JP3854851B2 - Carburizing method for steel parts - Google Patents

Carburizing method for steel parts Download PDF

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JP3854851B2
JP3854851B2 JP2001344338A JP2001344338A JP3854851B2 JP 3854851 B2 JP3854851 B2 JP 3854851B2 JP 2001344338 A JP2001344338 A JP 2001344338A JP 2001344338 A JP2001344338 A JP 2001344338A JP 3854851 B2 JP3854851 B2 JP 3854851B2
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carburizing
gas
diffusion
period
temperature
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JP2003147506A (en
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豊 武田
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Chugai Ro Co Ltd
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Chugai Ro Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は鋼材部品の浸炭方法、特に、鋼材部品の表面炭素濃度を均一化することができる浸炭方法に関するものである。
【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900〜1050℃の浸炭温度まで加熱し、均熱状態に達した時点で浸炭性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鋼材中に炭素を侵入させる浸炭期と、浸炭性ガスの供給を停止して真空下(約0.2kPa)で所定時間保持することにより鋼材中に炭素を拡散させる拡散期とを含むものである。この真空浸炭処理においては、浸炭深さと表面炭素濃度は、浸炭時間と拡散時間を制御することにより調整される。なお、浸炭性ガスとしては、プロパン、プロピレン、エチレン或いはアセチレン等が使用される。
【0003】
しかしながら、この真空浸炭処理は、COやH2等の吸熱型変成ガスを含む浸炭雰囲気中で行うガス浸炭処理と比較して浸炭時間を短縮できる長所があるが、高温で処理されること、及び拡散期が真空下であることから、鋼材部品の先鋭部にセメンタイトが析出されるという問題がある。即ち、浸炭期に鋼材部品表面に侵入した炭素は、拡散期に鋼材部品内部に拡散するが、この拡散は、単位表面に対して内部体積の小さい部位(例えば、角柱部品のコーナー部や歯車の歯先部等、以下、先鋭部という)では遅いことから、当該先鋭部以外の部分(例えば、平坦部)で所望の表面炭素濃度を確保しようとすると、前記先鋭部にセメンタイトが析出し、逆に、当該先鋭部で所望の表面炭素濃度を確保しようとすると、前記先鋭部以外の部分が浸炭不足(焼入硬度不足)となるという問題がある。
【0004】
他方、真空浸炭における表面炭素濃度を調整する手段として、拡散期を減圧脱炭雰囲気中で行う方法が特開昭61-117268号明細書にて提案されている。この方法は、CO2ガス単体又はCO2ガスとN2ガスとの混合ガスを断続的に或いは連続的に供給しながら所定時間保持することにより先鋭部の過剰浸炭を優先的に脱炭させるようにしたものである。
【0005】
【発明が解決しようとする課題】
前記拡散期を脱炭雰囲気ガス中で行う浸炭方法は、平滑部よりも先鋭部を優先的に脱炭させるため、先鋭部のセメンタイトの析出を防止できる利点はあるが、拡散処理を拡散時間の管理で行っているため、表面炭素濃度の均一化には厳格な拡散時間の管理が必要となると共に、拡散時間は鋼材部品の形状によって異なることから形状の異なる鋼材部品を混載処理することができないという問題があった。
【0006】
従って、本発明は、表面炭素濃度の均一化とセメンタイトの析出防止を図ることを課題とするものである。
【0007】
【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、浸炭期と拡散期を含む鋼材部品の浸炭方法において、浸炭期を所定減圧下の浸炭性ガス中で行うと共に、拡散期をCOを含む雰囲気ガス(以下、CO含有雰囲気ガスという。)中で、当該雰囲気中のカーボンポテンシャル(CP)値を管理しながら行うようにしたものである。
【0008】
即ち、本発明は、拡散期をCO含有雰囲気ガス中で行うと同時に、当該拡散期の雰囲気中のカーボンポテンシャル値を被処理材である鋼材部品の所望表面炭素濃度に応じて管理しながら行うことにより真空浸炭法の欠点を解消するようにしたものである。
【0009】
浸炭性ガスとしては、エチレン、アセチレンなどの不飽和炭化水素系ガスやメタン、エタン、プロパン、ブタンなどの飽和炭化水素が使用されるが、好ましい実施態様においては、浸炭性ガスとしてアセチレンガスが使用される。
【0010】
なお、所定減圧下とは浸炭性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、使用する浸炭性ガスの種類によって規定される。浸炭性ガスとしてアセチレンガスを使用する場合、浸炭処理は、通常、1.5〜3.5kPaのアセチレンガス下で5分〜2時間行われる。
【0011】
前記浸炭期初期の圧力を1.5kPa〜3.5kPa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。
【0012】
本発明に係る浸炭方法では、拡散期は、CO含有雰囲気ガス中で当該雰囲気中のカーボンポテンシャル値を管理しながら大気圧下で行われるが、前記CO含有雰囲気ガスとしては、吸熱型変成ガスが使用される。なお、前記吸熱型変成ガスの組成は、CO:20.9〜23.9%、CO2:0.15〜0.2%、H2:30.4〜38.9%、N2残である。前記CO含有雰囲気ガス中で鋼材部品を加熱すると、当該雰囲気ガスのCO濃度と鋼材中の炭素との間で平衡が成り立ち、当該雰囲気中のCO濃度、即ち、カーボンポテンシャルを制御することにより鋼材部品の表面炭素濃度を均一化することが可能となる。
【0013】
この拡散期のCO含有雰囲気ガス中のカーボンポテンシャル値の制御は、炉内のCO含有雰囲気中のカーボンポテンシャルを直接又は間接的に測定し、その測定値を設定目標値と比較して差を求め、その差に応じて炉内へのCO含有雰囲気ガス及びその添加ガス(炭化水素ガス)の供給量を増減することにより行うことができる。
【0014】
【発明の実施の形態】
以下、本発明に係る鋼材部品の浸炭方法において、浸炭期の浸炭性ガスとしてアセチレンガスを、拡散期のCO含有雰囲気ガスとして吸熱型変成ガスと窒素ガスとの混合ガス及び吸熱型変成ガス単体をそれぞれ用いた場合について、本発明方法の浸炭ヒートサイクルの一例を示す図1を参照して説明する。
【0015】
まず、炉の加熱室内に鋼材部品を配置し、加熱室内を窒素ガスに置換した後、ほぼ大気圧状態のN2雰囲気中で鋼材部品を対流加熱により浸炭温度(900〜1050℃)まで昇温させる。次いで、加熱室内を前記浸炭温度でクロム酸化物やマンガン酸化物などの鋼材部品表面の酸化物が還元する真空度(約0.02kPa)まで真空排気した後、所定量の炭素供給源(例えば、炭化水素系ガス)を加熱室内に導入し、加熱室内を前記真空度及び加熱室内温度に維持しながら0.1〜1時間加熱保持して鋼材部品表面を活性化させる。
【0016】
活性化処理後、前記浸炭温度を維持した状態で加熱室内に所定量の浸炭ガス(例えば、飽和炭化水素系ガス、不飽和炭化水素系ガス又はそれらの混合物)を供給し、加熱室内を所定の真空度に維持しながら所定時間(5分〜2時間)保持して浸炭処理を行う。浸炭処理後、浸炭ガスの供給を停止し、加熱室内にCO含有雰囲気ガスを供給して大気圧にまで昇圧させ、前記加熱室内を前記温度に維持し、かつ、炉内雰囲気のカーボンポテンシャルを所定値に維持しながら所定時間(5分〜2時間)加熱保持して拡散処理を行う。拡散処理終了後、加熱室内を前記雰囲気に維持したまま焼入れ温度まで降温させ、同温度に所定時間維持した後、焼入れ処理を行う。
【0017】
このように拡散期をCO含有雰囲気中で、かつ、当該雰囲気のカーボンポテンシャルを所定の一定値に制御しながら行うことにより、過剰浸炭となる部位(先鋭部)の表面では脱炭が行われる一方、平坦部表面では拡散が行われることになり、一様な表面炭素濃度を得ると共に、セメンタイトの析出を防止できる。また、装入室、浸炭室及び拡散室の各間に開閉式隔壁を介在させて小容積の中間室を設け、当該中間室を介して処理材の移送を順次行うようにすると、雰囲気を撹乱することなく浸炭及び拡散処理を行うことができる。
【0018】
【実施例1】
SCR420製シャフトを処理材とし、目標有効浸炭深さ0.8mmとして下記の条件下で浸炭処理を行った。
浸炭処理:
浸炭温度:950℃
浸炭時間:45分
浸炭性ガス:アセチレンガス
処理圧力:1.5kPa(制御値)
拡散処理:
拡散温度: 950℃
拡散時間: 40分間
処理圧力: 約100kPa
雰囲気: 吸熱型変成ガス+N2ガス(CO:10体積%)
CP値: 0.89
焼入れ処理:
焼入れ温度: 850℃
焼入れ液: 油(温度:120℃)
【0019】
得られた処理材の有効浸炭深さは0.78〜0.82mmでほぼ均一な浸炭層が形成されており、良好な浸炭処理材が得られた。
【0020】
【実施例2】
SCM420製歯車を処理材とし、目標有効浸炭深さ0.6mmとして下記の条件下で浸炭処理を行った。
浸炭処理:
浸炭温度:950℃
浸炭時間:30分
浸炭性ガス:アセチレンガス
処理圧力:1.5kPa(制御値)
拡散処理:
拡散温度: 950℃
拡散時間: 25分間
処理圧力: 約100kPa
雰囲気: 吸熱型変成ガス(CO:23体積%)
CP値: 0.85
焼入れ処理:
焼入れ温度: 850℃
焼入れ液: 油(温度:120℃)
【0021】
得られた処理材の有効浸炭深さは0.60〜0.65mmでほぼ均一な浸炭層が形成されており、良好な浸炭処理材が得られた。
【0022】
【実施例3】
SCM420製大型歯車を処理材とし、目標有効浸炭深さ1.2mmとして下記の条件下で浸炭処理を行った。
浸炭処理:
浸炭温度: 950℃
浸炭時間: 120分
浸炭性ガス:アセチレンガス
処理圧力: 1.5kPa(制御値)
拡散処理:
拡散温度: 950℃
拡散時間: 85分間
処理圧力: 約100kPa
雰囲気: 吸熱型変成ガス+N2ガス(CO:15体積%)
CP値: 0.85
焼入れ処理:
焼入れ温度: 850℃
焼入れ液: 油(温度:120℃)
【0023】
得られた処理材の有効浸炭深さは1.20〜1.24mmでほぼ均一な浸炭層が形成されており、良好な浸炭処理材が得られた。
【0024】
【実施例4】
SCM415製リニアブロックを処理材とし、目標有効浸炭深さ1.6mmとして下記の条件下で浸炭処理を行った。
浸炭処理:
浸炭温度: 950℃
浸炭時間: 200分
浸炭性ガス:アセチレンガス
処理圧力: 1.5kPa(制御値)
拡散処理:
拡散温度: 950℃
拡散時間: 160分間
処理圧力: 約100kPa
雰囲気: 吸熱型変成ガス+N2ガス(CO:8体積%)
CP値: 0.8
焼入れ処理:
焼入れ温度: 850℃
焼入れ液: 油(温度:120℃)
【0025】
得られた処理材の有効浸炭深さは1.56〜1.62mmでほぼ均一な浸炭層が形成されており、良好な浸炭処理材が得られた。
【0026】
【発明の効果】
以上の説明から明らかなように、本発明は、浸炭期と拡散期とを含む浸炭方法において、浸炭期を減圧下の浸炭性ガス雰囲気中で行い、拡散期をCO含有雰囲気中で当該雰囲気のカーボンポテンシャルを所定の一定値に制御しながら行うことにより、過剰浸炭となる部位の表面では脱炭しながら、表面全体で拡散を行うことになり、表面炭素濃度を均一化できると共に、セメンタイトの析出を防止できる。
【図面の簡単な説明】
【図1】 本発明方法における浸炭ヒートサイクルの一例を示す図
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a carburizing method for steel parts, and more particularly to a carburizing method capable of making the surface carbon concentration of steel parts uniform.
[0002]
[Prior art]
Conventionally, vacuum carburizing treatment has been performed 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 900 to 1050 ° C. in a vacuum, and when a soaking state is reached, a carburizing gas is supplied into the heating chamber, and the heating chamber is brought to the carburizing temperature. The carburization period in which carbon enters the steel material by holding it for a predetermined time under a predetermined reduced pressure (usually 10 to 70 kPa ) in the maintained state, and the supply of the carburizing gas is stopped and a vacuum (about 0.2 kPa ) and a diffusion period in which carbon is diffused into the steel material by holding for a predetermined time. In this vacuum carburizing process, the carburizing depth and surface carbon concentration are adjusted by controlling the carburizing time and the diffusion time. Note that propane, propylene, ethylene, acetylene, or the like is used as the carburizing gas.
[0003]
However, this vacuum carburizing process has the advantage that the carburizing time can be shortened as compared with the gas carburizing process performed in a carburizing atmosphere containing an endothermic metamorphic gas such as CO or H2, but it is processed at a high temperature and diffusion. Since the period is under vacuum, there is a problem that cementite is deposited on the sharp part of the steel part. In other words, carbon that has entered the surface of the steel part during the carburizing period diffuses into the steel part during the diffusion period, and this diffusion is caused by a portion having a small internal volume with respect to the unit surface (for example, a corner part of a prismatic part or a gear). Since it is slow in a tooth tip portion (hereinafter referred to as a pointed portion), when attempting to secure a desired surface carbon concentration in a portion other than the pointed portion (for example, a flat portion), cementite is deposited on the pointed portion, and conversely In addition, there is a problem that when a desired surface carbon concentration is secured at the sharpened portion, the portion other than the sharpened portion becomes insufficient in carburization (hardening hardness is insufficient).
[0004]
On the other hand, as a means for adjusting the surface carbon concentration in vacuum carburizing, a method of performing a diffusion period in a reduced pressure decarburizing atmosphere has been proposed in JP-A-61-117268. This method is designed to preferentially decarburize excessive carburization at sharp edges by holding CO2 gas alone or a mixed gas of CO2 gas and N2 gas intermittently or continuously for a predetermined time. It is.
[0005]
[Problems to be solved by the invention]
The carburizing method in which the diffusion period is performed in a decarburizing atmosphere gas has an advantage of preventing precipitation of cementite in the sharpened portion because the sharpened portion is preferentially decarburized over the smooth portion, but the diffusion treatment is performed at a diffusion time. Since it is performed by management, strict diffusion time management is required to make the surface carbon concentration uniform, and since the diffusion time varies depending on the shape of the steel part, it is not possible to mix and treat steel parts having different shapes There was a problem.
[0006]
Accordingly, an object of the present invention is to make the surface carbon concentration uniform and prevent precipitation of cementite.
[0007]
[Means for Solving the Problems]
As a means for solving the above-mentioned problems, the present invention provides a carburizing method for steel parts including a carburizing period and a diffusion period, wherein the carburizing period is performed in a carburizing gas under a predetermined reduced pressure, and the diffusion period is an atmosphere containing CO. In a gas (hereinafter referred to as CO-containing atmosphere gas), the carbon potential (CP) value in the atmosphere is managed.
[0008]
That is, according to the present invention, the diffusion period is performed in the CO-containing atmosphere gas, and at the same time, the carbon potential value in the atmosphere in the diffusion period is controlled according to the desired surface carbon concentration of the steel material component to be processed. This eliminates the drawbacks of the vacuum carburizing method.
[0009]
As the carburizing gas, unsaturated hydrocarbon gases such as ethylene and acetylene, and saturated hydrocarbons such as methane, ethane, propane, and butane are used. In a preferred embodiment, acetylene gas is used as the carburizing gas. Is done.
[0010]
Note that under the specified reduced pressure, the degree of vacuum is such that no soot adheres to the surface of the treated material due to thermal decomposition of the carburizing gas, and the carbon supply amount in the initial stage of carburizing can be ensured, and depending on the type of carburizing gas used. It is prescribed. When acetylene gas is used as the carburizing gas, the carburizing treatment is usually performed under 1.5 to 3.5 kPa of acetylene gas for 5 minutes to 2 hours.
[0011]
The reason why the pressure at the initial stage of the carburizing period is set within the range of 1.5 kPa to 3.5 kPa is as follows. That is, when the initial pressure setting value in the carburizing period is 3.5 kPa or less, it is possible to avoid the soot generated by the thermal decomposition of the acetylene gas from adhering to the surface of the treatment material, but when it exceeds 3.5 kPa , This is because it is difficult to avoid the generation of a large amount of soot due to the thermal decomposition of the acetylene gas and the soot from adhering to the surface of the treatment material. Further, when the pressure set value is less than 1.5 kPa , it is impossible to reliably secure the supply amount of acetylene gas at the initial stage of carburizing, which is an important factor for obtaining a uniform carburized layer.
[0012]
In the carburizing method according to the present invention, the diffusion period is performed under atmospheric pressure while managing the carbon potential value in the atmosphere in the CO-containing atmosphere gas. As the CO-containing atmosphere gas, an endothermic modified gas is used. used. The composition of the endothermic modified gas is CO: 20.9 to 23.9%, CO2: 0.15 to 0.2%, H2: 30.4 to 38.9%, and N2 remaining. When a steel part is heated in the CO-containing atmosphere gas, an equilibrium is established between the CO concentration in the atmosphere gas and the carbon in the steel, and the steel part is controlled by controlling the CO concentration in the atmosphere, that is, the carbon potential. It becomes possible to make the surface carbon concentration uniform.
[0013]
The control of the carbon potential value in the CO-containing atmosphere gas during the diffusion period is performed by directly or indirectly measuring the carbon potential in the CO-containing atmosphere in the furnace, and comparing the measured value with the set target value to obtain the difference. Depending on the difference, it can be carried out by increasing or decreasing the supply amount of the CO-containing atmosphere gas and its additive gas (hydrocarbon gas) into the furnace.
[0014]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, in the carburizing method for steel parts according to the present invention, acetylene gas is used as the carburizing gas in the carburizing period, and a mixed gas of endothermic modified gas and nitrogen gas and the endothermic modified gas alone as the CO-containing atmosphere gas in the diffusion period Each case will be described with reference to FIG. 1 showing an example of a carburizing heat cycle of the method of the present invention.
[0015]
First, steel parts are arranged in the furnace heating chamber, and the heating chamber is replaced with nitrogen gas, and then the steel parts are heated to the carburizing temperature (900 to 1050 ° C.) by convection heating in a substantially atmospheric pressure N 2 atmosphere. . Next, after evacuating the heating chamber to a vacuum degree (about 0.02 kPa ) at which the oxides on the surface of the steel material such as chromium oxide and manganese oxide are reduced at the carburizing temperature, a predetermined amount of carbon supply source (for example, , Hydrocarbon-based gas) is introduced into the heating chamber, and the surface of the steel part is activated by heating and holding for 0.1 to 1 hour while maintaining the degree of vacuum and the temperature in the heating chamber.
[0016]
After the activation treatment, a predetermined amount of carburizing gas (for example, saturated hydrocarbon gas, unsaturated hydrocarbon gas, or a mixture thereof) is supplied into the heating chamber while maintaining the carburizing temperature, Carburizing treatment is performed while maintaining a vacuum level for a predetermined time (5 minutes to 2 hours). After the carburizing process, the supply of the carburizing gas is stopped, the CO-containing atmosphere gas is supplied into the heating chamber, the pressure is increased to atmospheric pressure, the heating chamber is maintained at the temperature, and the carbon potential of the furnace atmosphere is set to a predetermined value. While maintaining the value, diffusion treatment is performed by heating and holding for a predetermined time (5 minutes to 2 hours). After the diffusion treatment is completed, the temperature is lowered to the quenching temperature while maintaining the inside of the heating chamber in the above atmosphere, and the quenching treatment is performed after maintaining the same temperature for a predetermined time.
[0017]
In this way, by performing the diffusion period in a CO-containing atmosphere and controlling the carbon potential of the atmosphere to a predetermined constant value, decarburization is performed on the surface of the portion (pointed portion) that becomes excessively carburized. In addition, diffusion is performed on the surface of the flat portion, so that uniform surface carbon concentration can be obtained and cementite precipitation can be prevented. In addition, if a small volume intermediate chamber is provided between the charging chamber, the carburizing chamber, and the diffusion chamber with an openable / closable partition, and the processing material is sequentially transferred through the intermediate chamber, the atmosphere is disturbed. Carburizing and diffusion treatment can be performed without any.
[0018]
[Example 1]
Carburizing treatment was performed under the following conditions using a shaft made of SCR420 as a treatment material and a target effective carburization depth of 0.8 mm.
Carburizing treatment:
Carburizing temperature: 950 ° C
Carburizing time: 45 minutes Carburizing gas: Acetylene gas Processing pressure: 1.5 kPa (Control value)
Diffusion processing:
Diffusion temperature: 950 ° C
Diffusion time: 40 minutes Processing pressure: about 100 kPa
Atmosphere: Endothermic metamorphic gas + N2 gas (CO: 10% by volume)
CP value: 0.89
Quenching process:
Quenching temperature: 850 ° C
Quenching liquid: Oil (Temperature: 120 ° C)
[0019]
The effective carburized depth of the obtained treated material was 0.78 to 0.82 mm, and a substantially uniform carburized layer was formed. Thus, a good carburized material was obtained.
[0020]
[Example 2]
Carburizing treatment was performed under the following conditions with a gear made of SCM420 as a treatment material and a target effective carburization depth of 0.6 mm.
Carburizing treatment:
Carburizing temperature: 950 ° C
Carburizing time: 30 minutes Carburizing gas: Acetylene gas Processing pressure: 1.5 kPa (Control value)
Diffusion processing:
Diffusion temperature: 950 ° C
Diffusion time: 25 minutes Processing pressure: about 100 kPa
Atmosphere: Endothermic modified gas (CO: 23% by volume)
CP value: 0.85
Quenching process:
Quenching temperature: 850 ° C
Quenching liquid: Oil (Temperature: 120 ° C)
[0021]
The effective carburized depth of the obtained treated material was 0.60 to 0.65 mm, and a substantially uniform carburized layer was formed, and a good carburized material was obtained.
[0022]
[Example 3]
Carburizing treatment was performed under the following conditions with a large gear made of SCM420 as the treatment material and a target effective carburization depth of 1.2 mm.
Carburizing treatment:
Carburizing temperature: 950 ° C
Carburizing time: 120 minutes Carburizing gas: Acetylene gas Processing pressure: 1.5 kPa (Control value)
Diffusion processing:
Diffusion temperature: 950 ° C
Diffusion time: 85 minutes Processing pressure: about 100 kPa
Atmosphere: Endothermic metamorphic gas + N2 gas (CO: 15% by volume)
CP value: 0.85
Quenching process:
Quenching temperature: 850 ° C
Quenching liquid: Oil (Temperature: 120 ° C)
[0023]
The effective carburized depth of the obtained treated material was 1.20 to 1.24 mm, and a substantially uniform carburized layer was formed, and a good carburized material was obtained.
[0024]
[Example 4]
Carburizing treatment was performed under the following conditions with a linear block made of SCM415 as the treatment material and a target effective carburization depth of 1.6 mm.
Carburizing treatment:
Carburizing temperature: 950 ° C
Carburizing time: 200 minutes Carburizing gas: Acetylene gas Processing pressure: 1.5 kPa (Control value)
Diffusion processing:
Diffusion temperature: 950 ° C
Diffusion time: 160 minutes Processing pressure: about 100 kPa
Atmosphere: Endothermic metamorphic gas + N2 gas (CO: 8% by volume)
CP value: 0.8
Quenching process:
Quenching temperature: 850 ° C
Quenching liquid: Oil (Temperature: 120 ° C)
[0025]
The effective carburized depth of the obtained treated material was 1.56 to 1.62 mm, and a substantially uniform carburized layer was formed, and a good carburized material was obtained.
[0026]
【The invention's effect】
As is apparent from the above description, the present invention is a carburizing method including a carburizing period and a diffusion period, wherein the carburizing period is performed in a carburizing gas atmosphere under reduced pressure, and the diffusion period is performed in a CO-containing atmosphere. By controlling the carbon potential to a predetermined constant value, the surface of the part that will be excessively carburized will be decarburized and diffused throughout the surface, making the surface carbon concentration uniform and the precipitation of cementite. Can be prevented.
[Brief description of the drawings]
FIG. 1 shows an example of a carburizing heat cycle in the method of the present invention.

Claims (1)

浸炭期と拡散期を含む鋼材部品の浸炭方法において、浸炭期を、浸炭性ガスとしてアセチレンガスを用いて1 . k a 〜3 . k a の浸炭性ガス中で行い、拡散期を、吸熱型変成ガス単体又は吸熱型変成ガスと窒素ガスの混合ガスからなるCO含有雰囲気中で当該雰囲気中のカーボンポテンシャル値を管理しながら大気圧下、浸炭期の浸炭温度で行うことを特徴とする鋼材部品の浸炭方法。In carburizing method of the steel parts, including carburizing period and the diffusion period, performs carburization phase, using acetylene gas as a carburizing gas at 1. 5 k P a ~3. Of 5 k P a carburizing gas, diffusion-life Is carried out at the carburizing temperature at the carburizing stage under atmospheric pressure while controlling the carbon potential value in the CO-containing atmosphere consisting of the endothermic shift gas alone or a mixed gas of the endothermic shift gas and nitrogen gas. Carburizing method for steel parts.
JP2001344338A 2001-11-09 2001-11-09 Carburizing method for steel parts Expired - Lifetime JP3854851B2 (en)

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US9212416B2 (en) 2009-08-07 2015-12-15 Swagelok Company Low temperature carburization under soft vacuum
US10246766B2 (en) 2012-01-20 2019-04-02 Swagelok Company Concurrent flow of activating gas in low temperature carburization

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JP4881577B2 (en) * 2005-05-18 2012-02-22 株式会社神戸製鋼所 Vacuum carburized parts and manufacturing method thereof
JP4629064B2 (en) 2007-03-23 2011-02-09 本田技研工業株式会社 Manufacturing method of carburized parts
JP2009235443A (en) * 2008-03-26 2009-10-15 Aisin Seiki Co Ltd Method of manufacturing steel with adjusted surface carbon concentration
JP5837282B2 (en) * 2010-03-15 2015-12-24 オリエンタルエンヂニアリング株式会社 Surface modification method
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JP2963869B2 (en) * 1995-03-29 1999-10-18 株式会社日本ヘイズ Vacuum carburizing method and apparatus and carburized product
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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
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

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