3…バルブ 4…窒素供給源 5…第一排気系ライン 6…第一排気弁 7…装入ドア 8…中間ドア 9…加熱室 10…アセチレンガス供給源 11…都市ガス供給源 12…第二排気系ライン 13…第二排気弁 1 ... Charge and extraction room 2 ... Gas supply line 3 ... Valve 4 ... Nitrogen supply source 5 ... First exhaust system line 6 ... First exhaust valve 7 ... Charging door 8 ... Middle door 9 ... Heating room 10 ... Acetylene gas supply source 11 ... City gas supply source 12 ... Second exhaust system line 13 ... Second exhaust valve

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 鋼材部品を減圧下で浸炭処理する真空浸
炭方法において、浸炭期に第一所定減圧下の不飽和炭化
水素系ガス下に引続き、第二所定減圧下の飽和炭化水素
系ガス下で浸炭処理することを特徴とする鋼材部品の真
空浸炭方法。
1. A vacuum carburizing method for carburizing steel parts under reduced pressure, wherein during a carburizing period, a first predetermined reduced pressure of an unsaturated hydrocarbon-based gas is continuously followed by a second predetermined reduced pressure of a saturated hydrocarbon-based gas. A method for vacuum carburizing steel parts, characterized in that
【請求項2】 1.5〜3.5KPaのアセチレンガス下
に引続き、5.0〜8.0KPaの13A都市ガス下で浸
炭処理を行うことを特徴とする請求項1記載の鋼材部品
の真空浸炭方法。
2. The vacuum of a steel part according to claim 1, wherein the carburizing treatment is performed under an acetylene gas of 1.5 to 3.5 KPa and subsequently under a 13A city gas of 5.0 to 8.0 KPa. Carburizing method.
JP2001313884A 2001-10-11 2001-10-11 Method for vacuum carburizing steel part Pending JP2003119558A (en)

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Publication Number Publication Date
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Family

ID=19132288

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Country Link
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005206895A (en) * 2004-01-23 2005-08-04 Koyo Thermo System Kk Vacuum carburizing furnace
KR100901572B1 (en) 2007-08-20 2009-06-08 현대자동차주식회사 Heat treatment method for annular gear
US9212416B2 (en) 2009-08-07 2015-12-15 Swagelok Company Low temperature carburization under soft vacuum
JP2016148091A (en) * 2015-02-13 2016-08-18 ジヤトコ株式会社 Vacuum carburization method and vacuum carburization device
US9617632B2 (en) 2012-01-20 2017-04-11 Swagelok Company Concurrent flow of activating gas in low temperature carburization

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005206895A (en) * 2004-01-23 2005-08-04 Koyo Thermo System Kk Vacuum carburizing furnace
JP4539904B2 (en) * 2004-01-23 2010-09-08 光洋サーモシステム株式会社 Vacuum carburizing furnace
KR100901572B1 (en) 2007-08-20 2009-06-08 현대자동차주식회사 Heat treatment method for annular gear
US9212416B2 (en) 2009-08-07 2015-12-15 Swagelok Company Low temperature carburization under soft vacuum
US10156006B2 (en) 2009-08-07 2018-12-18 Swagelok Company Low temperature carburization under soft vacuum
US10934611B2 (en) 2009-08-07 2021-03-02 Swagelok Company Low temperature carburization under soft vacuum
US9617632B2 (en) 2012-01-20 2017-04-11 Swagelok Company Concurrent flow of activating gas in low temperature carburization
US10246766B2 (en) 2012-01-20 2019-04-02 Swagelok Company Concurrent flow of activating gas in low temperature carburization
US11035032B2 (en) 2012-01-20 2021-06-15 Swagelok Company Concurrent flow of activating gas in low temperature carburization
JP2016148091A (en) * 2015-02-13 2016-08-18 ジヤトコ株式会社 Vacuum carburization method and vacuum carburization device

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