JP2000104159A - Surface hardening treating method for steel - Google Patents

Surface hardening treating method for steel

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Publication number
JP2000104159A
JP2000104159A JP10275304A JP27530498A JP2000104159A JP 2000104159 A JP2000104159 A JP 2000104159A JP 10275304 A JP10275304 A JP 10275304A JP 27530498 A JP27530498 A JP 27530498A JP 2000104159 A JP2000104159 A JP 2000104159A
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JP
Japan
Prior art keywords
nitriding
treatment
hydrogen sulfide
ppm
atmosphere
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.)
Granted
Application number
JP10275304A
Other languages
Japanese (ja)
Other versions
JP2971456B1 (en
Inventor
Hitoshi Ota
均 太田
Toichi Ikeuchi
統一 池内
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
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Chugai Ro Co Ltd
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Priority to JP27530498A priority Critical patent/JP2971456B1/en
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Publication of JP2971456B1 publication Critical patent/JP2971456B1/en
Publication of JP2000104159A publication Critical patent/JP2000104159A/en
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Abstract

PROBLEM TO BE SOLVED: To activate the surface of steel by breaking a passive film on the surface of the steel, to maintain the activated state, to form a nitride layer free from unevenness and simultaneously to eliminate the complication of the equipment and the increase of the cost caused by the toxicity and corrosivity of atmospheric gas. SOLUTION: In a temp. rising stage to a nitriding treating temp. and also in a gaseous nitrogen atmosphere contg. hydrogen sulfide, steel having a passive film is heated, is subjected to sulfurizing treatment, is thereafter held under heating for a prescribed time in a nitriding atmosphere and is subjected to nitriding treatment. The concn. of hydrogen sulfide at the time of sulfurizing treatment is set to 30 to 300 ppm, and, on the other hand, the concn. of oxygen at the time of the sulfurizing treatment and the nitriding treatment is set to <=150 ppm.

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】本発明は鋼材の表面硬化処理
方法、特に、不動態被膜を有する鋼材、例えば、オース
テナイト系ステンレス鋼を含む各種ステンレス鋼等の不
動態被膜を有する鋼材に適した表面硬化処理方法に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for surface hardening a steel material, and more particularly to a method for hardening a steel material having a passive film, for example, a steel material having a passive film such as various stainless steels including austenitic stainless steel. It relates to a processing method.

【0002】[0002]

【従来の技術】従来、鋼材表面の耐摩耗性その他の機械
的性質を向上させる表面硬化処理法の一形態として、ア
ンモニアガスを含む雰囲気中で加熱して内部に窒化層を
形成する窒化処理や軟窒化処理(以下、窒化処理とい
う。)が採用されている。しかしながら、約15%以上
のクロムを含むクロム鋼やオーステナイト系ステンレス
鋼などの鋼材は、その表面がクロム酸化物層からなる不
動態被膜で覆われ、この不動態被膜によって鋼材内部へ
の窒素の侵入が阻害されるため、窒化処理が困難であっ
た。
2. Description of the Related Art Conventionally, as one form of a surface hardening treatment method for improving the wear resistance and other mechanical properties of a steel material surface, a nitriding treatment for forming a nitride layer inside by heating in an atmosphere containing ammonia gas has been known. Soft nitriding treatment (hereinafter referred to as nitriding treatment) is employed. However, steel materials such as chromium steel and austenitic stainless steel containing about 15% or more of chromium are covered on the surface with a passivation film composed of a chromium oxide layer. , The nitriding treatment was difficult.

【0003】従って、この種の鋼材を窒化処理する場
合、鋼材表面の不動態被膜を除去することが必要であ
る。これを達成する伝統的方法として、窒化に先立って
鋼材を酸洗いする方法がある。しかしながら、酸洗い法
では、鋼材の種類によっては効果があるが、酸洗い後の
表面状態を維持するのが困難であり、また、オーステナ
イト系ステンレス鋼などに適用した場合、不動態被膜が
再生されてしまうため十分な効果が得られないという問
題があった。
[0003] Therefore, when nitriding this kind of steel, it is necessary to remove the passivation film on the surface of the steel. A traditional way to achieve this is to pickle the steel prior to nitriding. However, although the pickling method is effective depending on the type of steel material, it is difficult to maintain the surface state after pickling, and when applied to austenitic stainless steel, etc., the passivation film is regenerated. Therefore, there is a problem that a sufficient effect cannot be obtained.

【0004】[0004]

【発明が解決しようとする課題】前記問題を解決する手
段としては、例えば、特公平8−9766号公報により
窒化に先立って鋼材を弗素化合物又は弗素ガスを含む雰
囲気中で加熱保持して表面層に弗化物を形成させる窒化
方法が提案されている。
As means for solving the above-mentioned problems, for example, Japanese Patent Publication No. 8-9766 discloses a method in which a steel material is heated and held in an atmosphere containing a fluorine compound or a fluorine gas prior to nitriding. There is proposed a nitriding method for forming a fluoride.

【0005】前記方法は、鋼材表面の不動態被膜を弗化
物膜に変質させ、その後の窒化処理時に前記弗化物膜を
分解させて窒化を行うため、良好な窒化処理を行うこと
ができる利点はあるが、弗化処理に使用するフッ素ガス
及びフッ化窒素ガスの許容濃度が、それぞれ1ppm、3p
pmと極めて毒性が高く、腐食性も極めて高いため設備上
種々の制約を受け、設備自体が極めて複雑で高価となる
問題がある。しかも、不動態被膜を破壊しても、窒化処
理温度(通常、500〜600℃)における窒化雰囲気
は、鋼材成分のクロム、珪素、マンガン、アルミニウム
等に対しては酸化性であるため、窒化処理中に不動態被
膜が再形成され、以後の窒素の侵入が阻害されるなど、
安定した窒化処理が困難であることが明らかとなった。
In the above method, the passivation film on the surface of the steel material is transformed into a fluoride film, and the nitride film is decomposed during the subsequent nitriding treatment to perform nitriding. However, the permissible concentrations of fluorine gas and nitrogen fluoride gas used for fluoridation are 1 ppm and 3 p, respectively.
Due to the extremely high toxicity of pm and the extremely high corrosiveness, there are various restrictions on the equipment, and the equipment itself is extremely complicated and expensive. Moreover, even if the passivation film is destroyed, the nitriding atmosphere at the nitriding temperature (usually 500 to 600 ° C.) is oxidizing to steel components such as chromium, silicon, manganese, and aluminum. The passivation film is re-formed in the inside, and the subsequent intrusion of nitrogen is inhibited.
It became clear that stable nitriding treatment was difficult.

【0006】従って、本発明は、鋼材表面の不動態被膜
を破壊して表面を活性化し、その状態を維持してムラの
ない窒化物を形成することができると同時に、雰囲気ガ
スの毒性や腐食性に起因する設備の複雑化及び高コスト
化を排除できるようにすることを課題とするものであ
る。
Accordingly, the present invention is capable of activating the surface by destroying the passive film on the surface of the steel material, forming a uniform nitride while maintaining the state, and at the same time the toxicity and corrosion of the atmosphere gas. It is an object of the present invention to eliminate the complexity and high cost of equipment caused by the nature.

【0007】[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、窒化処理温度への昇温過程
で、かつ、硫化水素を含む窒素ガス雰囲気中で不動態被
膜を有する鋼材を加熱して硫化処理した後、窒化雰囲気
中で所定時間加熱保持して窒化処理するようにしたもの
である。
According to the present invention, there is provided a steel material having a passivation film in a nitrogen gas atmosphere containing hydrogen sulfide during a process of raising a temperature to a nitriding treatment temperature. Is heated and sulfurized, and then heated and held in a nitriding atmosphere for a predetermined time to perform a nitriding treatment.

【0008】好ましい実施態様においては、前記硫化処
理は、酸素濃度が150ppm以下で、硫化水素濃度が3
0〜300ppmである窒素ガス雰囲気で行われる。ま
た、前記硫化処理は、通常、常温から窒化処理温度(通
常、500〜600℃)に達するまで1〜2時間かけて
行われるが、鋼材が350〜450℃の温度に0.5〜
1時間維持されるように行うのが好ましい。
[0008] In a preferred embodiment, the sulfurization treatment has an oxygen concentration of 150 ppm or less and a hydrogen sulfide concentration of 3 ppm.
This is performed in a nitrogen gas atmosphere of 0 to 300 ppm. In addition, the sulfurizing treatment is usually performed for 1 to 2 hours from a room temperature to a nitriding treatment temperature (normally, 500 to 600 ° C.).
It is preferable to carry out the treatment so as to be maintained for one hour.

【0009】[0009]

【発明の実施の形態】本発明に係る鋼材の表面硬化処理
方法は、バッチ式窒化炉や連続式窒化炉など任意の形態
でも実施できるが、ここでは図1に示す二室型窒化炉を
用いて実施する場合を例に挙げて説明する。
BEST MODE FOR CARRYING OUT THE INVENTION The method for surface hardening steel according to the present invention can be carried out in any form such as a batch nitriding furnace or a continuous nitriding furnace, but here, a two-chamber nitriding furnace shown in FIG. 1 is used. An example of the case will be described.

【0010】図示の二室型窒化炉は、装入室1と加熱室
2とからなり、両室は中間ドア3を介して接続され、装
入室1の一端側には装入ドア4が配設されている。前記
加熱室2は、ガス供給ライン5a及びバルブ6a、6
b、6cを介して窒素供給源7、アンモニア供給源8及
び硫化水素供給源9に接続されると共に、排気系ライン
10a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。他方、装入室1は、ガス供給ライン5b及びバ
ルブ6a'を介して窒素供給源7に接続される一方、排
気系ライン10b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。なお、加熱室2はその内部を加熱す
る加熱手段が配設されている一方、装入室1と同様に被
処理材を移行させる移送コンベア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。
The illustrated two-chamber nitriding furnace comprises a charging chamber 1 and a heating chamber 2, both chambers being connected via an intermediate door 3, and a charging door 4 at one end of the charging chamber 1. It is arranged. The heating chamber 2 includes a gas supply line 5a and valves 6a, 6
b and 6c, are connected to a nitrogen supply source 7, an ammonia supply source 8, and a hydrogen sulfide supply source 9, and are connected to a vacuum exhaust system and an exhaust gas treatment system via an exhaust system line 10a. On the other hand, the charging chamber 1 is connected to a nitrogen supply source 7 via a gas supply line 5b and a valve 6a ', while being connected to a vacuum exhaust system and an exhaust gas treatment system via an exhaust system line 10b. The heating chamber 2 is provided with a heating means for heating the inside thereof, while a transfer conveyor for transferring the material to be processed is provided similarly to the charging chamber 1,
These have the same configuration as the known ones.

【0011】前記二室型窒化炉を用いて被処理材(例え
ば、不動態被膜を有する鋼材)を窒化処理する場合、ま
ず、被処理材を装入室1に装入し、排気系ライン10
a、10bを介して装入室1及び加熱室2内をそれぞれ
真空排気した後、ガス供給ライン5a、5bより窒素ガ
スを供給し、装入室1及び加熱室2内の雰囲気を酸素濃
度150ppm以下の窒素ガス雰囲気に調整すると共に、
加熱手段で加熱室2内を昇温させて350〜450℃の
範囲内の所定温度に維持する。この状態で被処理材を加
熱室2へ移行させると共に、バルブ6bを開いて硫化水
素供給源9から加熱室2内へ硫化水素の供給を開始し、
当該雰囲気中の硫化水素濃度が30〜300ppmとなる
ように継続的に供給しながら前記範囲内の温度で所定時
間維持して硫化処理と被処理材の昇温を行う。その後、
雰囲気温度を窒化処理温度まで上昇させる。
When the material to be treated (for example, a steel material having a passivation film) is nitrided using the two-chamber type nitriding furnace, first, the material to be treated is charged into the charging chamber 1 and the exhaust system line 10 is charged.
After the inside of the charging chamber 1 and the heating chamber 2 are evacuated through the gas supply lines 5a and 5b, the atmosphere in the charging chamber 1 and the heating chamber 2 is changed to an oxygen concentration of 150 ppm. Adjust to the following nitrogen gas atmosphere,
The inside of the heating chamber 2 is heated by the heating means and maintained at a predetermined temperature in the range of 350 to 450 ° C. In this state, the material to be treated is transferred to the heating chamber 2, and the valve 6b is opened to start supplying hydrogen sulfide from the hydrogen sulfide supply source 9 into the heating chamber 2.
While the hydrogen sulfide concentration in the atmosphere is continuously supplied to be 30 to 300 ppm, the sulfurating treatment and the temperature rise of the material to be treated are performed by maintaining the temperature within the above range for a predetermined time. afterwards,
Raise the ambient temperature to the nitriding temperature.

【0012】前記昇温時、効果的には鋼材の表面温度が
350℃以上であると、雰囲気中の硫化水素が鋼材表面
の酸化物と、式1:
When the temperature is raised, if the surface temperature of the steel material is effectively 350 ° C. or more, hydrogen sulfide in the atmosphere is converted into an oxide on the surface of the steel material by the following formula:

【化1】Mexy + yH2S = Mexy + yH2O (式中、Meは金属を表す。)で表される反応を生じて
鋼材表面の酸化物が硫化物に変わる。
(In the formula, Me represents. A metal) Me x O y + yH 2 S = Me x S y + yH 2 O changed to oxides sulfides steel surface caused the reaction represented by .

【0013】前記式1の反応は正逆両方向に進行する反
応であって、反応系の温度が450℃前後までは平衡位
置が右側に偏り鋼材表面の酸化物が容易に硫化物とな
る。しかしながら、反応系の温度上昇と共に反応の平衡
がずれ、500℃を越えると式1の平衡状態が左側に偏
るようになり窒化処理温度領域では硫化水素が存在して
いても硫化物が十分に生成されないのみならず、雰囲気
中の酸素の存在により鋼材表面に生成した硫化物が酸化
物に戻ることになる。この現象は昇温時の雰囲気中の酸
素濃度が高いほど著しい。これを防止するため、本発明
においては、昇温時の雰囲気中の酸素濃度を一定値以下
に抑制し、反応系の平衡位置が右側に偏り、かつ、反応
速度的に有利な350〜450℃の範囲内の温度で十分
に鋼材表面に硫化物を生成させるようにしている。
The reaction of the above formula 1 is a reaction which proceeds in both forward and reverse directions. When the temperature of the reaction system is around 450 ° C., the equilibrium position is shifted to the right, and oxides on the surface of the steel material easily become sulfides. However, when the temperature of the reaction system rises, the equilibrium of the reaction deviates. When the temperature exceeds 500 ° C., the equilibrium state of Equation 1 shifts to the left, and sufficient sulfide is generated even in the presence of hydrogen sulfide in the nitriding temperature range. Not only that, the sulfide formed on the surface of the steel material due to the presence of oxygen in the atmosphere returns to the oxide. This phenomenon is more remarkable as the oxygen concentration in the atmosphere at the time of temperature rise is higher. In order to prevent this, in the present invention, the oxygen concentration in the atmosphere at the time of raising the temperature is suppressed to a certain value or less, the equilibrium position of the reaction system is shifted to the right, and 350 to 450 ° C. which is advantageous for the reaction rate. Sufficiently, sulfides are formed on the surface of the steel material at a temperature within the range described above.

【0014】窒化処理温度への昇温が完了した時点で、
バルブ6cを開いてアンモニア源からアンモニアガスの
供給を開始して加熱室2内の雰囲気を窒素とアンモニア
からなる窒化雰囲気に置換すると共に、当該雰囲気中の
硫化水素濃度が30〜300ppmとなるように硫化水素
を継続的に供給しながら所定時間加熱維持して窒化処理
を行う。
When the temperature increase to the nitriding temperature is completed,
The valve 6c is opened to start supplying ammonia gas from the ammonia source to replace the atmosphere in the heating chamber 2 with a nitriding atmosphere composed of nitrogen and ammonia, and to adjust the hydrogen sulfide concentration in the atmosphere to 30 to 300 ppm. The nitriding treatment is performed by heating and maintaining for a predetermined time while continuously supplying hydrogen sulfide.

【0015】この窒化処理過程では、窒化雰囲気中のア
ンモニアの一部が分解して水素を発生し、この発生した
水素の作用により昇温時に鋼材表面に生成した硫化物
が、式2:
In this nitriding process, part of the ammonia in the nitriding atmosphere is decomposed to generate hydrogen, and the sulfide generated on the surface of the steel material at the time of raising the temperature by the action of the generated hydrogen is represented by the following formula 2:

【化2】Mexy + yH2 = xMe + yH2S で表される反応により活性な金属に還元されて鋼材表面
の不動態被膜(酸化物)が破壊されると同時に、アンモ
ニアの分解により生ずる発生期窒素の材料への侵入が容
易となり、窒化物を形成しながら鋼材表面から内部へ順
次拡散していく。この場合、硫黄は原子径が大きいため
鋼材表層の2〜10μmに硫化物を形成しているが、窒
素は原子径が小さいため鋼材内部の比較的深い部分まで
侵入して窒化物を形成する。
## STR2 ## Me x S y + yH 2 = xMe + yH 2 passivation film (oxide) in the reaction is reduced to the active metal of steel surfaces represented by S when is broken at the same time, decomposition of ammonia As a result, the nascent nitrogen generated by the gas can easily penetrate into the material, and is gradually diffused from the steel material surface to the inside while forming nitride. In this case, since sulfur has a large atomic diameter, sulfide is formed in the surface layer of the steel material at 2 to 10 μm, whereas nitrogen has a small atomic diameter and penetrates to a relatively deep portion inside the steel material to form nitride.

【0016】また、窒化処理中においても、式1の硫化
水素による酸化物の硫化及び式2による水素による硫化
物の還元が起こる。しかしながら、窒化雰囲気中の酸素
濃度が高い場合、還元された金属、即ち、還元金属は、
式3:
Further, even during the nitriding treatment, sulfuration of the oxide by the hydrogen sulfide of the formula 1 and reduction of the sulfide by the hydrogen of the formula 2 occur. However, when the oxygen concentration in the nitriding atmosphere is high, the reduced metal, that is, the reduced metal,
Equation 3:

【化3】(Me)x + (1/2O2)y = (Me)xy で表される反応によって再酸化されて不動態被膜が再生
され、以後の窒化が阻害される。この還元金属の再酸化
の問題は、雰囲気中の酸素濃度に応じて硫化水素濃度を
高くすることによって解決し得るが、硫化水素濃度の増
大によって高濃度の硫化物層が鋼材表面に形成され、か
えって窒化が阻害される。このような問題を防止するた
め、本発明においては、酸素濃度を150ppm以下に維
持し、高濃度の硫化物が鋼材表面に形成されるのを防止
している。
## STR3 ## By the reaction represented by (Me) x + (1/2 O 2 ) y = (Me) x O y , the oxide film is reoxidized to regenerate the passive film, thereby inhibiting the subsequent nitridation. The problem of reoxidation of the reduced metal can be solved by increasing the concentration of hydrogen sulfide according to the oxygen concentration in the atmosphere.However, the increased concentration of hydrogen sulfide causes a high-concentration sulfide layer to be formed on the steel material surface, On the contrary, nitriding is inhibited. In order to prevent such a problem, in the present invention, the oxygen concentration is maintained at 150 ppm or less to prevent a high concentration of sulfide from being formed on the surface of the steel material.

【0017】更に、窒化雰囲気中でも酸化物の硫化と硫
化物の還元を持続させる為には、昇温時だけでなく窒化
処理時にも適正量の硫化水素が存在する必要がある。従
って、窒化処理サイクル全体を通じて窒化雰囲気中の硫
化水素濃度が30〜300ppmとなるように硫化水素を
添加するのが望ましい。しかしながら、昇温時に鋼材表
面が十分に硫化されていれば、窒化処理時に鋼材や治具
及び炉材表面に形成されている硫化物が窒化雰囲気中の
水素と反応して硫化水素を生成して窒化雰囲気中の硫化
水素濃度が30〜300ppmとなるため、窒化処理時に
硫化水素を添加しなくても窒化を行うことができる。昇
温時に十分な硫化物を形成させるためには、昇温時の硫
化処理を350〜450℃、好ましくは、350〜40
0℃で0.5〜1時間行うのが好適である。
Furthermore, in order to maintain the sulfurization of oxides and the reduction of sulfides even in a nitriding atmosphere, an appropriate amount of hydrogen sulfide needs to be present not only at the time of temperature rise but also at the time of nitriding treatment. Therefore, it is desirable to add hydrogen sulfide so that the concentration of hydrogen sulfide in the nitriding atmosphere is 30 to 300 ppm throughout the entire nitriding cycle. However, if the surface of the steel material is sufficiently sulfided at the time of heating, the sulfide formed on the surface of the steel material, the jig and the furnace material during the nitriding treatment reacts with the hydrogen in the nitriding atmosphere to generate hydrogen sulfide. Since the concentration of hydrogen sulfide in the nitriding atmosphere is 30 to 300 ppm, nitriding can be performed without adding hydrogen sulfide during the nitriding treatment. In order to form a sufficient sulfide at the time of raising the temperature, the sulfidation treatment at the time of raising the temperature is performed at 350 to 450 ° C., preferably 350 to 40 ° C.
It is preferable to carry out at 0 ° C. for 0.5 to 1 hour.

【0018】前記硫化処理時及び窒化処理時の硫化水素
濃度は、30〜300ppmに設定されるが、これは硫化
水素濃度が30ppm未満では、鋼材表面に均一な硫化物
が形成されず、また、硫化水素濃度が300ppmを越え
ると、鋼材表面に高濃度の硫化物が形成され、表面が黒
色化し剥離し易くなると共に、鋼材内部への窒素の侵入
が阻害され窒化処理が困難となるからである。
The hydrogen sulfide concentration during the sulfurizing treatment and the nitriding treatment is set to 30 to 300 ppm. If the hydrogen sulfide concentration is less than 30 ppm, uniform sulfide is not formed on the steel material surface. If the concentration of hydrogen sulfide exceeds 300 ppm, a high concentration of sulfide is formed on the surface of the steel material, the surface becomes black and easily peels off, and the intrusion of nitrogen into the steel material is inhibited, and the nitriding treatment becomes difficult. .

【0019】このようにして硫化処理及び窒化処理を行
った後、バルブ6b,6cを閉じて硫化水素及びアンモ
ニアの供給を停止し、次いで、中間ドア3を開いて被処
理材を加熱室2から装入室1に移行させる。なお、装入
室1への移行は、加熱室2を真空排気した後、窒素雰囲
気に復圧してから行うようにしてよい。その後、中間ド
ア3を閉じて装入室1の窒素ガス雰囲気中でガス冷却す
ることにより被処理材の窒化処理が終わる。
After the sulfuration treatment and the nitridation treatment are performed in this manner, the valves 6b and 6c are closed to stop the supply of hydrogen sulfide and ammonia, and then the intermediate door 3 is opened to remove the workpiece from the heating chamber 2. Transfer to charging room 1. The transfer to the charging chamber 1 may be performed after the heating chamber 2 is evacuated and then restored to a nitrogen atmosphere. Thereafter, the intermediate door 3 is closed and gas cooling is performed in the nitrogen gas atmosphere in the charging chamber 1 to complete the nitriding of the workpiece.

【0020】なお、前記説明では、窒化処理の窒素供給
源としてアンモニアと窒素ガスとの混合ガスを採用した
場合を例に挙げたが、必ずしもアンモニアと窒素ガスと
の混合ガスに限定されるものではなく、アンモニア単体
或いはアンモニアと吸熱型ガスとの混合ガスからなるガ
ス雰囲気を使用しても良い。
In the above description, the case where a mixed gas of ammonia and nitrogen gas is employed as the nitrogen supply source for the nitriding treatment is described as an example. However, the present invention is not necessarily limited to the mixed gas of ammonia and nitrogen gas. Instead, a gas atmosphere consisting of ammonia alone or a mixed gas of ammonia and an endothermic gas may be used.

【0021】以下、本発明の実施例について説明する。Hereinafter, embodiments of the present invention will be described.

【0022】[0022]

【実施例1】図1に示す二室型窒化炉を用い、被処理材
を装入室1に装入し、装入室1及び加熱室2内の雰囲気
を酸素濃度が約50ppmの窒素ガス雰囲気に調整すると
共に、前記加熱室2内を約400℃に維持する。この状
態で、被処理材を加熱室2へ移行させると共に、加熱室
2内への硫化水素の供給を開始して当該雰囲気中の硫化
水素濃度が100ppmとなるように硫化水素を継続的に
供給しながら約350℃で30分間維持して硫化処理す
る。その後、約30分かけて窒化処理温度(約570℃)
まで昇温する。この昇温が完了した時点で加熱室2内の
雰囲気をアンモニアガスからなる窒化雰囲気に置換する
と共に、当該雰囲気中の硫化水素濃度が130ppmにな
るように硫化水素を継続的に供給しながら3.5時間加
熱保持して窒化処理する。なお、この窒化処理時におい
ても、酸素濃度は約50ppmに維持される。前記時間経
過後、被処理材を装入室1に移行させ、窒素ガス雰囲気
中でガス冷却して試料を得た。なお、被処理材として
は、SUS304製パイプ(100mmφ×3mmφ×10
0mm)並びにSUS304、SUS410、S45C製
の丸棒(直径30mmφ×100mm)を使用した。
Embodiment 1 Using a two-chamber nitriding furnace shown in FIG. 1, a material to be treated is charged into a charging chamber 1, and the atmosphere in the charging chamber 1 and the heating chamber 2 is changed to a nitrogen gas having an oxygen concentration of about 50 ppm. The atmosphere is adjusted and the inside of the heating chamber 2 is maintained at about 400 ° C. In this state, the material to be processed is transferred to the heating chamber 2 and the supply of hydrogen sulfide into the heating chamber 2 is started to continuously supply hydrogen sulfide so that the concentration of hydrogen sulfide in the atmosphere becomes 100 ppm. While maintaining the temperature at about 350 ° C. for 30 minutes, the sulfurating treatment is performed. Then, it takes about 30 minutes for nitriding temperature (about 570 ° C)
Heat up to 2. When the temperature increase is completed, the atmosphere in the heating chamber 2 is replaced with a nitriding atmosphere composed of ammonia gas, and hydrogen sulfide is continuously supplied so that the hydrogen sulfide concentration in the atmosphere becomes 130 ppm. Heating and holding for 5 hours are performed for nitriding. Note that the oxygen concentration is maintained at about 50 ppm even during this nitriding treatment. After the elapse of the time, the material to be treated was transferred to the charging chamber 1 and gas-cooled in a nitrogen gas atmosphere to obtain a sample. The material to be treated is a SUS304 pipe (100 mmφ × 3 mmφ × 10 mm).
0 mm) and SUS304, SUS410 and S45C round bars (diameter 30 mmφ × 100 mm).

【0023】[0023]

【実施例2】実施例1において、硫化処理時及び窒化処
理時における雰囲気中の酸素濃度をそれぞれ150ppm
に変更した以外は実施例1と同様にして硫化処理及び窒
化処理を行い、試料を得た。
Example 2 In Example 1, the oxygen concentration in the atmosphere during the sulfurizing treatment and the nitriding treatment was set to 150 ppm, respectively.
Except that the sulfuration treatment and the nitridation treatment were performed in the same manner as in Example 1 to obtain a sample.

【0024】[0024]

【比較例1】実施例1において、硫化処理時及び窒化処
理時における雰囲気中の酸素濃度をそれぞれ260ppm
に変更した以外は実施例1と同様にして硫化処理及び窒
化処理を行い、試料を得た。
[Comparative Example 1] In Example 1, the oxygen concentration in the atmosphere during the sulfurizing treatment and the nitriding treatment was 260 ppm, respectively.
Except that the sulfuration treatment and the nitridation treatment were performed in the same manner as in Example 1 to obtain a sample.

【0025】[0025]

【比較例2】実施例1において、硫化処理時及び窒化処
理時における雰囲気中の酸素濃度をそれぞれ750ppm
に変更した以外は実施例1と同様にして硫化処理及び窒
化処理を行い、試料を得た。
Comparative Example 2 In Example 1, the oxygen concentration in the atmosphere at the time of the sulfurizing treatment and the nitriding treatment was 750 ppm, respectively.
Except that the sulfuration treatment and the nitridation treatment were performed in the same manner as in Example 1 to obtain a sample.

【0026】実施例1及び2並びに比較例1及び2で得
た各試料について窒化物層の厚さを測定した。その結果
を表1に示す。表中、研磨面とはパイプの表面を研磨加
工した面、圧延面とは圧延のままの丸棒の表面を、切断
面とは丸棒を切断加工した面をそれぞれ意味する。
The thickness of the nitride layer was measured for each of the samples obtained in Examples 1 and 2 and Comparative Examples 1 and 2. Table 1 shows the results. In the table, the polished surface means the surface obtained by polishing the surface of the pipe, the rolled surface means the surface of the as-rolled round bar, and the cut surface means the surface obtained by cutting the round bar.

【0027】[0027]

【表1】 [Table 1]

【0028】表1に示す結果から、硫化水素濃度及び硫
化処理温度が所定条件下では、硫化処理時及び窒化処理
時の各雰囲気中の酸素濃度が窒化物層を形成する上での
要因となることが解る。即ち、酸素濃度が150ppm以
下ではステンレス鋼(SUS304及びSUS410)
からなる鋼材を窒化することができるが、比較例1及び
比較例2に示すように、酸素濃度が150ppmを越える
場合にはステンレス鋼からなる鋼材を窒化することがで
きない。なお、前記窒化物層の表層には数ミクロンの硫
化物層が認められた。
From the results shown in Table 1, when the concentration of hydrogen sulfide and the temperature of the sulfurizing treatment are predetermined, the oxygen concentration in each atmosphere during the sulfurizing treatment and the nitriding treatment is a factor in forming the nitride layer. I understand. That is, when the oxygen concentration is 150 ppm or less, stainless steel (SUS304 and SUS410)
Can be nitrided, but as shown in Comparative Examples 1 and 2, when the oxygen concentration exceeds 150 ppm, the stainless steel cannot be nitrided. Note that a sulfide layer of several microns was observed on the surface of the nitride layer.

【0029】[0029]

【実施例3】実施例1において、硫化処理時及び窒化処
理時の酸素濃度をそれぞれ100ppmとし、硫化処理時
の維持温度を450℃にした以外は、実施例1と同様に
して硫化処理及び窒化処理を行い、試料を得た。
Example 3 In Example 1, the sulfurating treatment and nitriding were performed in the same manner as in Example 1 except that the oxygen concentration during the sulfurizing treatment and the nitriding treatment were each set to 100 ppm, and the maintenance temperature during the sulfurizing treatment was 450 ° C. Processing was performed to obtain a sample.

【0030】[0030]

【比較例3】実施例1において、硫化処理時及び窒化処
理時の酸素濃度をそれぞれ100ppmとし、硫化処理時
の維持温度を500℃にした以外は、実施例1と同様に
して硫化処理及び窒化処理を行い、試料を得た。
Comparative Example 3 Sulfidation and nitriding were carried out in the same manner as in Example 1 except that the oxygen concentration during the sulfidation treatment and the nitridation treatment were each 100 ppm, and the maintenance temperature during the sulfurization treatment was 500 ° C. Processing was performed to obtain a sample.

【0031】[0031]

【比較例4】実施例1において、硫化処理時及び窒化処
理時の酸素濃度をそれぞれ100ppmとし、硫化処理時
の維持温度を550℃にした以外は、実施例1と同様に
して硫化処理及び窒化処理を行い、試料を得た。
Comparative Example 4 Sulfidation treatment and nitridation were carried out in the same manner as in Example 1 except that the oxygen concentration during the sulfurization treatment and the nitridation treatment were each set to 100 ppm, and the maintenance temperature during the sulfurization treatment was set to 550 ° C. Processing was performed to obtain a sample.

【0032】得られた各試料について表面状態を観察す
る一方、窒化物層の厚さを測定した。その結果を表2に
示す。
While observing the surface condition of each of the obtained samples, the thickness of the nitride layer was measured. Table 2 shows the results.

【0033】[0033]

【表2】 [Table 2]

【0034】表2に示す結果から、硫化水素濃度及び酸
素濃度が所定条件下では、硫化処理温度が窒化物層を形
成する上での要因となることが解る。即ち、硫化処理温
度が350〜450℃の範囲内では、ほぼ均一な窒化物
層を形成することできるが、比較例3及び比較例4に示
すように、硫化処理温度が450℃を越える場合には不
均一な窒化物層が形成される。
From the results shown in Table 2, it can be seen that under a predetermined condition of the concentration of hydrogen sulfide and the concentration of oxygen, the sulfidation temperature is a factor in forming a nitride layer. That is, when the sulfidation temperature is in the range of 350 to 450 ° C., a substantially uniform nitride layer can be formed. However, as shown in Comparative Examples 3 and 4, when the sulfidation temperature exceeds 450 ° C. A non-uniform nitride layer is formed.

【0035】[0035]

【実施例4】酸素濃度が50ppmの窒素ガス雰囲気中で
硫化水素を当該窒素ガス雰囲気中の硫化水素濃度が13
0ppmとなるように添加しながら約350℃で30分間
維持して硫化処理を行った後、酸素濃度が50ppmで、
かつ、窒素ガス(40体積%)とアンモニアガス(60
体積%)からなる窒化雰囲気中に硫化水素を当該窒化雰
囲気中の硫化水素濃度が130ppmとなるように添加し
ながら窒化処理温度(約570℃)に3.5時間加熱維
持して窒化処理し、その後、窒素ガス雰囲気中でガス冷
却し、試料を得た。
Embodiment 4 In a nitrogen gas atmosphere having an oxygen concentration of 50 ppm, hydrogen sulfide was changed to a hydrogen sulfide concentration of 13 ppm in the nitrogen gas atmosphere.
After performing sulfurization treatment at about 350 ° C. for 30 minutes while adding so that the concentration becomes 0 ppm, the oxygen concentration is 50 ppm,
In addition, nitrogen gas (40% by volume) and ammonia gas (60
% By volume) while maintaining the nitriding temperature (about 570 ° C.) for 3.5 hours while adding hydrogen sulfide so that the hydrogen sulfide concentration in the nitriding atmosphere becomes 130 ppm. Thereafter, the sample was cooled in a nitrogen gas atmosphere to obtain a sample.

【0036】[0036]

【実施例5】実施例4において、窒化処理時に硫化水素
を添加しない以外は、実施例4と同様に硫化処理及び窒
化処理を行い、試料を得た。
Example 5 In Example 4, except that hydrogen sulfide was not added at the time of nitriding, a sulfurating treatment and a nitriding treatment were performed in the same manner as in Example 4 to obtain a sample.

【0037】得られた試料について窒化物層の厚さを測
定した。その結果を表3に示す。
The thickness of the nitride layer of the obtained sample was measured. Table 3 shows the results.

【0038】[0038]

【表3】 [Table 3]

【0039】表3に示す結果から、窒化処理時に硫化水
素を窒化雰囲気中に添加しなくても、硫化処理及び窒化
処理のサイクル全体を通じて硫化水素を添加した実施例
4のものとほぼ同等の結果が得られることが解る。な
お、窒化処理時の排ガスからは硫化水素が検出された
が、これは昇温時に形成された硫化物がアンモニアの分
解により生じた水素と反応して生成されたものと考えら
れる。
From the results shown in Table 3, it can be seen that even when hydrogen sulfide was not added to the nitriding atmosphere during the nitriding treatment, the result was almost the same as that of Example 4 in which hydrogen sulfide was added throughout the entire cycle of the sulfurizing treatment and the nitriding treatment. Is obtained. Although hydrogen sulfide was detected from the exhaust gas during the nitriding treatment, it is considered that this was generated by the reaction of the sulfide formed during the temperature rise with the hydrogen generated by the decomposition of ammonia.

【0040】[0040]

【実施例6】実施例4において、硫化処理時及び窒化処
理時における雰囲気中の硫化水素濃度を300ppmに変
更した以外は、実施例4と同様にして硫化処理及び窒化
処理を行い、試料を得た。
Embodiment 6 A sulfuration treatment and a nitridation treatment were carried out in the same manner as in the embodiment 4 except that the concentration of hydrogen sulfide in the atmosphere during the sulfuration treatment and the nitridation treatment was changed to 300 ppm. Was.

【0041】[0041]

【比較例5】実施例4において、窒化処理温度への昇温
時に硫化水素が存在しない窒素ガスを用いた以外は、実
施例4と同様にして窒化処理を行い、試料を得た。
Comparative Example 5 A sample was obtained in the same manner as in Example 4 except that a nitrogen gas containing no hydrogen sulfide was used when the temperature was raised to the nitriding temperature.

【0042】[0042]

【比較例6】実施例4において、窒化処理温度への昇温
時に硫化水素が存在しない窒素ガス雰囲気を用いる一
方、窒化処理時に硫化水素が存在しないアンモニアガス
雰囲気を用いた以外は、実施例4と同様にして窒化処理
を行い、試料を得た。
Comparative Example 6 Example 4 was repeated except that a nitrogen gas atmosphere without hydrogen sulfide was used when the temperature was raised to the nitriding temperature, while an ammonia gas atmosphere without hydrogen sulfide was used during the nitriding process. A nitriding treatment was performed in the same manner as described above to obtain a sample.

【0043】実施例6、比較例5及び比較例6でそれぞ
れ得られた各試料について窒化物層の厚さを測定した。
その結果を表4に示す。
The thickness of the nitride layer was measured for each of the samples obtained in Example 6, Comparative Example 5, and Comparative Example 6.
Table 4 shows the results.

【0044】[0044]

【表4】 [Table 4]

【0045】表4に示す結果から、窒化処理温度への昇
温時に硫化水素が存在しない比較例5並びに昇温時及び
窒化処理時に硫化水素が存在しない比較例6の試料で
は、殆ど窒化物層が形成されていないことが判る。
From the results shown in Table 4, the samples of Comparative Example 5 in which no hydrogen sulfide was present at the time of raising the temperature to the nitriding temperature and Comparative Example 6 in which no hydrogen sulfide was present at the time of raising the temperature and the nitriding were almost completely nitrided. It can be seen that no is formed.

【0046】[0046]

【発明の効果】以上の説明から明らかなように、本発明
によれば、従来法では窒化し難いオーステナイト系ステ
ンレス鋼などの鋼材の不動態被膜を確実に破壊して表面
を活性化し、均一な窒化物層を形成することができる。
また、鋼種を問わず、低合金鋼の機械加工時の焼き付き
などに起因する窒化ムラを防止できる。また、鋼材表面
の不動態被膜を除去するのに使用する硫化水素は、許容
濃度が10ppmとフッ化窒素の許容濃度3ppmやフッ素の
許容濃度1ppmに比べて高いため、設備上の制約が緩和
され、設備を単純化することができる。さらに、窒化処
理温度程度の温度域で比較すると、炉材の耐食性もフッ
素系ガスよりも硫化水素の方が極めて有利となり製造コ
ストを低減することができる、など優れた効果が得られ
る。
As is apparent from the above description, according to the present invention, the passive film of steel, such as austenitic stainless steel, which is hardly nitrided by the conventional method, is surely destroyed to activate the surface and to form a uniform surface. A nitride layer can be formed.
Also, regardless of the type of steel, it is possible to prevent non-uniformity in nitriding due to seizure during machining of low alloy steel. In addition, hydrogen sulfide used to remove the passive film on the steel surface has an allowable concentration of 10 ppm, which is higher than the allowable concentration of nitrogen fluoride, 3 ppm, and the allowable concentration of fluorine, 1 ppm. , The equipment can be simplified. Furthermore, when compared in a temperature range around the nitriding temperature, excellent effects are obtained, such as hydrogen sulfide being extremely advantageous in terms of the corrosion resistance of the furnace material as compared with the fluorine-based gas, and the production cost can be reduced.

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

【図1】 本発明方法の実施に使用する窒化処理装置の
一例を示す説明図。
FIG. 1 is an explanatory view showing an example of a nitriding apparatus used for carrying out the method of the present invention.

【符号の説明】[Explanation of symbols]

1…装入室 2…加熱室 3…中間ドア 4…装入ドア 5…ガス供給ライン 6a、6b、6c、6a'…バルブ 7…窒素供給源 8…アンモニア供給源 9…硫化水素供給源 10a、10b…排気系ライン DESCRIPTION OF SYMBOLS 1 ... Loading room 2 ... Heating room 3 ... Intermediate door 4 ... Loading door 5 ... Gas supply line 6a, 6b, 6c, 6a '... Valve 7 ... Nitrogen supply source 8 ... Ammonia supply source 9 ... Hydrogen sulfide supply source 10a , 10b… Exhaust system line

─────────────────────────────────────────────────────
────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成11年7月14日(1999.7.1
4)
[Submission date] July 14, 1999 (1999.7.1)
4)

【手続補正1】[Procedure amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】特許請求の範囲[Correction target item name] Claims

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【特許請求の範囲】[Claims]

【手続補正2】[Procedure amendment 2]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0007[Correction target item name] 0007

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0007】[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、窒化処理温度への昇温過程時
に、酸素濃度150ppm以下で、かつ、硫化水素濃度3
0〜300ppmを含む窒素ガス雰囲気中で不動態被膜を
有する鋼材を350〜450℃の温度域で加熱して硫化
処理した後、窒化雰囲気中で所定時間加熱保持して窒化
処理するようにしたものである。
According to the present invention, as a means for solving the above-mentioned problems, an oxygen concentration of 150 ppm or less and a hydrogen sulfide concentration of 3
A steel material having a passivation film in a nitrogen gas atmosphere containing 0 to 300 ppm is heated in a temperature range of 350 to 450 ° C. to perform a sulfurating treatment, and then is heated and held in a nitriding atmosphere for a predetermined time to perform a nitriding treatment. It is.

【手続補正3】[Procedure amendment 3]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0008[Correction target item name] 0008

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0008】好ましい実施態様においては、前記硫化処
理は、酸素濃度が150ppm以下、硫化水素濃度が30
〜300ppmである窒素ガス雰囲気中、通常、常温から
窒化処理温度(通常、500〜600℃)に達するまで
1〜2時間かけて行われるが、鋼材が350〜450℃
の温度に0.5〜1時間維持されるように行われる。
In a preferred embodiment, the sulfurization treatment has an oxygen concentration of 150 ppm or less and a hydrogen sulfide concentration of 30 ppm or less.
In a nitrogen gas atmosphere of up to 300 ppm, it is usually carried out for 1 to 2 hours from room temperature to a nitriding treatment temperature (normally 500 to 600 ° C.).
At a temperature of 0.5 to 1 hour.

【手続補正4】[Procedure amendment 4]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0011[Correction target item name] 0011

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0011】前記二室型窒化炉を用いて被処理材(例え
ば、不動態被膜を有する鋼材)を窒化処理する場合、ま
ず、被処理材を装入室1に装入し、排気系ライン10
a、10bを介して装入室1及び加熱室2内をそれぞれ
真空排気した後、ガス供給ライン5a、5bより窒素ガ
スを供給し、装入室1及び加熱室2内の雰囲気を酸素濃
度150ppm以下の窒素ガス雰囲気に調整すると共に、
加熱手段で加熱室2内を昇温させて350〜450℃の
範囲内の所定温度に維持する。この状態で被処理材を加
熱室2へ移行させると共に、バルブ6cを開いて硫化水
素供給源9から加熱室2内へ硫化水素の供給を開始し、
当該雰囲気中の硫化水素濃度が30〜300ppmとなる
ように継続的に供給しながら前記範囲内の温度で所定時
間維持して硫化処理と被処理材の昇温を行う。その後、
雰囲気温度を窒化処理温度まで上昇させる。
When the material to be treated (for example, a steel material having a passivation film) is nitrided using the two-chamber type nitriding furnace, first, the material to be treated is charged into the charging chamber 1 and the exhaust system line 10 is charged.
After the inside of the charging chamber 1 and the heating chamber 2 are evacuated through the gas supply lines 5a and 5b, the atmosphere in the charging chamber 1 and the heating chamber 2 is changed to an oxygen concentration of 150 ppm. Adjust to the following nitrogen gas atmosphere,
The inside of the heating chamber 2 is heated by the heating means and maintained at a predetermined temperature in the range of 350 to 450 ° C. In this state, the material to be treated is transferred to the heating chamber 2, and the valve 6c is opened to start supplying hydrogen sulfide from the hydrogen sulfide supply source 9 into the heating chamber 2.
While the hydrogen sulfide concentration in the atmosphere is continuously supplied to be 30 to 300 ppm, the sulfurating treatment and the temperature rise of the material to be treated are performed by maintaining the temperature within the above range for a predetermined time. afterwards,
Raise the ambient temperature to the nitriding temperature.

【手続補正5】[Procedure amendment 5]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0014[Correction target item name] 0014

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0014】窒化処理温度への昇温が完了した時点で、
バルブ6bを開いてアンモニア源からアンモニアガスの
供給を開始して加熱室2内の雰囲気を窒素とアンモニア
からなる窒化雰囲気に置換すると共に、当該雰囲気中の
硫化水素濃度が30〜300ppmとなるように硫化水素
を継続的に供給しながら所定時間加熱維持して窒化処理
を行う。
When the temperature increase to the nitriding temperature is completed,
The valve 6b is opened to start supplying ammonia gas from the ammonia source to replace the atmosphere in the heating chamber 2 with a nitriding atmosphere composed of nitrogen and ammonia, and to adjust the hydrogen sulfide concentration in the atmosphere to 30 to 300 ppm. The nitriding treatment is performed by heating and maintaining for a predetermined time while continuously supplying hydrogen sulfide.

【手続補正6】[Procedure amendment 6]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0022[Correction target item name] 0022

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0022】[0022]

【実施例1】図1に示す二室型窒化炉を用い、被処理材
を装入室1に装入し、装入室1及び加熱室2内の雰囲気
を酸素濃度が約50ppmの窒素ガス雰囲気に調整すると
共に、前記加熱室2内を約400℃に維持する。この状
態で、被処理材を加熱室2へ移行させると共に、加熱室
2内への硫化水素の供給を開始して当該雰囲気中の硫化
水素濃度が100ppmとなるように硫化水素を継続的に
供給しながら約350℃で30分間維持して硫化処理す
る。その後、約30分かけて窒化処理温度(約570℃)
まで昇温する。この昇温が完了した時点で加熱室2内の
雰囲気をアンモニアガスからなる窒化雰囲気に置換する
と共に、当該雰囲気中の硫化水素濃度が130ppmにな
るように硫化水素を継続的に供給しながら3.5時間加
熱保持して窒化処理する。なお、この窒化処理時におい
ても、酸素濃度は約50ppmに維持される。前記時間経
過後、被処理材を装入室1に移行させ、窒素ガス雰囲気
中でガス冷却して試料を得た。なお、被処理材として
は、SUS304製パイプ(100mmφ×3mmφ×10
0mm)並びにSUS304、SUS410製の丸棒(直
径30mmφ×100mm)を使用した。
Embodiment 1 Using a two-chamber nitriding furnace shown in FIG. 1, a material to be treated is charged into a charging chamber 1, and the atmosphere in the charging chamber 1 and the heating chamber 2 is changed to a nitrogen gas having an oxygen concentration of about 50 ppm. The atmosphere is adjusted and the inside of the heating chamber 2 is maintained at about 400 ° C. In this state, the material to be processed is transferred to the heating chamber 2 and the supply of hydrogen sulfide into the heating chamber 2 is started to continuously supply hydrogen sulfide so that the concentration of hydrogen sulfide in the atmosphere becomes 100 ppm. While maintaining the temperature at about 350 ° C. for 30 minutes, the sulfurating treatment is performed. Then, it takes about 30 minutes for nitriding temperature (about 570 ° C)
Heat up to 2. When the heating is completed, the atmosphere in the heating chamber 2 is replaced with a nitriding atmosphere made of ammonia gas, and hydrogen sulfide is continuously supplied so that the concentration of hydrogen sulfide in the atmosphere becomes 130 ppm. Heating and holding for 5 hours are performed for nitriding. The oxygen concentration is maintained at about 50 ppm during the nitriding process. After the elapse of the time, the material to be processed was transferred to the charging chamber 1 and gas-cooled in a nitrogen gas atmosphere to obtain a sample. The material to be treated is a SUS304 pipe (100 mmφ × 3 mmφ × 10 mm).
0 mm) and SUS304 and SUS410 round bars (diameter 30 mmφ × 100 mm).

【手続補正7】[Procedure amendment 7]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0027[Correction target item name] 0027

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0027】[0027]

【表1】 [Table 1]

【手続補正8】[Procedure amendment 8]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0033[Correction target item name] 0033

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0033】[0033]

【表2】 [Table 2]

【手続補正9】[Procedure amendment 9]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0038[Correction target item name] 0038

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0038】[0038]

【表3】 [Table 3]

【手続補正10】[Procedure amendment 10]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0044[Correction target item name] 0044

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0044】[0044]

【表4】 [Table 4]

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 窒化処理温度への昇温過程で、かつ、硫
化水素を含む窒素ガス雰囲気中で不動態被膜を有する鋼
材を加熱して硫化処理した後、窒化雰囲気中で所定時間
加熱保持して窒化処理することを特徴とする鋼材の表面
硬化処理方法。
1. A steel material having a passivation film is heated and nitrided in a nitrogen gas atmosphere containing hydrogen sulfide during a process of raising the temperature to a nitriding temperature, and then heated and held in a nitriding atmosphere for a predetermined time. A surface hardening treatment method for a steel material, characterized by performing a nitriding treatment by a nitriding treatment.
【請求項2】 前記硫化処理を行う窒素ガス雰囲気が酸
素濃度150ppm以下で、硫化水素濃度30〜300ppm
であることを特徴とする請求項1に記載の方法。
2. The method according to claim 1, wherein the nitrogen gas atmosphere for performing the sulfidation treatment has an oxygen concentration of 150 ppm or less and a hydrogen sulfide concentration of 30 to 300 ppm.
The method of claim 1, wherein
【請求項3】 前記鋼材を350〜450℃の温度域で
0.5〜1時間加熱して硫化処理を行うことを特徴とす
る請求項1又は2に記載の方法。
3. The method according to claim 1, wherein the steel material is heated in a temperature range of 350 to 450 ° C. for 0.5 to 1 hour to perform a sulfurating treatment.
JP27530498A 1998-09-29 1998-09-29 Surface hardening method for steel Expired - Fee Related JP2971456B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27530498A JP2971456B1 (en) 1998-09-29 1998-09-29 Surface hardening method for steel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27530498A JP2971456B1 (en) 1998-09-29 1998-09-29 Surface hardening method for steel

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Publication Number Publication Date
JP2971456B1 JP2971456B1 (en) 1999-11-08
JP2000104159A true JP2000104159A (en) 2000-04-11

Family

ID=17553580

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27530498A Expired - Fee Related JP2971456B1 (en) 1998-09-29 1998-09-29 Surface hardening method for steel

Country Status (1)

Country Link
JP (1) JP2971456B1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004029320A1 (en) * 2002-09-24 2004-04-08 Honda Giken Kogyo Kabushiki Kaisha Method of nitriding metal ring and apparatus therefor
JP2016188417A (en) * 2015-03-30 2016-11-04 新日鐵住金ステンレス株式会社 Austenite stainless steel and manufacturing method thereof
JP2020070892A (en) * 2018-11-01 2020-05-07 国立研究開発法人物質・材料研究機構 Manufacturing method of container, manufacturing method of hydrogen sulfide housing body, and charging method of hydrogen sulfide

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004029320A1 (en) * 2002-09-24 2004-04-08 Honda Giken Kogyo Kabushiki Kaisha Method of nitriding metal ring and apparatus therefor
JP2016188417A (en) * 2015-03-30 2016-11-04 新日鐵住金ステンレス株式会社 Austenite stainless steel and manufacturing method thereof
JP2020070892A (en) * 2018-11-01 2020-05-07 国立研究開発法人物質・材料研究機構 Manufacturing method of container, manufacturing method of hydrogen sulfide housing body, and charging method of hydrogen sulfide
JP7117000B2 (en) 2018-11-01 2022-08-12 国立研究開発法人物質・材料研究機構 Method for manufacturing container, method for manufacturing hydrogen sulfide container, and method for filling hydrogen sulfide

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