JPH08325701A - Vacuum carburization method and device and carburized product - Google Patents

Vacuum carburization method and device and carburized product

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Publication number
JPH08325701A
JPH08325701A JP6793796A JP6793796A JPH08325701A JP H08325701 A JPH08325701 A JP H08325701A JP 6793796 A JP6793796 A JP 6793796A JP 6793796 A JP6793796 A JP 6793796A JP H08325701 A JPH08325701 A JP H08325701A
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JP
Japan
Prior art keywords
carburizing
gas
vacuum
heating chamber
depth
Prior art date
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Application number
JP6793796A
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Japanese (ja)
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JP2963869B2 (en
Inventor
Takeshi Kubota
健 久保田
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NIPPON HEIZU KK
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NIPPON HEIZU KK
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Abstract

PURPOSE: To make it possible to uniformly carburize each part of a work including the inside wall surfaces of a deep recessed part and to save the amt. of gas and heat quantity to be used by suppressing the generation of soot in a vacuum carburization method. CONSTITUTION: The work M is vacuum heated in a heating chamber 2 of a vacuum carburization furnace 1 and gaseous acetylene is supplied from a carburizing gas source C into the heating chamber 1. The work is subjected to a carburization treatment by maintaining a vacuum state of <=1Pa in the heating chamber 2 by a vacuum evacuation source V.

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、真空浸炭方法およ
びこの方法の実施に用いられる浸炭装置ならびに上記方
法で浸炭処理された鋼材製品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, a carburizing apparatus used for carrying out this method, and a steel product carburized by the above method.

【0002】[0002]

【従来の技術】鉄鋼の表面改質方法として最も広く利用
されている浸炭処理においては、ガス雰囲気を使用した
ガス浸炭が一般的であるが、ガス浸炭は、表面異常層の
発生、高温浸炭への炉構造の不備、高濃度浸炭での煤発
生、浸炭条件の管理項目の多さと繁雑さ等の問題点があ
り、これら問題点を克服するために開発されたのが真空
浸炭炉を用いる真空浸炭方法である。
2. Description of the Related Art In the most widely used carburizing method for surface modification of steel, gas carburizing is generally used in a gas atmosphere. However, gas carburizing involves generation of an abnormal surface layer and high temperature carburizing. There are problems such as incomplete furnace structure, generation of soot in high-concentration carburization, large number of management items of carburizing conditions and complexity, etc.Vacuum carburizing furnace was developed to overcome these problems. It is a carburizing method.

【0003】従来の真空浸炭方法では、浸炭用ガスとし
て、ガス状の鎖式飽和炭化水素が使用されていた。すな
わち、ガス状の鎖式飽和炭化水素は、メタン系ガスであ
り、メタンガス(CH4 )、プロパンガス(C
3 8 )、ブタンガス(C4 10)等が使用されてお
り、これら浸炭用ガスを、900〜1000℃程度に鋼
材よりなるワークを加熱して配した真空浸炭炉の加熱室
内に直接供給して、加熱室内で熱分解させ、その際に発
生する活性炭素を鋼材の表面に侵入させ、その表面から
浸炭・拡散させるようにしていた。
In the conventional vacuum carburizing method, a gaseous chain saturated hydrocarbon is used as a carburizing gas. That is, the gaseous chain saturated hydrocarbon is a methane-based gas, and includes methane gas (CH 4 ) and propane gas (C
3 H 8 ), butane gas (C 4 H 10 ), etc. are used, and these carburizing gases are directly supplied to the heating chamber of a vacuum carburizing furnace in which a work made of steel is heated to about 900 to 1000 ° C. Then, thermal decomposition is carried out in the heating chamber, and activated carbon generated at that time is made to enter the surface of the steel material, and is carburized and diffused from the surface.

【0004】この場合、ワークの全面に十分に浸炭用ガ
スが行き渡る必要があるため、ワークを収容した加熱室
を真空状態にしておき、上記浸炭用ガスを加熱室内に供
給するとともに、撹拌もしくはパルス投入による炉圧変
動により、ワークの表面への浸炭用ガスの充分な供給を
図っていた。
In this case, since the carburizing gas needs to be sufficiently spread over the entire surface of the work, the heating chamber containing the work is kept in a vacuum state, and the carburizing gas is supplied into the heating chamber while stirring or pulsing. Due to fluctuations in the furnace pressure caused by charging, the carburizing gas was sufficiently supplied to the surface of the work.

【0005】ところで、従来の真空浸炭方法において
は、一般的に浸炭性が強いとして、炭化水素を浸炭用ガ
スとして使用する認識があり、この炭化水素の中でも、
上述のようなメタン系ガスのようなガス状の鎖式飽和炭
化水素が使用されていた。
By the way, in the conventional vacuum carburizing method, it is generally recognized that the carburizing property is strong and hydrocarbon is used as the carburizing gas.
Gaseous chain saturated hydrocarbons such as the methane-based gases mentioned above have been used.

【0006】その理由は、当業者間では、メタン系ガス
は、鋼材を浸炭させる1100℃程度までの温度範囲で
は安定であるが、分子量が増すと安定性が減少し、煤の
発生があるものの、浸炭力が強くなると認識され、一
方、アセチレン系ガスのようなガス状の鎖式不飽和炭化
水素は、メタン系ガスよりも不安定であり、浸炭反応よ
りも熱分解が盛んに行なわれるから、浸炭用ガスに使用
しても単に煤を発生させるだけであって、浸炭用ガスに
は全く適さないと認識されていたからである(河上 護
著「金属表面硬化熱処理技術」槇書店昭和46年10月
25日発行第139頁参照)。
The reason is that among those skilled in the art, methane-based gas is stable in the temperature range up to about 1100 ° C. for carburizing steel, but the stability decreases as the molecular weight increases, and soot is generated. It is recognized that the carburizing power becomes stronger, while gaseous chain unsaturated hydrocarbons such as acetylene-based gas are more unstable than methane-based gas and thermal decomposition is more active than carburization reaction. However, it was recognized that even if used as a carburizing gas, it would only generate soot and was not suitable as a carburizing gas at all (Mamoru Kawakami "Metal Surface Hardening Heat Treatment Technology" Maki Shoten 1969 10 See page 139, issued 25th of May).

【0007】そのため、実際には、真空浸炭での浸炭用
ガスとしては、ガス状の鎖式飽和炭化水素であるメタン
系ガスの、メタンガス(CH4 )、プロパンガス(C3
8)、ブタンガス(C4 10)等しか使用されず、ガ
ス状の鎖式不飽和炭化水素であるアセチレン系ガスは見
向きもされなかった。
Therefore, in practice, as a carburizing gas in vacuum carburization, methane gas (CH 4 ) and propane gas (C 3 ) which are methane series gases which are gaseous chain saturated hydrocarbons are used.
H 8 ), butane gas (C 4 H 10 ), etc. were only used, and no acetylene-based gas, which is a gaseous chain unsaturated hydrocarbon, was observed.

【0008】[0008]

【発明が解決しようとする課題】しかしながら、従来の
真空浸炭方法によれば、ガス浸炭での品質上での問題点
は解決されたものの、依然として下記のような問題点を
抱えている。
However, although the conventional vacuum carburizing method has solved the problem of quality in gas carburizing, it still has the following problems.

【0009】すなわち、 1.煤の発生が多く、メンテナンス作業が繁雑で汚い、 2.炉の加熱室内へのワークの挿入量を減らしてガス量
を増さないと均一浸炭が困難である、 3.ワークの小径の深い孔や狭い隙間への浸炭が不充分
である、 4.設備費が高く、特殊用途への使用に限定される、 5.ガス浸炭に比べて生産性が低く、処理コストが高
い、等である。
That is, 1. Soot is often generated, and maintenance work is complicated and dirty. 2. It is difficult to perform uniform carburization unless the amount of gas inserted into the heating chamber of the furnace is reduced and the amount of gas is increased. 3. Insufficient carburization into small diameter deep holes or narrow gaps in the work. 4. Equipment costs are high and limited to special purposes. It has lower productivity and higher treatment cost than gas carburizing.

【0010】下式は従来用いられている浸炭用ガスの熱
分解のメカニズムを示すものである。
The following equation shows the mechanism of thermal decomposition of the conventionally used carburizing gas.

【0011】[0011]

【数1】 [Equation 1]

【0012】上式において〔C〕は浸炭に寄与する活性
炭素である。ただし、ワークの表面以外の炉内空間で分
解した活性炭素はそのまま煤になり、これが真空浸炭に
おける煤の発生の原因となっている。
In the above formula, [C] is activated carbon that contributes to carburization. However, the activated carbon decomposed in the furnace space other than the surface of the work becomes soot as it is, which causes soot generation in vacuum carburization.

【0013】この煤の発生量をより少なくする方策とし
ては、 a.炉内での浸炭用ガスの量をできるだけ稀薄にするた
めに、供給ガスを不活性ガスで希釈して(ガス圧は従来
通り)使用する、 b.異常層が発生しない程度に浸炭用ガスに酸素源(例
えばアルコール)を混入して、活性炭素の一部をCOと
して浸炭に利用するとともに、残余のCOガスを炉外に
排出する、 c.煤対策以外の効果もあるが、ワーク表面付近にプラ
ズマを発生させて、稀薄浸炭ガスをイオン化してワーク
表面に引き付けて有効に浸炭に利用し、他の炉空間での
分解発生煤を少なくする(プラズマ浸炭)、等がある。
Measures for reducing the amount of soot generated include: a. To dilute the amount of carburizing gas in the furnace as much as possible, use the feed gas diluted with an inert gas (gas pressure is conventional), b. An oxygen source (for example, alcohol) is mixed into the carburizing gas to such an extent that an abnormal layer is not generated, and a part of the activated carbon is used as CO for carburizing, and the residual CO gas is discharged to the outside of the furnace. C. Although it has effects other than soot countermeasures, it generates plasma in the vicinity of the work surface, ionizes the dilute carburizing gas and attracts it to the work surface, effectively uses it for carburization, and reduces decomposition and soot in other furnace spaces. (Plasma carburization), etc.

【0014】これらの対策によれば、いずれも煤の発生
量を低減することができるが、そのために、設備費や処
理コストが上昇したり、本来の真空浸炭のメリットが損
なわれたりする問題がある。
According to these measures, the amount of soot generated can be reduced in any case, but this causes a problem that the equipment cost and the processing cost increase and the original merit of vacuum carburization is impaired. is there.

【0015】また、従来のメタン系ガスを浸炭用ガスと
して使用する真空浸炭では、積載ワークの間隔が不充分
であったり、ワークに小径の深い孔や狭い隙間がある場
合には、ワーク全体に亘って均一に浸炭しようとして
も、孔の深い内部や狭い隙間ハ勿論、隣接ワークが近す
ぎる場合においては充分な浸炭深さが得られず、浸炭深
さのバラツキが避けられなかった。例えば、炉内の加熱
室にガス循環装置、ガス撹拌装置、ガス高速噴射装置等
を設置して浸炭処理を行なっても、ワークに内径4mmで
深さ28mmの孔があけられている場合、ワーク外周面で
の有効浸炭深さが0.51mm程度であるのに対し、孔の
底部の有効浸炭深さは0.30mm程度となっていた。
Further, in the conventional vacuum carburization using the methane-based gas as the carburizing gas, when the intervals between the loaded works are insufficient, or when the works have deep holes with a small diameter or narrow gaps, the entire work is Even if it is attempted to uniformly carburize over a wide range, it is impossible to obtain a sufficient carburizing depth when the adjacent workpieces are too close to each other, as well as in a deep hole or a narrow gap c, and variations in carburizing depth cannot be avoided. For example, even if a gas circulating device, a gas stirring device, a gas high-speed injection device, etc. are installed in the heating chamber in the furnace for carburizing, if the workpiece has a hole with an inner diameter of 4 mm and a depth of 28 mm, While the effective carburizing depth on the outer peripheral surface was about 0.51 mm, the effective carburizing depth at the bottom of the hole was about 0.30 mm.

【0016】このような浸炭深さのバラツキは、使用す
る浸炭用ガスが、炭素原子数に比べて水素原子の数が多
く、加熱室内で原子状炭素を発生させるように分解する
と、分解生成ガスとしての水素ガス等の分子数が多くな
って、浸炭用ガスの分子の平均自由行程(mean free pa
th)をより小さくするためと推定される。
Such variations in carburizing depth are caused by decomposition gas produced when the carburizing gas used has a large number of hydrogen atoms compared to the number of carbon atoms and is decomposed to generate atomic carbon in the heating chamber. As the number of molecules of hydrogen gas, etc., increases, the mean free path (mean free pa
It is estimated that th) is made smaller.

【0017】そして、小径の孔の内壁面も所定の浸炭深
さを確保できるように浸炭処理を行なうためには、孔の
中に炭素を供給したり、必要以上に浸炭用ガスを供給
し、かつそのガスを流動撹拌させたりして浸炭処理を行
なうこととなって、煤の発生量が増大する結果を招いて
いた。
In order to carry out the carburizing treatment so that the inner wall surface of the small-diameter hole can also secure a predetermined carburizing depth, carbon is supplied into the hole or a carburizing gas is supplied more than necessary. In addition, the gas is fluidized and agitated to carry out the carburizing treatment, resulting in an increase in the amount of soot generated.

【0018】本発明は、上述のような問題に鑑み、煤の
発生を抑えて、深い凹部の内壁面を含めてワーク全体に
亘って各部を均一に浸炭することできるとともに、使用
するガス量や熱量も少なくて済む真空浸炭方法および装
置ならびに浸炭処理された鋼材製品を提供することを目
的とする。
In view of the above-mentioned problems, the present invention can suppress the generation of soot, uniformly carburize each portion including the inner wall surface of the deep recessed portion over the entire work, and the amount of gas used and An object of the present invention is to provide a vacuum carburizing method and apparatus that require a small amount of heat and a carburized steel product.

【0019】[0019]

【課題を解決するための手段】本発明による真空浸炭方
法は、鋼材よりなるワークを、真空浸炭炉の加熱室内で
真空加熱するとともに、この加熱室内に浸炭用ガスを供
給して浸炭処理を行なう方法であって、浸炭用ガスとし
てガス状の鎖式不飽和炭化水素を使用するとともに、加
熱室内を1kPa 以下の真空状態として浸炭処理を行なう
ことを特徴とするものである。
In the vacuum carburizing method according to the present invention, a work made of steel is vacuum-heated in a heating chamber of a vacuum carburizing furnace, and a carburizing gas is supplied into the heating chamber for carburizing treatment. The method is characterized in that a gaseous chain unsaturated hydrocarbon is used as a carburizing gas, and a carburizing process is performed in a heating chamber in a vacuum state of 1 kPa or less.

【0020】上記ガス状の鎖式不飽和炭化水素として
は、アセチレン系ガス、特にアセチレンガスを使用する
ことが望ましい。
As the above-mentioned gaseous chain unsaturated hydrocarbon, it is desirable to use acetylene gas, especially acetylene gas.

【0021】さらに本発明による真空浸炭方法は、浸炭
処理のみでなく、鋼材の表面に炭素(C)と同時に窒素
(N)を浸入させる浸炭窒化処理にも適用することがで
きる。その場合は、浸炭用ガスとしてのアセチレンガス
に加えて、ガス状の窒素源として例えばアンモニアガス
(NH3 )を添加すればよい。
Further, the vacuum carburizing method according to the present invention can be applied not only to the carburizing treatment but also to the carbonitriding treatment in which nitrogen (N) is infiltrated into the surface of the steel at the same time as carbon (C). In that case, for example, ammonia gas (NH 3 ) may be added as a gaseous nitrogen source in addition to acetylene gas as a carburizing gas.

【0022】また、本発明による真空浸炭装置は、鋼材
よりなるワークを加熱する加熱室を備えた真空浸炭炉
と、上記加熱室内にアセチレン系ガスを供給する浸炭用
ガス源と、加熱室内を真空排気する真空排気源とを備
え、1kPa 以下の真空状態で真空浸炭を行なうことを特
徴とするものである。
Further, the vacuum carburizing apparatus according to the present invention comprises a vacuum carburizing furnace equipped with a heating chamber for heating a work made of steel, a carburizing gas source for supplying acetylene-based gas into the heating chamber, and a vacuum for the heating chamber. It is characterized in that it is provided with a vacuum exhaust source for exhausting, and performs vacuum carburization in a vacuum state of 1 kPa or less.

【0023】さらに、本発明による浸炭処理された鋼材
製品は、内径をDとする閉端孔を備え、この閉端孔の内
壁面における浸炭深さのほぼ等しい領域が、該閉端孔の
開口端から深さLの範囲に亘って形成されているもので
あって、上前記深さLの値が、L/D比で12乃至50
の範囲内にあることを特徴とするものである。
Further, the carburized steel product according to the present invention is provided with a closed end hole having an inner diameter D, and the region of the inner wall surface of the closed end hole having substantially the same carburizing depth is the opening of the closed end hole. It is formed over the range of the depth L from the end, and the value of the depth L is 12 to 50 in terms of L / D ratio.
It is characterized by being within the range of.

【0024】煤のない真空浸炭(減圧ガス浸炭)を実現
するためには、浸炭に直接寄与する炭素以外は炉中で分
解させないようにすることが望ましいから、炉内に供給
する炭素源には、できるだけワークの表面だけで分解ま
たは反応し、他の炉材や炉空間では分解または反応しな
いものが望ましい。
In order to realize soot-free vacuum carburization (pressure-reduced gas carburization), it is desirable that only carbon that directly contributes to carburization is decomposed in the furnace. It is desirable that the material decomposes or reacts only on the surface of the work as much as possible and does not decompose or react on other furnace materials or furnace spaces.

【0025】この条件からみて、従来の真空浸炭方法に
おいて浸炭用ガスとして使用されていた安定なメタン系
ガスよりも化学的には不安定で活性なガスのほうが浸炭
用ガスとして望ましい。
In view of this condition, a chemically unstable and active gas is more preferable as the carburizing gas than the stable methane-based gas used as the carburizing gas in the conventional vacuum carburizing method.

【0026】そこで、本発明による真空浸炭方法では、
鋼材を浸炭処理する1100℃程度までの温度範囲では
メタンガス、プロパンガス等の鎖式飽和炭化水素ガスよ
りも化学的に活性で、反応および分解し易い鎖式不飽和
炭化水素ガスを浸炭用ガスとして使用する。
Therefore, in the vacuum carburizing method according to the present invention,
Chain unsaturated hydrocarbon gas, which is more chemically active than the chain saturated hydrocarbon gas such as methane gas and propane gas, and which is easy to react and decompose, is used as the carburizing gas in the temperature range up to about 1100 ° C where the steel material is carburized. use.

【0027】ただし、これらの不安定なガスは、炉中の
滞在時間が限界を超えると、従来から使用されている飽
和炭化水素ガスよりも容易に熱分解して煤を発生するの
で、炉内の滞在時間を厳密に制限し、ワーク表面で反応
分解するには充分であるが熱分解するには不充分な時間
の範囲で炉外に排出する必要がある。
However, when the residence time in the furnace exceeds the limit, these unstable gases are more easily thermally decomposed than the conventionally used saturated hydrocarbon gas to generate soot. It is necessary to discharge the gas from the furnace within a time range that is sufficient for reactive decomposition on the surface of the work but insufficient for thermal decomposition, by strictly limiting the residence time.

【0028】そのため、本発明による真空浸炭方法で
は、浸炭用ガスの炉内滞在時間を短くするために、炉内
圧力を従来の真空浸炭方法よりも極端に低い1kPa以
下として、ワークの表面での分解反応は起きるが、炉内
空間では殆ど煤を発生しない真空浸炭方法を実現してい
る。
Therefore, in the vacuum carburizing method according to the present invention, in order to shorten the residence time of the carburizing gas in the furnace, the furnace pressure is set to 1 kPa or less, which is extremely lower than that in the conventional vacuum carburizing method, and the surface of the work is reduced. Although a decomposition reaction occurs, a vacuum carburizing method has been realized which hardly generates soot in the furnace space.

【0029】また、従来の真空浸炭方法では、ワークの
表面で分解して炭素の供給を終了した複生ガスを速やか
に移動させて新しい供給ガスを均一に分布させるため
に、ガス圧力をある程度高く(15〜70kPa )して、
炉内をファン等で撹拌するか、またはガス投入をパルス
方式として複生ガスを減圧によって少なくし、パルス投
入で新しい高い圧力のガスを供給して、ワーク表面の供
給炭素量を確保している。当然ながら、このことがま
た、浸炭に必要な量よりもはるかに多量の浸炭用ガスを
供給することとなって、煤の発生をより助長することに
なっている。
Further, in the conventional vacuum carburizing method, the gas pressure is raised to a certain degree in order to quickly move the compound gas decomposed on the surface of the work and finished supplying carbon to uniformly distribute the new supply gas ( 15 ~ 70kPa)
The amount of carbon supplied to the surface of the work is secured by stirring the inside of the furnace with a fan or the like, or by using a pulse system for gas injection to reduce the amount of compound gas by decompressing and supplying a new high pressure gas by pulse injection. Of course, this would also provide a much larger amount of carburizing gas than is needed for carburizing, further promoting the generation of soot.

【0030】[0030]

【発明の効果】これに対して、本発明による真空浸炭方
法では、ガス状の鎖式不飽和炭化水素を浸炭用ガスとし
て使用するものであり、このガス状の鎖式不飽和炭化水
素であるエチレンガス(C2 4 )やアセチレンガス
(C2 2 )は、従来使用されていたメタン系ガスと相
違し、炭素原子数に比べて水素原子の数が少ない。
On the other hand, in the vacuum carburizing method according to the present invention, a gaseous chain unsaturated hydrocarbon is used as a carburizing gas, and this gaseous chain unsaturated hydrocarbon is used. The ethylene gas (C 2 H 4 ) and the acetylene gas (C 2 H 2 ) have a smaller number of hydrogen atoms than the number of carbon atoms, unlike the conventionally used methane-based gas.

【0031】そのため、加熱室内で浸炭用ガスが原子状
炭素を発生させるように分解しても、分解生成ガスであ
る水素ガス等の分子数が多くならないため、浸炭ガス分
子としてワークに接触しようとする際の水素ガス分子等
の妨害を少なくすることができる。その結果、浸炭処理
時の圧力が低いこともあり、浸炭ガス分子の平均自由行
程(mean free path)が伸び、ワークの深い凹部の内壁
周面にも、浸炭ガス分子が侵入し易くなり、さらに浸炭
ガス分子が化学的に活性で、高温にしなくても、また時
間をかけなくても分解し易い不飽和炭化水素であるた
め、ワーク表面で短時間で容易に反応、分解して原子状
炭素をワーク表面に供給できることと相俟って、ワーク
の各部を均一に浸炭することができることとなる。
Therefore, even if the carburizing gas is decomposed so as to generate atomic carbon in the heating chamber, the number of molecules of hydrogen gas, which is a decomposition product gas, does not increase, so that it is attempted to come into contact with the work as carburizing gas molecules. It is possible to reduce the interference of hydrogen gas molecules and the like during the operation. As a result, the pressure during the carburizing process may be low, the mean free path of the carburizing gas molecules may be extended, and the carburizing gas molecules may easily enter the inner peripheral surface of the deep recess of the work. Since the carburizing gas molecule is an unsaturated hydrocarbon that is chemically active and easily decomposes even at high temperature and without taking time, it easily reacts and decomposes on the surface of the work in a short time to form atomic carbon. In addition to being able to supply to the work surface, each part of the work can be uniformly carburized.

【0032】そして、この浸炭の均一性は炉内圧力を低
くするほど顕著になる。ちなみに、内径をDとする閉端
孔を備えたワークに対して浸炭処理を行なって、この閉
端孔の内壁面における全浸炭深さのほぼ等しい領域が、
この閉端孔の開口端から深さLの範囲に亘って形成され
たとするとき、炉内圧力を0.02kPa として浸炭処理
を行なった場合、上記深さLの値がL/D比で36にま
で達した。さらに炉内圧力を低くすれば、全浸炭深さの
ほぼ等しい領域の深さLの値を、L/D比で50程度に
まですることができる。このような値は、従来のガス浸
炭では勿論、真空浸炭あるいはプラズマ浸炭でも達成不
可能である。
The uniformity of carburization becomes remarkable as the furnace pressure is lowered. By the way, when a carburizing process is performed on a work having a closed end hole having an inner diameter D, a region where the total carburizing depth is almost equal on the inner wall surface of the closed end hole,
When it is assumed that the closed end hole is formed over the range of the depth L from the open end, when the carburizing process is performed with the furnace pressure of 0.02 kPa, the value of the depth L is 36 in L / D ratio. Reached Further, if the pressure in the furnace is lowered, the value of the depth L in the region where the total carburizing depth is substantially equal can be increased to about 50 in L / D ratio. Such a value cannot be achieved by vacuum carburization or plasma carburization as well as conventional gas carburization.

【0033】また、本発明では、加熱室内を従来の真空
浸炭に比べて極端に低圧の1kPa 以下で浸炭処理を行な
っているため、加熱室内に供給されてから低圧に維持す
るための吸引手段で吸引されるまでの時間、すなわち、
浸炭用ガスの加熱室内での滞留時間が短くなる。滞留時
間が短くなれば、分解浸炭に至らなかった浸炭用ガス
を、加熱室内で分解して煤を発生させる以前に、加熱室
内から除去することが可能になり、加熱室内での煤の発
生を防止することができる。
Further, in the present invention, since the carburizing process in the heating chamber is carried out at an extremely low pressure of 1 kPa or less as compared with the conventional vacuum carburization, the suction means for maintaining the low pressure after being supplied into the heating chamber. Time to be inhaled, ie
The residence time of the carburizing gas in the heating chamber becomes shorter. If the residence time is shortened, it becomes possible to remove the carburizing gas that has not been decomposed and carburized from the heating chamber before it is decomposed in the heating chamber to generate soot. Can be prevented.

【0034】そのため、不安定で分解し易いガス状の不
飽和炭化水素を浸炭用ガスとして使用しても、短い時間
で必要量の浸炭用ガスをワーク表面に対して接触分解さ
せて浸炭することができて、浸炭に支障を生じず、か
つ、未分解の、煤を発生し易い浸炭用ガスを分解後の生
成ガス(水素ガス等)とともに直ちに加熱室外に排出で
きることから、煤の発生を防止してワークの浸炭処理を
行なうことが可能になった。また、分解生成ガスも短時
間で加熱室外に排出できることから、一層、浸炭用ガス
分子の平均自由行程を伸ばすことにも寄与できて、ワー
クの各部の均一浸炭に貢献できることになる。
Therefore, even if an unstable and easily decomposed gaseous unsaturated hydrocarbon is used as the carburizing gas, the necessary amount of carburizing gas is catalytically decomposed to the surface of the work in a short time to carburize. As a result, the undecomposed carburizing gas that easily generates soot can be immediately discharged to the outside of the heating chamber together with the generated gas after decomposition (hydrogen gas etc.), which prevents the generation of soot. It became possible to carburize the work. Further, since the decomposition product gas can be discharged to the outside of the heating chamber in a short time, it is possible to further extend the mean free path of the carburizing gas molecules, which contributes to uniform carburization of each part of the work.

【0035】さらに、排気ポンプから外部に排出される
浸炭用ガスの量を測定して、加熱室内に投入する浸炭用
ガスの量を適切に制御することによって、浸炭用ガスの
使用量を最少量に抑えることができる。
Furthermore, by measuring the amount of carburizing gas discharged from the exhaust pump to an appropriate amount and controlling the amount of carburizing gas to be introduced into the heating chamber, the amount of carburizing gas used is minimized. Can be suppressed to

【0036】そしてまた、本発明による真空浸炭方法で
は、化学的に活性で、反応、分解し易いガス状の鎖式不
飽和炭化水素を浸炭用ガスとして使用しているため、従
来のメタン系ガスのように、必要量以上に浸炭用ガスを
供給しなくても、ワーク表面で容易に反応、分解して浸
炭することができ、浸炭用ガスの供給量は、ワーク表面
の浸炭に必要な全炭素量の2倍程度以内の炭素原子数の
もので済む。ちなみに、従来の真空浸炭では、浸炭に必
要な全炭素量の数十倍程度を炉内に供給していた。さら
に、本発明による真空浸炭方法では、1kPa 以下の低圧
で真空浸炭を行なっており、加熱室自体が加熱室外に対
して断熱効果を発揮することから、放熱が少なく、加熱
室内の温度を維持するための熱量を少なくすることがで
きる。
Further, in the vacuum carburizing method according to the present invention, since a chain-like unsaturated hydrocarbon which is chemically active and easily reacts and decomposes is used as the carburizing gas, the conventional methane-based gas is used. Even if the carburizing gas is not supplied in excess of the required amount, the work surface can be easily reacted, decomposed and carburized, and the carburizing gas is supplied in the total amount required for carburizing the work surface. The number of carbon atoms within about twice the amount of carbon is sufficient. By the way, in the conventional vacuum carburizing, about tens of times the total carbon amount required for carburizing was supplied into the furnace. Furthermore, in the vacuum carburizing method according to the present invention, vacuum carburizing is performed at a low pressure of 1 kPa or less, and since the heating chamber itself exhibits an adiabatic effect to the outside of the heating chamber, heat dissipation is small and the temperature inside the heating chamber is maintained. It is possible to reduce the amount of heat required for this.

【0037】したがって、本発明による真空浸炭方法で
は、浸炭用ガスとして、従来では煤の発生を招くだけと
して見向きもされなかったガス状の鎖式不飽和炭化水素
を敢えて使用したにも拘らず、従来の真空浸炭方法に比
べて、煤の発生を抑えて、深い凹部の内壁面をも含めて
ワークの各部を均一に浸炭でき、さらに使用するガス量
や熱量も節減することができるという、著しい効果を得
ることができる。
Therefore, in the vacuum carburizing method according to the present invention, as the carburizing gas, a chain-like unsaturated hydrocarbon in the form of gas, which has not been considered in the past for only causing the generation of soot, is used, Compared with the conventional vacuum carburizing method, it is possible to suppress the generation of soot, uniformly carburize each part of the work including the inner wall surface of the deep recess, and further reduce the amount of gas and heat used. The effect can be obtained.

【0038】さらに、本発明による真空浸炭方法では、
加熱室内を1kPa 以下の低圧にしており、加熱室自体が
加熱室外に対して断熱効果を発揮することから、加熱室
自体を、水冷したり、断熱保護したりする必要が低減さ
れるため、加熱室を含む真空容器の外壁を、低圧に維持
する構造のみにして、特別の断熱構造としなくても済
み、真空浸炭炉の製造工数、製造コストを低減すること
にも寄与できる。
Further, in the vacuum carburizing method according to the present invention,
Since the heating chamber is set to a low pressure of 1 kPa or less and the heating chamber itself exerts a heat insulating effect against the outside of the heating chamber, it is possible to reduce the need for water cooling or heat insulating protection of the heating chamber itself. The outer wall of the vacuum container including the chamber does not have to have a special heat insulating structure by only maintaining the structure at a low pressure, which can contribute to reduction of manufacturing steps and manufacturing cost of the vacuum carburizing furnace.

【0039】なお、ワークを低圧で浸炭する方法として
は、イオン浸炭やプラズマ浸炭が知られているが、これ
らの浸炭方法でも、ワークに深い凹部がある場合には、
イオン化したガスが凹部の底までまで到達できない等の
理由により、浸炭ムラが発生することが避けられず、ま
た従来の真空浸炭方法より煤の発生が少ないものの、本
発明の真空浸炭方法のように煤の発生を抑えることがで
きず、さらに、設備コストも高いという欠点がある。
Ion carburizing and plasma carburizing are known as methods for carburizing a work at a low pressure. However, even with these carburizing methods, if the work has a deep recess,
Due to the reason that the ionized gas cannot reach the bottom of the recess, it is unavoidable that carburizing unevenness occurs, and soot is less generated than the conventional vacuum carburizing method, but like the vacuum carburizing method of the present invention. There is a drawback that the generation of soot cannot be suppressed and the equipment cost is high.

【0040】そして、本発明で使用するガス状の鎖式不
飽和炭化水素としてのエチレンガスやアセチレンガスの
中でアセチレンガスを使用する場合には、エチレンガス
に比べて構成する水素原子が少なく、活性で、浸炭処理
を行ない易く、かつ、使用量を低減し、処理コストを低
減することができる。
When acetylene gas is used among ethylene gas and acetylene gas as the gaseous chain unsaturated hydrocarbon used in the present invention, the number of hydrogen atoms formed is smaller than that of ethylene gas. It is active and easy to carry out carburizing treatment, and it is possible to reduce the amount used and the treatment cost.

【0041】さらに浸炭用ガスとしてのアセチレンガス
に加えて、ガス状の窒素源として例えばアンモニアガス
(NH3 )を添加して浸炭窒化処理を行なうことによ
り、より低い温度からの焼入れ処理が可能になり、歪み
を小さくすることができる。
Further, in addition to acetylene gas as a carburizing gas, for example, ammonia gas (NH 3 ) is added as a gaseous nitrogen source to carry out carbonitriding treatment, whereby quenching treatment from a lower temperature becomes possible. Therefore, the distortion can be reduced.

【0042】[0042]

【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0043】図1は本発明による真空浸炭装置の一実施
の形態を示す図で、真空浸炭炉1は真空容器4で覆われ
た加熱室2とこの加熱室2に隣接する冷却室3とを備え
ている。
FIG. 1 is a diagram showing an embodiment of a vacuum carburizing apparatus according to the present invention. A vacuum carburizing furnace 1 includes a heating chamber 2 covered with a vacuum container 4 and a cooling chamber 3 adjacent to the heating chamber 2. I have it.

【0044】加熱室2は、高温環境の真空中および大気
中において化学的・強度的に安定な発熱体2aおよび断
熱材2bから構成されている。発熱体2aとしては、例
えば再結晶処理した炭化ケイ素系発熱体、あるいは、そ
の表面にアルミナ溶射被覆層を形成したものを使用する
ことができる。断熱材2bとしては、高純度セラミック
ファイバを使用することができる。冷却室3は、その外
壁が真空容器4の一部で構成され、油槽3aを備えてい
る。
The heating chamber 2 is composed of a heating element 2a and a heat insulating material 2b which are chemically and strength stable in vacuum and in the atmosphere of a high temperature environment. As the heating element 2a, it is possible to use, for example, a recrystallized silicon carbide-based heating element or one having an alumina sprayed coating layer formed on the surface thereof. A high-purity ceramic fiber can be used as the heat insulating material 2b. The cooling chamber 3 has an outer wall formed of a part of the vacuum container 4 and includes an oil tank 3a.

【0045】そして、加熱室2と冷却室3には、ともに
真空排気源Vが接続され、また加熱室2には、アセチレ
ンガスをアセトンに溶解させて、アセチレンガスを供給
可能な浸炭ガス源Cが接続され、冷却室3には、この冷
却室3内を大気圧以上に加圧可能な窒素ガス等の不活性
ガス源Gが接続されている。
A vacuum exhaust source V is connected to both the heating chamber 2 and the cooling chamber 3, and the carburizing gas source C capable of supplying acetylene gas to the heating chamber 2 by dissolving acetylene gas in acetone. Is connected to the cooling chamber 3. An inert gas source G such as nitrogen gas that can pressurize the inside of the cooling chamber 3 to atmospheric pressure or more is connected to the cooling chamber 3.

【0046】また、加熱室2の上流端には搬入扉5が、
下流端には中間扉6が、冷却室3の下流端には搬出扉7
が設けられ、加熱室2から冷却室3に亘って上流から下
流へワークMを搬送する内部搬送装置8が設けられてい
る。冷却室3内にはワークMを油槽3aに出し入れする
ための昇降台9が設置されている。さらに加熱室2には
内部搬入扉5aと内部中間扉6aで前後端を閉じた加熱
部が設けられている。
A carry-in door 5 is provided at the upstream end of the heating chamber 2.
An intermediate door 6 is provided at the downstream end, and a carry-out door 7 is provided at the downstream end of the cooling chamber 3.
And an internal transfer device 8 that transfers the work M from the upstream to the downstream from the heating chamber 2 to the cooling chamber 3. An elevating table 9 for loading and unloading the work M into and from the oil tank 3a is installed in the cooling chamber 3. Further, the heating chamber 2 is provided with a heating section whose front and rear ends are closed by an internal carry-in door 5a and an internal intermediate door 6a.

【0047】次にこのような構成を有する真空浸炭装置
を使用した真空浸炭方法について、図2を参照して説明
する。なお、予め加熱室2を大気圧状態で所定の温度に
加熱しておく。
Next, a vacuum carburizing method using the vacuum carburizing apparatus having such a structure will be described with reference to FIG. The heating chamber 2 is preheated to a predetermined temperature under atmospheric pressure.

【0048】第1工程 搬入扉5,5aを開放して、第1ワークM1を加熱室2
内に搬入し、直ちに搬入扉5,5aを閉鎖する。
The first process carry-in doors 5 and 5a are opened, and the first work M1 is heated in the heating chamber 2
It is carried in, and the carry-in doors 5 and 5a are immediately closed.

【0049】第2工程 加熱室2を真空排気源Vによって0.05kPa まで真空
排気しながら、第1ワークM1を所定温度(900℃)
まで真空加熱し、その後、浸炭ガス源Cからアセチレン
ガスを加熱室2内に供給して(このとき、加熱室2内は
0.1kPa となる)、浸炭処理を行なう。そして、アセ
チレンガスの供給を停止して、加熱室2内を再び0.0
5kPa までの真空として拡散処理を行ない、さらに、焼
入れ温度の850℃まで降温均熱加熱を行なう。なお、
その間に、冷却室3を真空排気しておく。
Second step While the heating chamber 2 is evacuated to 0.05 kPa by the vacuum exhaust source V, the first work M1 is heated to a predetermined temperature (900 ° C.).
It is vacuum-heated up to, and then acetylene gas is supplied from the carburizing gas source C into the heating chamber 2 (at this time, the inside of the heating chamber 2 becomes 0.1 kPa) to perform the carburizing treatment. Then, the supply of acetylene gas is stopped, and the inside of the heating chamber 2 is again set to 0.0
Diffusion treatment is performed under a vacuum of up to 5 kPa, and further soaking and heating are performed to lower the quenching temperature to 850 ° C. In addition,
Meanwhile, the cooling chamber 3 is evacuated.

【0050】第3工程 中間扉6,6aを開放し、内部搬送装置8によって、第
1ワークM1を冷却室3の昇降台9上に移送し、直ちに
中間扉6,6aを閉鎖する。
Third step The intermediate doors 6, 6a are opened, the first work M1 is transferred onto the elevating table 9 of the cooling chamber 3 by the internal transfer device 8, and the intermediate doors 6, 6a are immediately closed.

【0051】第4工程 不活性ガス源Gからの不活性ガスの供給により冷却室3
を大気圧以上に加圧しつつ、昇降台9を降下させて第1
ワークM1を焼入れ処理する。その間に高温の加熱室2
内へ空気を導入して大気状態とし、さらに搬入扉5,5
aを開放して、第2ワークM2を加熱室2内に搬入し、
直ちに搬入扉5,5aを閉鎖する。なお、冷却室3を大
気圧以上に加圧する理由は、加熱室2内に空気を導入す
る際、その空気が冷却室3内へ入り込まないようにする
ためである。
Fourth step Cooling chamber 3 is supplied by supplying an inert gas from inert gas source G.
While raising the pressure above the atmospheric pressure, the elevator 9 is lowered to
The work M1 is quenched. Meanwhile, the high temperature heating chamber 2
Air is introduced into the inside to make it into an atmospheric state, and then the carry-in doors 5 and 5
a is opened, the second work M2 is loaded into the heating chamber 2,
Immediately, the carry-in doors 5 and 5a are closed. The reason why the cooling chamber 3 is pressurized above atmospheric pressure is to prevent the air from entering the cooling chamber 3 when the air is introduced into the heating chamber 2.

【0052】第5工程 昇降台9を上昇させ、搬出扉7を開放して第1ワークM
1を炉1外へ搬出し、直ちに搬出扉7を閉鎖して冷却室
3を真空冷却する。その間に、第2ワークM2を第2工
程と同様に取り扱う。
Fifth step The lift table 9 is raised, the carry-out door 7 is opened, and the first work M is opened.
1 is carried out of the furnace 1, the carrying-out door 7 is immediately closed, and the cooling chamber 3 is vacuum-cooled. Meanwhile, the second work M2 is handled in the same manner as the second step.

【0053】以下、定常状態では、第3〜第5工程が反
復され、順次ワークの浸炭処理が行なわれる。
Hereinafter, in a steady state, the third to fifth steps are repeated and the carburizing process of the work is sequentially performed.

【0054】このように浸炭処理が施されるワークの一
例として、図3に断面図で示すような、外径寸法を20
mm、長さを30mmとして、内径6mm、深さ28mmの閉端
孔11と、内径4mm、深さ28mmの閉端孔12とを備え
たワークサンプル10を、幅400mm、長さ600mm、
高さ50mmの治具に300個並置し、その治具を6段重
ねて加熱室2内に配置し、浸炭温度900℃で、浸炭時
間40分、拡散時間70分、焼入れ温度850℃として
処理した場合、各ワークの有効浸炭深さt0 は0.51
mm前後であったのに対し、小径の閉端孔12の底部の有
効浸炭深さt2は0.49mm前後であった。すなわち、
これは本実施の形態の真空浸炭方法によれば、0.02
mm前後のバラツキで、各部を均一に浸炭処理を行なうこ
とができることを実証している。
As an example of the work carburized in this manner, the outer diameter dimension is 20 as shown in the sectional view of FIG.
mm, length 30 mm, work sample 10 having a closed end hole 11 having an inner diameter of 6 mm and a depth of 28 mm and a closed end hole 12 having an inner diameter of 4 mm and a depth of 28 mm, a width of 400 mm, a length of 600 mm,
300 pieces are juxtaposed on a jig with a height of 50 mm, and the jigs are stacked in 6 stages and placed in the heating chamber 2. Carburizing temperature is 900 ° C., carburizing time is 40 minutes, diffusion time is 70 minutes, and quenching temperature is 850 ° C. In this case, the effective carburizing depth t 0 of each work is 0.51
While it was around mm, the effective carburizing depth t 2 at the bottom of the small-diameter closed end hole 12 was around 0.49 mm. That is,
According to the vacuum carburizing method of the present embodiment, this is 0.02
It has been proved that each part can be uniformly carburized with a variation of around mm.

【0055】そして、この試験を数百回反復しても、加
熱室2内には煤の堆積が認められなかった。また、上記
ワークサンプル10に対し、長さをほぼ2倍にしたサン
プルに、内径4mm、深さ50mmの閉端孔を設け、同様に
浸炭処理しても、外周面での有効浸炭深さと孔底部の有
効浸炭深さとの差を0.03mm前後の範囲内に抑えるこ
とができ、本実施の形態の真空浸炭方法によれば、各部
を均一に浸炭処理を行なうことができることを示してい
る。
Even when this test was repeated several hundred times, no soot was found in the heating chamber 2. Further, even if the carburized in the same way as the above-mentioned work sample 10, a closed end hole having an inner diameter of 4 mm and a depth of 50 mm is provided in a sample whose length is almost doubled, and the effective carburizing depth and hole on the outer peripheral surface are The difference from the effective carburizing depth of the bottom can be suppressed within a range of about 0.03 mm, which indicates that the vacuum carburizing method of the present embodiment can uniformly carburize each part.

【0056】ちなみに、従来のメタン系ガスを浸炭用ガ
スとして、ワークサンプル10を従来の真空浸炭方法で
浸炭処理した場合には、浸炭時間を2倍程度として、加
熱室内に10倍以上の浸炭用ガスを供給しても、ワーク
サンプル10の外周面での有効浸炭深さが0.51mm
で、4mmφの孔12の底部の有効浸炭深さが0.30mm
となって、浸炭ムラが発生していた。そしてさらに、従
来の真空浸炭方法では、浸炭処理を5〜20回反復すれ
ば、バーンアウトしても加熱室2内に煤が多量に蓄積
し、清掃が必要となっていた。当然ながら、一般に実施
されているガス浸炭では、孔12の底部への浸炭は全く
期待できない。
By the way, when the work sample 10 is carburized by the conventional vacuum carburizing method using the conventional methane-based gas as the carburizing gas, the carburizing time is set to about twice, and the carburizing time is 10 times or more for the carburizing. Even if gas is supplied, the effective carburizing depth on the outer peripheral surface of the work sample 10 is 0.51 mm.
And the effective carburizing depth at the bottom of the 4 mmφ hole 12 is 0.30 mm.
Then, uneven carburization occurred. Further, in the conventional vacuum carburizing method, if the carburizing treatment is repeated 5 to 20 times, a large amount of soot is accumulated in the heating chamber 2 even after burnout, and cleaning is required. As a matter of course, in the case of gas carburizing generally performed, carburization of the bottom of the hole 12 cannot be expected at all.

【0057】なお、本発明の真空浸炭方法では、加熱室
内を1kPa 以下の真空状態で浸炭を行なっていることに
より、アセチレンガスを浸炭用ガスとして使用しても、
ワークの浸炭ムラをなくし、かつ煤の発生を抑えて浸炭
処理を行なうことがができるが、加熱室内を1kPa を超
える圧力として浸炭処理を行なった場合は、煤の発生を
抑え難くなり、浸炭も不均一になって望ましくない。
In the vacuum carburizing method of the present invention, since the heating chamber is carburized in a vacuum state of 1 kPa or less, even if acetylene gas is used as the carburizing gas,
Carburizing treatment can be performed by eliminating uneven carburization of the work and suppressing soot generation. However, when carburizing treatment is performed with a pressure exceeding 1 kPa in the heating chamber, it becomes difficult to suppress soot generation and carburization also occurs. Unevenness is not desirable.

【0058】そして、加熱室内を低圧にすればする程、
本発明の方法の効果を増大させることができ、さらに、
加熱室自体の断熱効果も有効に発揮でき、水冷、保温等
が不要となって、省エネルギー効果を高めることができ
る観点から、望ましくは、加熱室内を0.3kPa 以下、
さらに望ましくは0.1kPa 以下に減圧して、浸炭処理
を行なうことが好ましい。
The lower the pressure in the heating chamber is, the more
It is possible to increase the effect of the method of the present invention, and further,
From the viewpoint that the heat insulating effect of the heating chamber itself can be effectively exerted, water cooling, heat retention, etc. are not required and the energy saving effect can be enhanced, it is desirable that the heating chamber has 0.3 kPa or less,
More desirably, it is preferable to carry out the carburizing treatment under a reduced pressure of 0.1 kPa or less.

【0059】図4は、内径6mm、深さ27mmの閉端孔を
備えた外径20mm、長さ30mmのサンプル(SCM41
5)に対して、温度930℃において、保持時間、浸炭
時間および拡散時間(図2参照)をそれぞれ30分、3
0分、45分として、アセチレンガスを用いて浸炭処理
を施した場合の炉内圧力に対する浸炭深さの関係および
煤発生状況を示すグラフである。折線Aは閉端孔の底部
における浸炭深さの変化を、折線Bはワークサンプルの
表面における浸炭深さの変化をそれぞれ表すグラフであ
る。
FIG. 4 shows a sample (SCM41) having an inner diameter of 6 mm and a closed end hole having a depth of 27 mm and having an outer diameter of 20 mm and a length of 30 mm.
5), at a temperature of 930 ° C., holding time, carburizing time and diffusion time (see FIG. 2) were 30 minutes and 3 respectively.
It is a graph which shows the relationship of the carburizing depth with respect to the pressure in the furnace when the carburizing treatment is performed using acetylene gas as 0 minutes and 45 minutes, and the soot generation state. A polygonal line A is a graph showing a change in carburizing depth at the bottom of the closed end hole, and a polygonal line B is a graph showing a change in carburizing depth at the surface of the work sample.

【0060】図4から明らかなように、サンプルの表面
に関しては、炉内圧力が1.0kPa以下のとき、ほぼ一
定の浸炭深さが得られる。しかしながら、閉端孔の内外
を均一に浸炭するためには、炉内圧力を0.3kPa 以下
にすることが望ましい。
As is clear from FIG. 4, with respect to the surface of the sample, when the pressure in the furnace is 1.0 kPa or less, a substantially constant carburizing depth is obtained. However, in order to uniformly carburize the inside and outside of the closed end hole, it is desirable that the furnace pressure be 0.3 kPa or less.

【0061】また煤発生状況から見れば、炉内圧力が
1.0kPa 以下であれば問題はない。
From the viewpoint of soot generation, there is no problem if the furnace pressure is 1.0 kPa or less.

【0062】図5は、内径3.4mm、深さ175mmの閉
端孔を備えた外径20mm、長さ182mmの寸法を有する
サンプル(SCM415)に本発明の浸炭方法を実施し
て浸炭層を形成した状態を示す断面図と、浸炭の均一性
を表すグラフである。この場合、炉内温度930℃、炉
内圧力0.02kPa 、浸炭時間と拡散時間の和を430
分とし、サンプルの積載条件は前述と同様である。
FIG. 5 shows a sample (SCM415) having an inner diameter of 3.4 mm, a closed end hole having a depth of 175 mm and an outer diameter of 20 mm, and a length of 182 mm, which is subjected to the carburizing method of the present invention to form a carburized layer. It is a sectional view showing a formed state, and a graph showing uniformity of carburization. In this case, the furnace temperature is 930 ° C., the furnace pressure is 0.02 kPa, and the sum of carburizing time and diffusion time is 430.
The sample loading conditions are the same as described above.

【0063】図5から明らかなように、閉端孔の内壁面
における全浸炭深さがほぼ等しい(2.1mm)領域が閉
端孔の入口から122mmの深さに達し、深さ156mmの
位置で全浸炭深さがゼロになった。すなわち、の内径を
Dとする閉端孔の内壁面における全浸炭深さのほぼ等し
い領域が、この閉端孔の開口端から深さLの領域に亘っ
て形成されているとするとき、上記Lの値がL/D比で
36にまで達している。このように、炉内圧力が低くな
るに伴って、浸炭の均一性も増大している。さらに炉内
圧力を低くすれば、全浸炭深さのほぼ等しい領域の深さ
Lの値を、L/D比で50程度にまですることができ
る。
As is clear from FIG. 5, a region where the total carburizing depth on the inner wall surface of the closed end hole is approximately equal (2.1 mm) reaches a depth of 122 mm from the inlet of the closed end hole, and a depth of 156 mm. The total carburizing depth became zero. That is, when it is assumed that a region of the inner wall surface of the closed end hole having a total carburizing depth substantially equal to that of D is formed from the open end of the closed end hole to the region of depth L, The value of L reaches 36 in the L / D ratio. Thus, as the pressure inside the furnace decreases, the uniformity of carburization also increases. Further, if the pressure in the furnace is lowered, the value of the depth L in the region where the total carburizing depth is substantially equal can be increased to about 50 in L / D ratio.

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

【図1】本発明による真空浸炭装置の一実施の形態を示
す断面図
FIG. 1 is a sectional view showing an embodiment of a vacuum carburizing apparatus according to the present invention.

【図2】本発明による真空浸炭炉の運転パターンを示す
FIG. 2 is a diagram showing an operation pattern of the vacuum carburizing furnace according to the present invention.

【図3】本発明による真空浸炭方法により浸炭処理した
サンプルの断面図
FIG. 3 is a sectional view of a sample carburized by a vacuum carburizing method according to the present invention.

【図4】本発明による真空浸炭方法を実施した場合の炉
内圧力に対する浸炭深さの関係および煤発生状況を示す
グラフ
FIG. 4 is a graph showing the relationship between carburizing depth and pressure in the furnace and the soot generation state when the vacuum carburizing method according to the present invention is carried out.

【図5】本発明による真空浸炭方法を実施したサンプル
における全浸炭層を示す断面図と浸炭深さの均一性を表
すグラフ
FIG. 5 is a cross-sectional view showing the entire carburized layer in a sample subjected to the vacuum carburizing method of the present invention and a graph showing the uniformity of carburizing depth.

【符号の説明】[Explanation of symbols]

1 真空浸炭炉 2 加熱室 3 冷却室 M ワーク V 真空排気源 C 浸炭ガス源 G 不活性ガス源 1 Vacuum carburizing furnace 2 Heating chamber 3 Cooling chamber M Work V Vacuum exhaust source C Carburizing gas source G Inert gas source

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 鋼材よりなるワークを、真空浸炭炉の加
熱室内で真空加熱するとともに、該加熱室内に浸炭用ガ
スを供給して浸炭処理を行なう真空浸炭方法であって、 前記浸炭用ガスとしてガス状の鎖式不飽和炭化水素を使
用するとともに、前記加熱室内を1kPa 以下の真空状態
として浸炭処理を行なうことを特徴とする真空浸炭方
法。
1. A vacuum carburizing method in which a workpiece made of steel material is vacuum-heated in a heating chamber of a vacuum carburizing furnace and a carburizing gas is supplied into the heating chamber to perform carburizing treatment. A vacuum carburizing method characterized in that a gaseous chain unsaturated hydrocarbon is used, and a carburizing process is performed in a vacuum state of 1 kPa or less in the heating chamber.
【請求項2】 前記ガス状の鎖式不飽和炭化水素がアセ
チレン系ガスよりなることを特徴とする請求項1記載の
真空浸炭方法。
2. The vacuum carburizing method according to claim 1, wherein the gaseous chain unsaturated hydrocarbon comprises an acetylene-based gas.
【請求項3】 前記アセチレン系ガスがアセチレンガス
よりな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 acetylene-based gas comprises acetylene gas.
【請求項4】 前記浸炭用ガスにガス状の窒素源を添加
して浸炭処理を行なうことをことを特徴とする請求項1
記載の真空浸炭方法。
4. The carburizing process is performed by adding a gaseous nitrogen source to the carburizing gas.
The vacuum carburizing method described.
【請求項5】 鋼材よりなるワークを加熱する加熱室を
備えた真空浸炭炉と、前記加熱室内にアセチレン系ガス
を供給する浸炭用ガス源と、前記加熱室内を真空排気す
る真空排気源とを備え、1kPa 以下の真空状態で真空浸
炭を行なうことを特徴とする真空浸炭装置。
5. A vacuum carburizing furnace having a heating chamber for heating a work made of steel, a carburizing gas source for supplying an acetylene-based gas into the heating chamber, and a vacuum exhaust source for evacuating the heating chamber. A vacuum carburizing device, which is equipped with a vacuum carburizing method of 1 kPa or less.
【請求項6】 内径をDとする閉端孔を備え、該閉端孔
の内壁面における浸炭深さのほぼ等しい領域が、該閉端
孔の開口端から深さLの範囲に亘って形成されている浸
炭処理された鋼材製品であって、 前記深さLの値が、L/D比で12乃至50の範囲内に
あることを特徴とする浸炭処理された鋼材製品。
6. A closed end hole having an inner diameter of D is provided, and a region having substantially the same carburizing depth on the inner wall surface of the closed end hole is formed over a range of a depth L from an open end of the closed end hole. Carburized steel product, wherein the value of the depth L is within the range of 12 to 50 in terms of L / D ratio.
【請求項7】 前記閉端孔の内壁面における浸炭深さ
が、L/D比で12乃至36の領域に亘ってほぼ等しい
ことを特徴とする請求項6記載の浸炭処理された鋼材製
品。
7. The carburized steel product according to claim 6, wherein the carburizing depth on the inner wall surface of the closed end hole is substantially equal over a region of 12 to 36 in terms of L / D ratio.
JP6793796A 1995-03-29 1996-03-25 Vacuum carburizing method and apparatus and carburized product Expired - Lifetime JP2963869B2 (en)

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JP6793796A JP2963869B2 (en) 1995-03-29 1996-03-25 Vacuum carburizing method and apparatus and carburized product
TW85104133A TW400394B (en) 1995-03-29 1996-04-09 Vacuum carburizing method and device, and carburized

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JP7-72043 1995-03-29
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