JP2001240954A - Vacuum carburizing method, and carburizing furnace therefor - Google Patents

Vacuum carburizing method, and carburizing furnace therefor

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Publication number
JP2001240954A
JP2001240954A JP2000056594A JP2000056594A JP2001240954A JP 2001240954 A JP2001240954 A JP 2001240954A JP 2000056594 A JP2000056594 A JP 2000056594A JP 2000056594 A JP2000056594 A JP 2000056594A JP 2001240954 A JP2001240954 A JP 2001240954A
Authority
JP
Japan
Prior art keywords
gas
carburizing
vacuum
chamber
ethylene
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
JP2000056594A
Other languages
Japanese (ja)
Other versions
JP3321732B2 (en
Inventor
Kazuyoshi Yamaguchi
和嘉 山口
Haruhiro Kurata
晴弘 倉田
Shu Matsubara
周 松原
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.)
JTEKT Thermo Systems Corp
Original Assignee
Koyo Thermo Systems Co Ltd
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Filing date
Publication date
Application filed by Koyo Thermo Systems Co Ltd filed Critical Koyo Thermo Systems Co Ltd
Priority to JP2000056594A priority Critical patent/JP3321732B2/en
Publication of JP2001240954A publication Critical patent/JP2001240954A/en
Application granted granted Critical
Publication of JP3321732B2 publication Critical patent/JP3321732B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Furnace Details (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a carburizing furnace to implement a carburizing method in which the number of ethylene molecules in a carburizing chamber is substantially nonincreased from the beginning to the terminating period of carburization when ethylene and hydrogen are used as the vacuum carburizing gas. SOLUTION: The vacuum carburizing furnace comprises a carburizing chamber 2 to carburize a work inside, a vacuum carburizing gas feed means 4 to feed the vacuum carburizing gas containing ethylene gas and hydrogen gas to the work in the carburizing chamber 2 from the top, and an evacuating means 6 to suck the gas in the carburizing chamber 2 from the bottom of the work. It further comprises an increase/decrease detecting means 33 to detect the increase/decrease of the number of molecules of ethylene gas, and an exhaust quantity adjusting means 7 to adjust the exhaust quantity of the vacuum carburizing gas to be exhausted from the carburizing chamber 2 based on the increase/decrease of the number of molecules of ethylene gas.

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
びこの真空浸炭方法を実施する浸炭炉に関する。
The present invention relates to a vacuum carburizing method and a carburizing furnace for performing the vacuum carburizing method.

【0002】なお、本明細書において「ガス浸炭」と
は、大気圧下で行われるガス浸炭を意味し、「真空浸
炭」とは減圧下で行われるガス浸炭を意味するものとす
る。
[0002] In the present specification, "gas carburization" means gas carburization performed under atmospheric pressure, and "vacuum carburization" means gas carburization performed under reduced pressure.

【0003】[0003]

【従来の技術】従来の浸炭炉として図6に記載のものが
ある。
2. Description of the Related Art FIG. 6 shows a conventional carburizing furnace.

【0004】この浸炭炉は、真空浸炭を行うためのもの
であり、浸炭炉は真空容器(51)と、真空容器(51)内にお
いて高純度セラミックファイバにより形成された壁によ
り囲われた浸炭室(52)と、浸炭室(52)と隣り合って設け
られた油槽室(53)と、ダイアフラムの変位量を機械的に
検知する方式の真空計(54)とを備えたものであり、図示
は省略したが真空容器(51)の壁および浸炭室(52)の壁を
貫通して先端が浸炭室(52)内に位置したガス導入管によ
り真空浸炭用ガスが浸炭室(52)内部に導入されるように
なっている。
This carburizing furnace is for performing vacuum carburizing. The carburizing furnace is a carburizing chamber surrounded by a vacuum vessel (51) and a wall formed of high-purity ceramic fiber in the vacuum vessel (51). (52), an oil tank chamber (53) provided adjacent to the carburizing chamber (52), and a vacuum gauge (54) for mechanically detecting the amount of displacement of the diaphragm. Was omitted, but the gas for vacuum carburizing was introduced into the carburizing chamber (52) by a gas introduction pipe which penetrated the wall of the vacuum vessel (51) and the carburizing chamber (52) and whose tip was located in the carburizing chamber (52). It is being introduced.

【0005】そして浸炭室(52)内の圧力が真空計(54)に
より検出され、この検出値に基づき浸炭室(52)内の圧力
が所定の値に調整されるようになっている。この例では
浸炭用ガスとしてアセチレンガスが用いられる。他にエ
チレンガスを用いる真空浸炭方法も公知である。本発明
は浸炭用ガスとしてエチレンガスを用いる方法および装
置に関するものである。
The pressure in the carburizing chamber (52) is detected by a vacuum gauge (54), and the pressure in the carburizing chamber (52) is adjusted to a predetermined value based on the detected value. In this example, acetylene gas is used as the carburizing gas. A vacuum carburizing method using ethylene gas is also known. The present invention relates to a method and an apparatus using ethylene gas as a carburizing gas.

【0006】[0006]

【発明が解決しようとする課題】上記従来の浸炭炉およ
び真空浸炭方法においては、浸炭が行われることによ
り、炉内で分解、生成したガスと真空浸炭用ガスとの混
合ガスの全圧力を絶対圧で計測していることになる。
In the above-mentioned conventional carburizing furnace and vacuum carburizing method, the total pressure of the mixed gas of the gas decomposed and generated in the furnace and the gas for vacuum carburizing is absolutely reduced by carburizing. This means that pressure is being measured.

【0007】ところで、浸炭プロセスにおいては煤の発
生を抑える等の目的でより高い精度でプロセスの経過と
ともに必要度に応じた量のエチレンを浸炭室に供給する
ことが望ましい。このような観点から、発明者らはエチ
レンを用いた浸炭プロセス中の系内のガス分子の挙動を
四重極質量分析計によりモニタしていたところ、次のこ
とが分かった。すなわち、浸炭プロセスにおいては、終
期に比べて初期に多くのエチレン分子を必要とするが、
従来の装置では浸炭室内の全圧力の絶対圧を計測してい
るために、浸炭室内におけるエチレンの量を制御するこ
とができなかった。実際に、圧力60〜70Torrで実験
を行ったところ、従来の装置においては浸炭初期に対し
終期にはエチレンの検出値が2倍程度まで増加し、プロ
セスが要求するのと反対の経過をたどっていることが分
かった。
In the carburizing process, it is desirable to supply ethylene to the carburizing chamber with a higher degree of accuracy as the process proceeds with the aim of suppressing the generation of soot and the like. From such a viewpoint, the present inventors have monitored the behavior of gas molecules in the system during the carburization process using ethylene with a quadrupole mass spectrometer, and found the following. In other words, in the carburizing process, more ethylene molecules are required at the beginning than at the end,
Since the conventional apparatus measures the absolute pressure of the total pressure in the carburizing chamber, the amount of ethylene in the carburizing chamber cannot be controlled. Actually, when the experiment was conducted at a pressure of 60 to 70 Torr, the detected value of ethylene increased to about twice at the end of the conventional carburization compared to the initial stage of carburization, and it followed the course opposite to that required by the process. I knew it was there.

【0008】本発明の目的は、上記課題を解決した、エ
チレンと水素を真空浸炭用ガスとして用いたときに、浸
炭室内におけるエチレン分子の数が浸炭の初期から終期
にかけて実質的に増加しない、煤の発生が少なく、大容
量のパッチ内の浸炭ばらつきを極めて小さく抑えること
のできる優れた真空浸炭方法およびこの方法を実施する
浸炭炉を提供することにある。
[0008] An object of the present invention is to solve the above-mentioned problems. When ethylene and hydrogen are used as a vacuum carburizing gas, the number of ethylene molecules in the carburizing chamber does not substantially increase from the beginning to the end of carburization. It is an object of the present invention to provide an excellent vacuum carburizing method capable of minimizing carburization variation in a large-capacity patch and minimizing the occurrence of carburizing, and a carburizing furnace for performing the method.

【0009】[0009]

【課題を解決するための手段および発明の効果】上記課
題を解決するために本発明の真空浸炭方法は、エチレン
ガスと水素ガスとを含む真空浸炭用ガスを浸炭室に給気
するととともに給気された真空浸炭用ガスを排気する真
空浸炭方法において、浸炭の初期から終期にかけて浸炭
室内のエチレン分子数が実質的に増加しないことを特徴
とするものである。
Means for Solving the Problems and Effects of the Invention In order to solve the above problems, a vacuum carburizing method according to the present invention supplies a vacuum carburizing gas containing ethylene gas and hydrogen gas to a carburizing chamber and supplies air. In the vacuum carburizing method for exhausting the vacuum carburizing gas, the number of ethylene molecules in the carburizing chamber does not substantially increase from the beginning to the end of carburizing.

【0010】この方法によれば、多くの炭素供給源を必
要とする浸炭の初期には十分なエチレンが存在して浸炭
ばらつきを少なくできると同時に、より少ない炭素供給
源でよい終期には、エチレンの分子数が増加しないの
で、煤の発生を抑えることができる。
According to this method, there is sufficient ethylene present at the beginning of carburizing which requires a large amount of carbon source to reduce carburizing variability, and at the end of the period when less carbon source is required, ethylene is used. Since the number of molecules does not increase, generation of soot can be suppressed.

【0011】また、本発明の浸炭炉は、内部にてワーク
を浸炭処理する浸炭室と、エチレンガスと水素ガスとを
含む真空浸炭用ガスを浸炭室内のワークに上方から供給
する真空浸炭用ガス給気手段と、浸炭室内のガスをワー
クの下方から吸い出す真空排気手段とを備えた浸炭炉に
おいて、エチレンガスの分子数の増減を検知する増減検
知手段と増減検知手段により検知されたエチレンガスの
分子数の増減に基づいて浸炭室から排気される真空浸炭
用ガスの排気量を調整する排気量調整手段とを有し、真
空浸炭用ガス給気手段が、真空浸炭用ガスをワークに均
一に分散させて給気するためのガス分散手段を有し、真
空排気手段が、浸炭用ガスを均一に排気するための複数
の真空排気口に分岐接続されていることを特徴とするも
のである。
Further, the carburizing furnace of the present invention has a carburizing chamber for carburizing a work therein, and a vacuum carburizing gas for supplying a vacuum carburizing gas containing ethylene gas and hydrogen gas to the work in the carburizing chamber from above. In a carburizing furnace equipped with an air supply unit and a vacuum exhaust unit that sucks gas in the carburizing chamber from below the work, an increase / decrease detection unit that detects an increase / decrease in the number of molecules of ethylene gas and an amount of the ethylene gas detected by the increase / decrease detection unit. An exhaust amount adjusting means for adjusting an exhaust amount of the vacuum carburizing gas exhausted from the carburizing chamber based on an increase or a decrease in the number of molecules, wherein the vacuum carburizing gas supply means uniformly applies the vacuum carburizing gas to the workpiece. A gas dispersing means for dispersing and supplying air is provided, and the vacuum exhaust means is branched and connected to a plurality of vacuum exhaust ports for uniformly exhausting the carburizing gas.

【0012】この浸炭炉においては上記の方法を容易に
実施できる。また、浸炭用ガスがワークの周面全域にわ
たって均一に分散されて給気され、複数の排気兼真空引
管をほぼ等しい量のガスが流れるようにして排気される
ので複数の処理品を炉内における異なる位置に配しても
均一に浸炭処理された高い品質の処理品が得られる。
In this carburizing furnace, the above method can be easily implemented. In addition, the carburizing gas is uniformly dispersed and supplied over the entire peripheral surface of the workpiece, and the plurality of exhausted and evacuated pipes are evacuated so that approximately the same amount of gas flows. Even if they are arranged at different positions in, a high-quality treated product uniformly carburized can be obtained.

【0013】なお、増減検知手段には水晶式真空計を用
いることが好ましい。水晶式真空計とは、水晶振動子の
共振インピーダンスが圧力に応じて変化するという現象
を利用して圧力を測定するものであるが、エチレンガス
と水素を含む真空浸炭用ガスを炉内に導入し、同時に排
気しながらこの真空計を用いて圧力制御して真空浸炭処
理したところ、エチレンの分子数が浸炭プロセス中にお
いて実質的に一定に保たれ、所要の好結果が再現性よく
得られ、量産に適していることが分かった。その原理に
ついては現在解明中である。
It is preferable to use a quartz vacuum gauge for the increase / decrease detection means. A quartz vacuum gauge measures pressure by using the phenomenon that the resonance impedance of a quartz oscillator changes according to pressure, but a vacuum carburizing gas containing ethylene gas and hydrogen is introduced into the furnace. Then, when performing vacuum carburizing treatment by controlling the pressure using this vacuum gauge while simultaneously evacuating, the number of ethylene molecules is kept substantially constant during the carburizing process, and the required good results are obtained with good reproducibility, It turned out to be suitable for mass production. The principle is currently being elucidated.

【0014】上記の炉において、ガス分散手段が、ガス
分散手段が、浸炭室を貫通してワークの上方までのびる
水平状ガス導入管と、導入管から分岐状に設けられてい
るとともに周壁下部に軸方向に間隔をおいて複数のガス
吹出孔があけられている1または2以上の先端閉鎖水平
状ガス分岐管とを備えていることがある。
In the above furnace, the gas dispersing means is provided with a horizontal gas introducing pipe extending through the carburizing chamber and extending to above the work, and a gas dispersing means provided in a branched shape from the introducing pipe and at a lower portion of the peripheral wall. It may include one or more closed-end horizontal gas branch pipes having a plurality of gas outlets spaced apart in the axial direction.

【0015】上記の炉によれば真空浸炭用ガス給気手段
の構成が簡易となり装置が安価になる。
According to the above furnace, the structure of the gas supply means for vacuum carburizing is simplified and the apparatus is inexpensive.

【0016】また、浸炭室の壁が、断熱性材料とこれの
外側を覆う気密性材料により形成され、ガス浸炭用ガス
を浸炭室内に供給するガス浸炭用ガス給気手段と、ガス
浸炭用ガスを排気するガス浸炭用ガス排気手段と、浸炭
室内上部に設けられた攪拌ファンとを備えていることこ
とがある。
Further, a wall of the carburizing chamber is formed of a heat insulating material and an airtight material covering the outside thereof, and a gas carburizing gas supply means for supplying a gas for carburizing into the carburizing chamber; May be provided with gas exhaust means for gas carburizing for exhausting gas, and a stirring fan provided at the upper part of the carburizing chamber.

【0017】この炉においては真空浸炭だけでなくガス
浸炭をも行うことができる。
In this furnace, gas carburizing as well as vacuum carburizing can be performed.

【0018】さらに、ガス分散手段を、浸炭室の壁を上
方から貫通した回転自在な垂直状ガス導入管と、ガス導
入管の下端から放射状に伸びかつ周壁下部に軸方向に間
隔をおいて複数のガス吹出孔があけられている複数の先
端閉鎖水平状ガス分岐管とにより構成してもよい。
Further, the gas dispersing means includes a rotatable vertical gas introduction pipe penetrating the wall of the carburizing chamber from above, a plurality of gas dispersion means extending radially from the lower end of the gas introduction pipe and being axially spaced below the peripheral wall. And a horizontal gas branch pipe having a plurality of closed-end gas outlets.

【0019】このようにしても真空浸炭用ガス給気手段
の構成を簡易化することができ装置が安価になる。
In this way, the structure of the gas supply means for vacuum carburizing can be simplified and the apparatus can be made inexpensive.

【0020】[0020]

【発明の実施の形態】以下、図面を参照して本発明の実
施形態について説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0021】図1および図2は本発明における第1の実
施形態の真空浸炭炉を示したものである。
FIGS. 1 and 2 show a vacuum carburizing furnace according to a first embodiment of the present invention.

【0022】炉(1)は、壁(w)が断熱性材料とこれの外側
を覆う金属板により形成された浸炭室(2)と、浸炭室(2)
に隣り合って設けられた油槽室(3)と、浸炭室(2)に真空
浸炭用ガスを供給する真空浸炭用ガス給気経路(4)と、
真空浸炭時において浸炭室(2)内の真空浸炭用ガスを排
気する際および浸炭室(2)内を真空引きする際に用いら
れる真空排気経路(6)と、水晶式真空計(33)と、圧力調
節計(34)およびモータバルブ(32)とからなる排気量調整
手段(7)とを備えている。なお、図示は省略したが、浸
炭炉(1)には、外部から油槽室(3)にワークを搬入および
油槽室(3)から外部にワークを搬出する公知の搬入出装
置と油槽室(3)から浸炭室(2)にワークを搬入および浸炭
室(2)から油槽室(3)にワークを搬出する公知の搬入出装
置とが設けられている。
The furnace (1) comprises a carburizing chamber (2) having a wall (w) formed of a heat insulating material and a metal plate covering the outside thereof, and a carburizing chamber (2).
An oil tank chamber (3) provided adjacent to the gas supply path (4) for supplying a gas for vacuum carburizing to the carburizing chamber (2);
A vacuum evacuation path (6) used for evacuating the vacuum carburizing gas in the carburizing chamber (2) during vacuum carburizing and for evacuating the carburizing chamber (2), and a crystal vacuum gauge (33). , A pressure regulator (34) and a motor valve (32). Although not shown in the drawings, the carburizing furnace (1) has a well-known loading / unloading device and an oil tank chamber (3) that carry a work into and out of the oil tank chamber (3) from outside to the oil tank chamber (3). ) And a known carry-in / out device for carrying the work into the carburizing chamber (2) from the carburizing chamber (2) and carrying the work from the carburizing chamber (2) to the oil tank chamber (3).

【0023】浸炭室(2)は、扉(2a)によって開閉される
ワーク搬入出口によって油槽室(3)と連通し、油槽室(3)
には扉(3a)によって開閉されるワーク搬入出口が形成さ
れている。また、浸炭室(2)内には複数のラジアントチ
ューブヒータ(12)が配置され、浸炭室(2)内が所定の温
度まで昇温されるようになっている。
The carburizing chamber (2) communicates with the oil tank chamber (3) through a work loading / unloading opening and closing by a door (2a), and the oil tank chamber (3)
Is formed with a work loading / unloading opening and closing that is opened and closed by a door (3a). Further, a plurality of radiant tube heaters (12) are arranged in the carburizing chamber (2) so that the temperature inside the carburizing chamber (2) is raised to a predetermined temperature.

【0024】さらに、浸炭室(2)には復圧用窒素ガス供
給管(24)が接続され、一方油槽室(3)には真空ポンプ(1
5)および復圧用窒素ガス供給管(16)が接続されている。
なお、浸炭室(2)と油槽室(3)とは内部の圧力を同一にす
ることができるように配管(25)により接続されている。
なお、壁(w)の断熱性材料は、セラミックファイバを真
空圧縮成形したものであり、ガスの浸透が防止されるよ
うになっている。
Further, a nitrogen gas supply pipe (24) for pressure recovery is connected to the carburizing chamber (2), while a vacuum pump (1) is connected to the oil tank chamber (3).
5) and a nitrogen gas supply pipe (16) for pressure recovery.
The carburizing chamber (2) and the oil tank chamber (3) are connected by a pipe (25) so that the internal pressure can be made equal.
The heat insulating material of the wall (w) is a ceramic fiber formed by vacuum compression molding, so that gas penetration is prevented.

【0025】真空浸炭用ガス給気経路(4)は、浸炭室(2)
に浸炭ガスとしてエチレンと水素との混合ガスを供給す
るものであり、浸炭室(2)の上壁を貫通した垂直状ガス
導入管(10)と、ガス導入管(10)の下端から放射状に伸び
た複数の水平状ガス分岐管(11)とを備えている。図示は
省略したが、ガス分岐管(11)の周壁下部には軸方向に間
隔を置いて複数のガス吹出孔があけられている。
The vacuum carburizing gas supply path (4) is provided in a carburizing chamber (2).
A gaseous mixture of ethylene and hydrogen is supplied as a carburizing gas to a vertical gas inlet pipe (10) penetrating the upper wall of the carburizing chamber (2), and radially from the lower end of the gas inlet pipe (10). A plurality of extended horizontal gas branch pipes (11). Although not shown, a plurality of gas blowing holes are formed at a lower portion of the peripheral wall of the gas branch pipe (11) at intervals in the axial direction.

【0026】導入管(10)は、上流側が分岐した接続管(1
8)にロータリジョイント(17)を介して接続されている。
そして、導入管(10)はこれの上端に接続された駆動機(1
3)、例えば電動モータにより垂直軸周りに回転するよう
になっている。接続管(18)の分岐側端部にはエチレンボ
ンベ(8)および水素ボンベ(9)が接続されている。接続管
(18)の分岐部分におけるボンベ(8)(9)の下流側にはレギ
ュレータ(20)(21)が設けられている。なお、図示は省略
したが分岐部分には流量計等も配されている。分岐して
いない部分にはガス導入弁(23)が配されている。
The introduction pipe (10) is a connection pipe (1) whose upstream side is branched.
8) is connected via a rotary joint (17).
Then, the introduction pipe (10) is connected to the driving machine (1
3), for example, rotating about a vertical axis by an electric motor. An ethylene cylinder (8) and a hydrogen cylinder (9) are connected to a branch end of the connection pipe (18). Connection pipe
Regulators (20) and (21) are provided on the downstream side of the cylinders (8) and (9) in the branch portion of (18). Although not shown, a flow meter or the like is also provided at the branch portion. A gas introduction valve (23) is provided in a portion that is not branched.

【0027】真空排気経路(6)は、浸炭室(2)の底面に開
口した複数の真空排気口を備えたマニフォルド(26)を備
えている。マニフォルド(26)の真空排気口は、真空浸炭
を行うさいなど、ガスを排気するときに各真空排気口を
流れるガスの量が等しくなるように、前後左右に所定の
間隔を置いて2列に配されている。
The evacuation path (6) includes a manifold (26) having a plurality of evacuation ports opened at the bottom of the carburizing chamber (2). The vacuum exhaust ports of the manifold (26) are arranged in two rows at predetermined intervals in the front, rear, left and right so that the amount of gas flowing through each vacuum exhaust port is equal when exhausting gas, such as during vacuum carburization. Are arranged.

【0028】マニフォルド(26)は、水平状ガス導出管(2
7)に接続されている。ガス導出管(27)は、途中で2経路
に分岐した配管を介して真空ポンプ(28)に接続されてい
る。配管における分岐部分の一方には大真空弁(30)が、
他方には小真空弁(31)とモータバルブ(32)が配されてい
る。
The manifold (26) is provided with a horizontal gas outlet pipe (2).
7) is connected. The gas outlet pipe (27) is connected to a vacuum pump (28) via a pipe branched into two paths on the way. A large vacuum valve (30) is provided on one of the branches in the piping,
On the other side, a small vacuum valve (31) and a motor valve (32) are arranged.

【0029】水晶式真空計(33)は、圧力調節計(34)に接
続され、圧力調節計(34)には前述のモータバルブ(32)が
接続されている。なお、圧力調節計(34)およびモータバ
ルブ(32)は公知のものであり詳細な説明は省略する。
The crystal vacuum gauge (33) is connected to a pressure controller (34), and the motor valve (32) is connected to the pressure controller (34). The pressure controller (34) and the motor valve (32) are publicly known, and a detailed description thereof will be omitted.

【0030】なお、上記の炉(1)において、浸炭室(2)内
の有効空間の上端と分岐管(11)との間隔は100〜15
0mm程度が好ましい。また分岐管(11)のガス吹出口の
口径は3mm程度、ピッチは32〜53mmがよい。ま
た、マニフォルド(26)の真空排気口は有効空間の下方
に、10個程度形成するのが好ましい。
In the furnace (1), the distance between the upper end of the effective space in the carburizing chamber (2) and the branch pipe (11) is 100 to 15
About 0 mm is preferable. The diameter of the gas outlet of the branch pipe (11) is preferably about 3 mm, and the pitch is preferably 32 to 53 mm. Further, it is preferable to form about ten vacuum exhaust ports of the manifold (26) below the effective space.

【0031】さらに好ましくは2列5個ずつに並べる。
またマニフォルド(26)の管径は20mm程度が好まし
い。
More preferably, they are arranged in two rows of five pieces each.
The diameter of the manifold (26) is preferably about 20 mm.

【0032】上記のように構成された炉(1)においては
以下のようにして真空浸炭処理が行われる。なお以下の
圧力値は、特に記載がある場合を除き、いずれも炉(1)
内の実際の絶対圧である。
In the furnace (1) configured as described above, vacuum carburizing is performed as follows. The following pressure values were used for furnace (1) unless otherwise specified.
Is the actual absolute pressure inside.

【0033】浸炭室(2)内を処理温度(通常930〜1
050°)まで昇温する。同時に浸炭室(2)内を真空ポ
ンプ(28)によって真空引(通常1Torr(133.32Pa)以
下)しておく。なお、この際大真空弁(30)があけられ小
真空弁(31)は閉じられている。一方、油槽室(3)内には
復圧用窒素ガス供給管(16)から窒素ガスが供給されて油
槽室(3)内の圧力は大気圧となされている。
The inside of the carburizing chamber (2) is treated at a processing temperature (normally 930 to 1).
050 °). At the same time, the inside of the carburizing chamber (2) is evacuated (usually 1 Torr (133.32 Pa) or less) by a vacuum pump (28). At this time, the large vacuum valve (30) is opened and the small vacuum valve (31) is closed. On the other hand, a nitrogen gas is supplied into the oil tank chamber (3) from a nitrogen gas supply pipe (16) for pressure recovery, and the pressure in the oil tank chamber (3) is set to the atmospheric pressure.

【0034】そして、扉(3a)をあけて油槽室(3)内にワ
ークを搬入したのち、扉(3a)を閉じる。つぎに油槽室
(3)内を真空ポンプ(15)によって真空引(通常1Torr(13
3.32Pa)以下)し、油槽室(3)と浸炭室(2)とを配管(25)
により同圧にする。
Then, after opening the door (3a) and carrying the work into the oil tank chamber (3), the door (3a) is closed. Next, the oil tank room
The inside of (3) is evacuated by a vacuum pump (15) (normally 1 Torr (13
3.32Pa) or less), and pipe (25) between the oil tank room (3) and the carburizing room (2).
To make the same pressure.

【0035】油槽室(3)と浸炭室(2)とを同圧にした後、
扉(2a)をあけて浸炭室(2)内にワークを搬入し、扉(2a)
を閉じて浸炭室(2)内が処理温度に復温するのを待つ。
復温後は所定時間(通常40分以上)浸炭室(2)内にて
ワークを保持して予熱する。なお、この際油槽室(3)を
600Torr(79992Pa)程度まで復圧しておく。
After the oil tank chamber (3) and the carburizing chamber (2) have the same pressure,
Open the door (2a), carry the workpiece into the carburizing chamber (2), and open the door (2a).
And wait until the inside of the carburizing chamber (2) has returned to the processing temperature.
After the temperature is restored, the workpiece is held and preheated in the carburizing chamber (2) for a predetermined time (normally 40 minutes or more). At this time, the pressure in the oil tank chamber (3) is restored to about 600 Torr (79992 Pa).

【0036】予熱完了後、真空浸炭用ガス導入弁(23)を
あけて浸炭室(2)内に真空浸炭用ガスを供給する。この
際レギュレータ(20)(21)により供給される真空浸炭用ガ
スの圧力が750Torr(0.1MPa)程度になるように調整
されている。
After the completion of the preheating, the vacuum carburizing gas is supplied into the carburizing chamber (2) by opening the vacuum carburizing gas introduction valve (23). At this time, the pressure of the vacuum carburizing gas supplied by the regulators (20) and (21) is adjusted to be about 750 Torr (0.1 MPa).

【0037】真空浸炭用ガス供給時にはガス導入管(10)
は、駆動機(13)により垂直軸周りに回転させられてお
り、ワークの上方で分岐管(11)が回転しながら真空浸炭
用ガスを供給しかつ供給した真空浸炭用ガスをワークに
均一に分散して真空浸炭用ガスが給気されるようになっ
ている。
When supplying gas for vacuum carburization, a gas introduction pipe (10)
Is rotated about a vertical axis by a driving machine (13), and while the branch pipe (11) rotates above the work, the vacuum carburizing gas is supplied and the supplied vacuum carburizing gas is uniformly applied to the work. The gas for vacuum carburizing is dispersed and supplied.

【0038】また、壁(w)の内張はガスバリア性材料で
あるので浸炭用ガスが壁に浸透する量はごくわずかであ
るため浸透室(2)内に供給された浸炭用ガスは有効に浸
炭に用いられて煤化することがない。
Further, since the lining of the wall (w) is a gas barrier material, the amount of the carburizing gas permeating the wall is very small, so that the carburizing gas supplied into the permeation chamber (2) can be effectively used. It is not sooted by carburizing.

【0039】一方真空浸炭用ガスが供給されているさい
は、大真空弁(30)を閉じ、小真空弁(31)を開け、浸炭室
(2)内のガスを排気する。この際真空計(33)により浸炭
室(2)内の圧力が測定され、圧力調節計(34)によってモ
ータバルブ(32)の開度が調整され、浸炭室(2)から排気
されるガスの量が調整される。
On the other hand, when the vacuum carburizing gas is supplied, the large vacuum valve (30) is closed, the small vacuum valve (31) is opened, and the carburizing chamber is opened.
Exhaust the gas in (2). At this time, the pressure in the carburizing chamber (2) is measured by the vacuum gauge (33), the opening of the motor valve (32) is adjusted by the pressure controller (34), and the gas exhausted from the carburizing chamber (2) is The amount is adjusted.

【0040】例えば、真空計(33)により測定された圧力
が50Torrである場合に浸炭室(2)に給気された真空浸炭
用ガスと同量のガスが浸炭室(2)から排気されるように
排気量を定める。そして、真空計(33)により測定された
測定値の変化に応じてガスの排気量が変化して浸炭室
(2)内のエチレンの分子数が実質的に一定に保たれる。
この際浸炭室(2)内の実際の圧力は排気量の変化に伴い
変化するが、通常、25〜65Torr(3333〜8665.8Pa)
に保たれる。なお、エチレンの分子数がわずかに減少す
るようにしてもよい。
For example, when the pressure measured by the vacuum gauge (33) is 50 Torr, the same amount of gas as the vacuum carburizing gas supplied to the carburizing chamber (2) is exhausted from the carburizing chamber (2). To determine the displacement. The displacement of the gas changes according to the change in the measurement value measured by the vacuum gauge (33),
The number of ethylene molecules in (2) is kept substantially constant.
At this time, the actual pressure in the carburizing chamber (2) changes with the change in the displacement, but usually 25 to 65 Torr (3333 to 8665.8 Pa)
Is kept. Note that the number of ethylene molecules may be slightly reduced.

【0041】所定時間の浸炭が行われた後は、小真空弁
(31)を閉じ大真空弁(30)を開き真空ポンプ(28)によって
浸炭室(2)内を真空引し、拡散処理を行う。拡散処理終
了後は、ワークを焼入温度まで降温、均熱する。この後
大真空弁(30)を閉じて浸炭室(2)に復圧用窒素ガス供給
管(24)から窒素を供給し600Torr(79992Pa)に復圧し
た後、浸炭室(2)と油槽室(3)とを同圧にし、浸炭室(2)
から油槽室(3)にワークを搬出して油槽室(3)にて焼入を
行う。
After carburizing for a predetermined time, the small vacuum valve
(31) is closed, the large vacuum valve (30) is opened, and the inside of the carburizing chamber (2) is evacuated by the vacuum pump (28) to perform diffusion treatment. After the completion of the diffusion processing, the temperature of the work is lowered to the quenching temperature and the work is uniformly heated. Thereafter, the large vacuum valve (30) is closed, nitrogen is supplied to the carburizing chamber (2) from the nitrogen gas supply pipe (24) for decompression and the pressure is restored to 600 Torr (79992 Pa), and then the carburizing chamber (2) and the oil tank chamber ( 3) and the same pressure, carburizing chamber (2)
The work is carried out to the oil tank chamber (3) and quenched in the oil tank chamber (3).

【0042】以下に、グロス240kgの被処理物を搭
載したバスケット内の炉(1)内において高さ方向および
炉(1)の長さ方向に異なる位置に配置された5つの試料
(SCM420H2製)を1Torr(133.32Pa)、950℃にて予
熱100分、50Torr(6666Pa)、950℃にて浸炭7
0分、1Torr(133.32Pa)、950℃にて拡散50分、1
Torr(133.32Pa)、850℃にて均熱30分の処理をそ
れぞれ行い、600Torr(79992Pa)にて焼入した後16
0℃にて焼戻90分を行った結果の各試料の表面硬度、
硬化層深さおよび表面炭素濃度を示す表を図3に示す。
なお、給気の際のエチレンガスの流量は10L/min
であり、水素の流量は5L/minである。
In the following, five samples (manufactured by SCM420H2) arranged at different positions in the height direction and the length direction of the furnace (1) in the furnace (1) in the basket on which the object to be processed having a gross of 240 kg is mounted. Is preheated at 1 Torr (133.32 Pa) and 950 ° C. for 100 minutes, carburized at 50 Torr (6666 Pa) and 950 ° C. 7
0 min, 1 Torr (133.32 Pa), diffusion at 950 ° C. 50 min, 1
Torr (133.32 Pa), soaking at 850 ° C. for 30 minutes, and quenching at 600 Torr (79992 Pa).
Surface hardness of each sample as a result of tempering at 0 ° C. for 90 minutes,
FIG. 3 is a table showing the depth of the hardened layer and the surface carbon concentration.
The flow rate of ethylene gas at the time of air supply is 10 L / min.
And the flow rate of hydrogen is 5 L / min.

【0043】この図から各試料の表面硬度、硬化層深さ
および表面炭素濃度はほぼ均一であることが分かり、こ
の炉(1)により高い品質で真空浸炭が行えることが分か
る。また、壁(w)の内側を形成する断熱材料がセラミッ
クファイバを真空圧縮成型して形成されているので浸炭
用ガスがほとんど染みいることがなく、浸炭室に給気さ
れた浸炭用ガスが有効に浸炭に用いられるとともに浸炭
用ガス圧力の制御が容易になる。
From this figure, it can be seen that the surface hardness, hardened layer depth and surface carbon concentration of each sample are almost uniform, and that this furnace (1) can perform vacuum carburization with high quality. In addition, since the heat insulating material that forms the inside of the wall (w) is formed by vacuum-compressing ceramic fibers, the carburizing gas is hardly stained, and the carburizing gas supplied to the carburizing chamber is effective. It is used for carburizing and the control of the carburizing gas pressure becomes easy.

【0044】つぎに図4および図5を参照して本発明に
おける第2の実施形態の炉(40)について説明する。第1
の実施形態の炉(1)と同一部分および対応する部分につ
いては同一の符号を付けて説明は省略する。
Next, a furnace (40) according to a second embodiment of the present invention will be described with reference to FIGS. First
The same parts as those of the furnace (1) of the embodiment and the corresponding parts are denoted by the same reference numerals and description thereof will be omitted.

【0045】炉(40)は、真空浸炭用ガス給気手段(41)が
第1の実施形態の炉(1)と異なるとともにガス浸炭をも
実施しうるようにしたものである。
The furnace (40) is different from the furnace (1) of the first embodiment in that the gas supply means (41) for vacuum carburizing is also capable of performing gas carburizing.

【0046】真空浸炭用ガス給気手段(41)は、浸炭室の
垂直壁を側方から貫通してワークの上方までのびるとと
もに互いに対向するように設けられた第1および第2水
平状ガス導入管(43)(44)と、第1導入管(43)から第2導
入管(44)側に向かって伸びるとともに周壁下部に軸方向
に間隔をおいて複数のガス吹出孔(図示略)があけられ
ている複数の先端閉鎖水平状第1導入管側ガス分岐管(4
5)と、第2導入管(44)から第1導入管(43)側に向かって
かつ第1導入管側ガス分岐管(45)と交互に位置するよう
に伸びるとともに周壁下部に軸方向に間隔をおいて複数
のガス吹出孔(図示略)があけられている複数の先端閉
鎖水平状第2導入管側ガス分岐管(46)とを備えている。
また、炉(40)は、浸炭室内上部に設けられた攪拌ファン
(42)と、浸炭室(2)にガス浸炭用ガスを供給するガス浸
炭用ガス給気経路(5)と、ガス浸炭時においてガス浸炭
用ガスを排気するガス浸炭用ガス排気管(35)とを備えて
いるものである。
The vacuum carburizing gas supply means (41) is provided with first and second horizontal gas inlets provided so as to extend from the side of the vertical wall of the carburizing chamber to the upper side of the work and to face each other. A plurality of gas outlets (not shown) extending from the first inlet pipe (43) toward the second inlet pipe (44) and extending in the lower part of the peripheral wall at an axial distance are provided at the pipes (43) and (44). A plurality of gas-closed pipes (4
5), extending from the second inlet pipe (44) toward the first inlet pipe (43) side and alternately with the first inlet pipe side gas branch pipe (45), and extending axially below the peripheral wall. A plurality of gas outlet pipes (46) having a plurality of gas outlet holes (not shown) spaced apart from each other and having a closed end at the end thereof are provided on the second inlet pipe side.
The furnace (40) is a stirring fan provided at the upper part of the carburizing chamber.
(42), gas carburizing gas supply path (5) for supplying gas carburizing gas to carburizing chamber (2), and gas carburizing gas exhaust pipe (35) for exhausting gas carburizing gas during gas carburizing It is provided with.

【0047】この真空浸炭用ガス給気手段(41)において
も真空浸炭用ガスはワークの周面全域にわたって均一に
供給される。また、真空浸炭を行う手順は第1の実施形
態の炉(1)と変わるところはない。なお、この実施例の
浸炭炉(40)においてはガス浸炭も可能とするためガス浸
炭用ガス給気経路(5)およびガス浸炭用ガス排気管(35)
の他に炉内雰囲気を攪拌するためのファン(42)が設置さ
れ、ガス浸炭を実施することができる。
Also in this vacuum carburizing gas supply means (41), the vacuum carburizing gas is supplied uniformly over the entire peripheral surface of the work. Further, the procedure for performing vacuum carburization is not different from the furnace (1) of the first embodiment. In the carburizing furnace (40) of this embodiment, a gas supply path for gas carburizing (5) and a gas exhaust pipe for gas carburizing (35) to enable gas carburizing.
In addition, a fan (42) for stirring the atmosphere in the furnace is provided, and gas carburization can be performed.

【0048】ガス浸炭を行う際は、浸炭室(2)内に窒素
ガス供給管(24)によって窒素ガスを供給して浸炭室(2)
内を復圧する。この後、ガス浸炭用ガス給気経路(5)か
ら窒素ガスを供給する。浸炭室(2)内の圧力が大気圧以
上にまで上昇するとガス浸炭用ガス排気管(35)から窒素
ガスが排出される。所定時間浸炭室(2)内のパージが行
われると、ガス浸炭用ガス給気経路(5)から導入される
ガスが吸熱形炉気に切り替えて導入される。
When gas carburizing is performed, nitrogen gas is supplied into the carburizing chamber (2) by a nitrogen gas supply pipe (24).
Repressurize inside. Thereafter, nitrogen gas is supplied from the gas supply path (5) for gas carburizing. When the pressure in the carburizing chamber (2) rises above the atmospheric pressure, nitrogen gas is discharged from the gas carburizing gas exhaust pipe (35). When the purge in the carburizing chamber (2) is performed for a predetermined time, the gas introduced from the gas carburizing gas supply path (5) is switched to the endothermic furnace gas and introduced.

【0049】浸炭室(2)の容積の3〜7倍以上の浸炭用
ガスを流した後、浸炭室(2)内に処理品が搬入されて浸
炭処理が行われる。ガス浸炭中の処理手順は従来のガス
浸炭専用の浸炭炉における手順と変わるところはなく詳
細な説明は省略する。
After flowing a carburizing gas of at least 3 to 7 times the volume of the carburizing chamber (2), the treated product is carried into the carburizing chamber (2) to be carburized. The processing procedure during gas carburizing is the same as the procedure in a conventional carburizing furnace dedicated to gas carburizing, and detailed description is omitted.

【0050】なお、上記の炉(40)においても、第1の実
施形態の炉(1)と同様、有効空間の上端と分岐管(45)(4
6)との間隔は100〜150mm程度が好ましい。また
分岐管(45)(46)のガス吹出口の口径も3mm程度、ピッ
チも32〜53mmがよい。
In the furnace (40), similarly to the furnace (1) of the first embodiment, the upper end of the effective space and the branch pipes (45) (4)
The distance from 6) is preferably about 100 to 150 mm. The diameter of the gas outlets of the branch pipes (45) and (46) is preferably about 3 mm, and the pitch is preferably 32 to 53 mm.

【0051】上記の実施形態の炉(1)(40)においては加
熱装置としてラジアントチューブヒータが用いられてい
るが、加熱装置はこれに限られるものではなく、処理条
件等に応じ、適当な加熱装置を用いればよい。
In the furnaces (1) and (40) of the above embodiment, a radiant tube heater is used as a heating device. However, the heating device is not limited to this, and appropriate heating may be performed according to processing conditions and the like. An apparatus may be used.

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

【図1】本発明の第1の実施形態における浸炭炉の概略
図である。
FIG. 1 is a schematic view of a carburizing furnace according to a first embodiment of the present invention.

【図2】同浸炭炉の要部の平面図である。FIG. 2 is a plan view of a main part of the carburizing furnace.

【図3】(a)、(b)、(c)は、同浸炭炉において真空浸炭
した複数の試料の表面硬度、硬化層深さ、表面炭素濃度
を比較した結果を示す図である。
FIGS. 3 (a), (b), and (c) are diagrams showing the results of comparing the surface hardness, hardened layer depth, and surface carbon concentration of a plurality of samples vacuum carburized in the same carburizing furnace.

【図4】本発明の第2の実施形態における浸炭炉の要部
の概略図である。
FIG. 4 is a schematic view of a main part of a carburizing furnace according to a second embodiment of the present invention.

【図5】同浸炭炉における図2相当の図である。FIG. 5 is a diagram corresponding to FIG. 2 in the carburizing furnace.

【図6】従来の浸炭炉の概略図である。FIG. 6 is a schematic view of a conventional carburizing furnace.

【符号の説明】[Explanation of symbols]

(1)(40) 浸炭炉 (2) 浸炭室 (4)(41) 真空浸炭用ガス給気手段 (5) ガス浸炭用ガス給気手段 (6) 真空排気手段 (7) 排気量調整手段 (10) 垂直状ガス導入管 (11) 水平状ガス分岐管 (26) 複数の真空排気口を備えたマニフォルド (32) 排気量調整手段(モータバルブ) (33) 増減検知手段(水晶式真空計) (34) 排気量調整手段(圧力調節計) (35) ガス浸炭用ガス排気管 (42) 攪拌ファン (43)(44) 第1、第2ガス導入管 (45)(46) 第1ガス導入管側、第2ガス導入管側ガス分
岐管 (w) 浸炭室の壁
(1) (40) Carburizing furnace (2) Carburizing chamber (4) (41) Vacuum carburizing gas supply means (5) Gas carburizing gas supply means (6) Vacuum exhaust means (7) Displacement adjusting means ( 10) Vertical gas inlet pipe (11) Horizontal gas branch pipe (26) Manifold with multiple vacuum exhaust ports (32) Exhaust volume adjustment means (motor valve) (33) Increase / decrease detection means (crystal vacuum gauge) (34) Displacement adjustment means (pressure controller) (35) Gas exhaust pipe for gas carburizing (42) Stirring fan (43) (44) First and second gas introduction pipes (45) (46) First gas introduction Pipe side, second gas introduction pipe side gas branch pipe (w) Carburizing chamber wall

───────────────────────────────────────────────────── フロントページの続き (72)発明者 松原 周 奈良県天理市嘉幡町229番地 光洋サーモ システム 株式会社内 Fターム(参考) 4K028 AA01 AC03 AC08 4K063 AA05 AA15 AA16 BA02 CA03 DA01 DA15 DA19 DA28 DA33 DA34  ────────────────────────────────────────────────── ─── Continued on the front page (72) Inventor Shu Matsubara 229 Kahata-cho, Tenri-shi, Nara Koyo Thermo System Co., Ltd. F-term (reference) 4K028 AA01 AC03 AC08 4K063 AA05 AA15 AA16 BA02 CA03 DA01 DA15 DA19 DA28 DA33 DA34

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 エチレンガスと水素ガスとを含む真空浸
炭用ガスを浸炭室に給気するととともに給気された真空
浸炭用ガスを排気する真空浸炭方法において、 浸炭の初期から終期にかけて浸炭室内のエチレン分子数
が実質的に増加しないことを特徴とする真空浸炭方法。
In a vacuum carburizing method, a vacuum carburizing gas containing ethylene gas and hydrogen gas is supplied to a carburizing chamber and the supplied vacuum carburizing gas is exhausted. A vacuum carburizing method characterized in that the number of ethylene molecules does not substantially increase.
【請求項2】 内部にてワークを浸炭処理する浸炭室
と、エチレンガスと水素ガスとを含む真空浸炭用ガスを
浸炭室内のワークに上方から供給する真空浸炭用ガス給
気手段と、浸炭室内のガスをワークの下方から吸い出す
真空排気手段とを備えた浸炭炉において、 エチレンガスの分子数の増減を検知する増減検知手段と
増減検知手段により検知されたエチレンガスの分子数の
増減に基づいて浸炭室から排気される真空浸炭用ガスの
排気量を調整する排気量調整手段とを有し、 真空浸炭用ガス給気手段が、真空浸炭用ガスをワークに
均一に分散させて給気するためのガス分散手段を有し、 真空排気手段が、浸炭用ガスを均一に排気するための複
数の真空排気口に分岐接続されていることを特徴とする
浸炭炉。
2. A carburizing chamber for carburizing a work therein, a vacuum carburizing gas supply means for supplying a vacuum carburizing gas containing ethylene gas and hydrogen gas to a work in the carburizing chamber from above, and a carburizing chamber. In a carburizing furnace equipped with vacuum evacuation means for sucking out the gas from below the work, based on the increase / decrease detection means for detecting the increase / decrease in the number of ethylene gas molecules and the increase / decrease in the number of ethylene gas molecules detected by the increase / decrease detection means An exhaust amount adjusting means for adjusting an exhaust amount of the vacuum carburizing gas exhausted from the carburizing chamber, wherein the vacuum carburizing gas supply means uniformly supplies the vacuum carburizing gas to the work and supplies the gas. A carburizing furnace, characterized in that the evacuation means is branched and connected to a plurality of evacuation ports for uniformly exhausting the carburizing gas.
【請求項3】 ガス分散手段が、浸炭室を貫通してワー
クの上方までのびる水平状ガス導入管と、導入管から分
岐状に設けられているとともに周壁下部に軸方向に間隔
をおいて複数のガス吹出孔があけられている1または2
以上の先端閉鎖水平状ガス分岐管とを備えていることを
特徴とする請求項2記載の浸炭炉。
3. A gas dispersing means comprising: a horizontal gas introducing pipe extending through a carburizing chamber and extending above a work; a plurality of gas dispersing means being provided in a branched shape from the introducing pipe and being provided at a lower portion of a peripheral wall at an axial interval. 1 or 2 with gas outlets
The carburizing furnace according to claim 2, further comprising the above-mentioned horizontal gas branch pipe with a closed end.
【請求項4】浸炭室の壁が、断熱性材料とこれの外側を
覆う気密性材料により形成され、 ガス浸炭用ガスを浸炭室内に供給するガス浸炭用ガス給
気手段と、ガス浸炭用ガスを排気するガス浸炭用ガス排
気手段と、浸炭室内上部に設けられた攪拌ファンとを備
えていることを特徴とする請求項2または3に記載の浸
炭炉。
4. A gas carburizing gas supply means for supplying a gas carburizing gas into a carburizing chamber, wherein a wall of the carburizing chamber is formed of a heat insulating material and an airtight material covering the outside thereof. The carburizing furnace according to claim 2 or 3, further comprising a gas carburizing gas exhaust means for exhausting gas, and a stirring fan provided at an upper portion of the carburizing chamber.
【請求項5】 ガス分散手段が、浸炭室の壁を上方から
貫通した回転自在な垂直状ガス導入管と、ガス導入管の
下端から放射状に伸びかつ周壁下部に軸方向に間隔をお
いて複数のガス吹出孔があけられている複数の先端閉鎖
水平状ガス分岐管とを備えていることを特徴とする請求
項2記載の浸炭炉。
5. A gas dispersing means, comprising: a rotatable vertical gas introduction pipe penetrating from the top of a wall of a carburizing chamber; and a plurality of gas dispersion means extending radially from a lower end of the gas introduction pipe and being axially spaced below a peripheral wall. 3. A carburizing furnace according to claim 2, comprising a plurality of horizontal gas branch pipes each having a closed end and having a plurality of gas discharge holes.
JP2000056594A 2000-03-02 2000-03-02 Vacuum carburizing method and carburizing furnace for implementing the method Expired - Lifetime JP3321732B2 (en)

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