JPH0717942B2 - Atmosphere control method in continuous annealing furnace - Google Patents

Atmosphere control method in continuous annealing furnace

Info

Publication number
JPH0717942B2
JPH0717942B2 JP19689290A JP19689290A JPH0717942B2 JP H0717942 B2 JPH0717942 B2 JP H0717942B2 JP 19689290 A JP19689290 A JP 19689290A JP 19689290 A JP19689290 A JP 19689290A JP H0717942 B2 JPH0717942 B2 JP H0717942B2
Authority
JP
Japan
Prior art keywords
furnace
gas
zone
atmosphere
supplied
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.)
Expired - Fee Related
Application number
JP19689290A
Other languages
Japanese (ja)
Other versions
JPH0483818A (en
Inventor
喜志夫 久保
征司 谷本
忠良 藤坂
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.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP19689290A priority Critical patent/JPH0717942B2/en
Publication of JPH0483818A publication Critical patent/JPH0483818A/en
Publication of JPH0717942B2 publication Critical patent/JPH0717942B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、連続焼鈍炉における炉内雰囲気制御方法に関
する。
TECHNICAL FIELD The present invention relates to a furnace atmosphere control method in a continuous annealing furnace.

〔従来の技術〕[Conventional technology]

鋼管の焼鈍に使用される焼鈍炉として、ラジアントチュ
ーブからの輻射熱を用いた間接加熱方式の連続炉焼鈍が
ある。この焼鈍炉は、通常、炉体両端が開放され、炉内
が所定雰囲気に保持されるように、炉内に雰囲気ガスが
連続的に供給される。
As an annealing furnace used for annealing a steel tube, there is an indirect heating type continuous furnace annealing using radiant heat from a radiant tube. In this annealing furnace, both ends of the furnace body are normally opened, and atmospheric gas is continuously supplied into the furnace so that the inside of the furnace is maintained in a predetermined atmosphere.

ところで、焼鈍に供される鋼管が熱間で製造された場
合、その表層部には脱炭層が形成されていることが多
い。このような鋼管は、焼鈍の際にその雰囲気を浸炭雰
囲気とすることにより、脱炭層を除去することができ
る。
By the way, when a steel pipe used for annealing is manufactured hot, a decarburized layer is often formed in the surface layer portion. Such a steel pipe can remove the decarburized layer by making the atmosphere a carburizing atmosphere during annealing.

浸炭性の雰囲気ガスとしてはRXガスであり、特開昭52−
156707号公報には、炉体両端が閉塞された炉であるが、
RXガスをN2ガスで希釈した雰囲気ガスを炉内に供給する
炉内雰囲気制御方法が開示されている。この方法では、
加熱帯に導入する雰囲気ガスN2ガス量を高めてCO2の発
生を抑え、且つ炉出口側から炉入口側へ雰囲気ガスの強
制的な流れを形成して、加熱帯で発生したCO2を逐次排
出する。
RX gas is used as the carburizing atmosphere gas.
Japanese Patent No. 156707 discloses a furnace in which both ends of the furnace body are closed,
An in-furnace atmosphere control method is disclosed in which an atmosphere gas obtained by diluting RX gas with N 2 gas is supplied into the furnace. in this way,
The amount of atmospheric gas N 2 introduced into the heating zone is increased to suppress the generation of CO 2 , and a forced flow of atmospheric gas is formed from the furnace outlet side to the furnace inlet side to remove the CO 2 generated in the heating zone. Discharge sequentially.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

ところが、このような炉内雰囲気制御方法では、鋼管の
製造過程でその表層部に形成された脱炭層は充分に除去
されず、場合によっては組織が悪化するおそれもある。
それは、この方法では炉内全体が浸炭雰囲気になるから
である。
However, in such a furnace atmosphere control method, the decarburized layer formed in the surface layer portion of the steel pipe during the manufacturing process is not sufficiently removed, and in some cases the structure may deteriorate.
This is because this method creates a carburizing atmosphere throughout the furnace.

すなわち、炉内全体が浸炭雰囲気に保持されると、雰囲
気温度の低い加熱帯の前半部および冷却帯の後半部で
は、浸炭に寄与するはずのCが鋼管表面にススとなって
付着するために、表層部の浸炭が進まず、RXガスは無駄
になる。逆に、雰囲気温度が高い均熱帯近傍では、Cに
よって表層部の組織が悪化する危険性がある。
That is, when the entire furnace is maintained in a carburizing atmosphere, C, which should contribute to carburizing, adheres to the surface of the steel pipe as soot in the first half of the heating zone and the latter half of the cooling zone where the atmospheric temperature is low. The carburization of the surface layer does not proceed and the RX gas is wasted. On the contrary, in the vicinity of the soaking zone where the ambient temperature is high, there is a risk that C may deteriorate the structure of the surface layer.

このようなことから、表層部に脱炭層が形成された鋼管
を焼鈍過程で問題なく浸炭するためには、雰囲気温度が
高くも低くもない中間温度となる冷却帯の中間部乃至中
間部から前半部にかけての部分を強い浸炭雰囲気とし、
雰囲気温度が高い均熱帯や雰囲気温度が低い加熱帯およ
び冷却帯の後半部では平衡乃至は弱脱炭雰囲気としなけ
ればならない。
For this reason, in order to carburize a steel pipe with a decarburized layer formed on the surface layer without any problem during the annealing process, the ambient temperature is neither high nor low, and the intermediate temperature of the cooling zone is from the middle to the first half. Create a strong carburizing atmosphere in the part
Equilibrium or weak decarburization atmosphere should be used in the latter half of the soaking zone where the ambient temperature is high and the heating zone and the cooling zone where the ambient temperature is low.

本発明の目的は、かかる要求に答え、炉内長手方向の中
間温度部分のみを浸炭雰囲気とする連続焼鈍炉における
炉内雰囲気制御方法を提供することにある。
An object of the present invention is to provide a method for controlling the atmosphere in a continuous annealing furnace in a continuous annealing furnace in which only the intermediate temperature portion in the longitudinal direction of the furnace has a carburizing atmosphere in response to such a request.

〔課題を解決するための手段〕[Means for Solving the Problems]

連続焼鈍炉内の長手方向に所定の雰囲気分布を与える方
法として、RXガスとNXガスとの混合ガスを用い、炉内長
手方向の各ゾーンでその混合比を変える方法が考えられ
る。この方法で、冷却帯中間のゾーンにRXガスの最も濃
い混合ガスを供給し、そのゾーンから離れるに連れてRX
ガスの混合比率を低下させれば、焼鈍開始期には理想的
な雰囲気分布が得られるはずである。しかし、浸炭反応
の進むゾーンではその反応に伴ってCO2が生じ、焼鈍開
始から時間が経過するに連れて雰囲気ガスの浸炭能力が
低下する。そのため焼鈍開始期の後も所定の雰囲気分布
を維持し続けようとすると、雰囲気ガス供給量が著しく
増大し、ガス原単位の低下を招く。
As a method of giving a predetermined atmosphere distribution in the longitudinal direction in the continuous annealing furnace, a method of using a mixed gas of RX gas and NX gas and changing the mixing ratio in each zone in the longitudinal direction of the furnace can be considered. With this method, the densest mixture of RX gas is supplied to the zone in the middle of the cooling zone, and RX becomes more distant from that zone.
If the gas mixing ratio is lowered, an ideal atmosphere distribution should be obtained at the beginning of annealing. However, in the zone where the carburization reaction proceeds, CO 2 is generated along with the reaction, and the carburizing ability of the atmospheric gas decreases as time elapses from the start of annealing. Therefore, if it is attempted to maintain a predetermined atmosphere distribution even after the annealing start period, the supply amount of the atmosphere gas is remarkably increased, and the gas unit consumption is lowered.

本発明の第1の炉内雰囲気制御方法は、雰囲気ガスを節
減しつつ炉内長手方向の中間温度部分を浸炭雰囲気とす
るものであり、その特徴は、炉体両端が開放され、炉内
長手方向の各ゾーン毎に雰囲気ガスが独立供給される間
接加熱方式の連続焼鈍炉において、基本となる雰囲気ガ
スとしてNXガスを用いると共に、冷却帯に属し且つ雰囲
気温度が浸炭可能温度となる少なくとも1つのゾーンに
NXガスとRXガスとの混合ガスを供給し、当該ゾーンにお
ける雰囲気ガス供給量を他のゾーンにおける雰囲気ガス
供給量よりも大とする点にある。
A first method for controlling an atmosphere in a furnace of the present invention is to set a carburizing atmosphere at an intermediate temperature portion in a longitudinal direction of the furnace while reducing the atmosphere gas. In an indirect heating type continuous annealing furnace in which atmospheric gas is independently supplied to each zone in the direction, NX gas is used as the basic atmospheric gas, and at least one that belongs to the cooling zone and has an atmospheric temperature that allows carburization In the zone
The point is that a mixed gas of NX gas and RX gas is supplied, and the supply amount of atmospheric gas in the zone is made larger than the supply amount of atmospheric gas in other zones.

本発明の第2の炉内雰囲気制御方法は、第1の方法にお
いて、炉内長手方向の各ゾーン毎に炉内雰囲気のO2
度、CO濃度を測定し、その測定結果より算出した各ゾー
ン毎カーボンポンテンシャルが、あらかじめ各ゾーンに
設定された所定値となるように、混合ガスの混合比およ
び供給量を制御することを特徴としている。
A second furnace atmosphere control method according to the present invention is the first method, in which the O 2 concentration and CO concentration in the furnace atmosphere are measured for each zone in the furnace longitudinal direction, and each zone is calculated from the measurement results. It is characterized in that the mixing ratio and the supply amount of the mixed gas are controlled so that each carbon pontitial has a predetermined value set in advance in each zone.

〔作用〕[Action]

本発明の第1の方法では冷却帯に属し且つ雰囲気温度が
浸炭可能温度となる少なくとも1つのゾーンにRXガスと
NXガスとの混合ガスを供給することにより、中間温度部
分を浸炭雰囲気にできる。中間温度部分とは、温度が高
い部分(均熱帯)と温度が低い部分(加熱帯および冷却
帯の後半部)とを除いた部分である。冷却帯の浸炭可能
温度部分に混合ガスを供給することにより中間温度部分
が浸炭雰囲気になるのは、冷却帯に温度が高い部分は実
質的に存在せず、また、冷却帯の後半部のような低温部
分では浸炭が進行しないから、冷却帯で浸炭可能な温度
部分は中間温度部分に他ならないためである。しかも、
当該ゾーンでのガス供給量を他のゾーンでのガス供給量
に比して多くするので、当該ゾーンから炉入口および炉
出口の双方へ向かうガス流れが形成される。その結果、
浸炭反応に伴って生じたCO2が炉入口側および炉出口側
へ向かい、ガス流れの分岐点となる当該ゾーンの近傍で
所定の浸炭雰囲気が保持され続けると共に、そのゾーン
から離れるに連れて雰囲気ガスの浸炭能力が漸減する。
かくして、炉内長手方向の中間温度部分のみが浸炭雰囲
気になり、その部分から離れに連れて浸炭能力が低下す
るという理想的な雰囲気分布が、比較的少量のガス供給
で得られる。
In the first method of the present invention, RX gas is provided in at least one zone belonging to the cooling zone and having an ambient temperature at which the carburizable temperature is reached.
By supplying a mixed gas with NX gas, the intermediate temperature part can be made into a carburizing atmosphere. The intermediate temperature portion is a portion excluding a portion having a high temperature (soaking zone) and a portion having a low temperature (the latter half of the heating zone and the cooling zone). By supplying the mixed gas to the carburizable temperature portion of the cooling zone, the intermediate temperature portion becomes a carburizing atmosphere because there is substantially no high temperature portion in the cooling zone, and it seems that the latter half of the cooling zone. This is because carburization does not proceed in such a low temperature portion, so that the temperature portion where carburization is possible in the cooling zone is nothing but the intermediate temperature portion. Moreover,
Since the gas supply amount in the zone is made larger than the gas supply amounts in the other zones, a gas flow from the zone to both the furnace inlet and the furnace outlet is formed. as a result,
The CO 2 generated by the carburization reaction goes to the furnace inlet side and the furnace outlet side, and the predetermined carburizing atmosphere is maintained near the zone where the gas flow branches, and the atmosphere becomes more distant from the zone. The carburizing ability of gas gradually decreases.
Thus, an ideal atmosphere distribution in which only the intermediate temperature portion in the longitudinal direction of the furnace becomes the carburizing atmosphere, and the carburizing ability decreases with distance from the portion, is obtained with a relatively small amount of gas supply.

本発明の第2の方法では、浸炭能力の指標となるカーボ
ンポテンシャル炉内長手方向で所定分布に制御される。
In the second method of the present invention, the carbon potential is controlled to a predetermined distribution in the longitudinal direction in the carbon potential furnace, which serves as an index of carburizing ability.

〔実施例〕〔Example〕

以下に本発明の実施例を説明する。 Examples of the present invention will be described below.

全長60m、断面図5m22で、炉内長手方向で9ゾーンに分
割され、両端が開放された連続焼鈍炉で、0.5%C鋼よ
りなる外径63.5mm、肉厚5.9mm、全長15mのマンネスマン
鋼管を炉内移送速度1m/Hで焼鈍する際に、No.5,6,7ゾー
ンにNXガスとRXガスとの混合ガスを供給し、他のゾーン
にはNXガスのみを供給した。
A continuous annealing furnace with a total length of 60 m, a sectional view of 5 m 22 , divided into 9 zones in the longitudinal direction of the furnace, with both ends open. When the steel pipe was annealed at a transfer speed of 1 m / H in the furnace, a mixed gas of NX gas and RX gas was supplied to the No. 5, 6, and 7 zones, and only NX gas was supplied to the other zones.

混合ガスにおけるRXガス比は、第1図(a)に示すよう
に、No.5ゾーンでは20体積%、No.6ゾーンでは30体積
%、No.7ゾーンでは50体積%とした。また、ガス供給量
は総量が300N3/Hで、これを第1図(b)に示す比率で
各ゾーンに分配した。
The RX gas ratio in the mixed gas was 20% by volume in the No. 5 zone, 30% by volume in the No. 6 zone, and 50% by volume in the No. 7 zone, as shown in FIG. The total amount of gas supplied was 300 N 3 / H, which was distributed to each zone at the ratio shown in FIG. 1 (b).

すなわち、混合ガスが供給されるNo.5〜7ゾーンに供給
量を集中させ、RXガス比が最大のNo.7ゾーンに最大量の
雰囲気ガスを供給した。その結果、炉内ガスは、No.7ゾ
ーンから炉入口、炉出口の双方へ流れた。このときのヒ
ートパターンを第2図に、またカーボンポテンシャル分
布を第3図に示す。
That is, the supply amount was concentrated in the No. 5 to 7 zones where the mixed gas was supplied, and the maximum amount of the ambient gas was supplied to the No. 7 zone in which the RX gas ratio was the maximum. As a result, the furnace gas flowed from the No. 7 zone to both the furnace inlet and the furnace outlet. The heat pattern at this time is shown in FIG. 2, and the carbon potential distribution is shown in FIG.

第2図および第3図から分かるように、炉内雰囲気は、
冷却帯の中間に位置するNo.7ゾーンで最も強い浸炭能力
を示し、No.7ゾーンから離れるに連れて浸炭能力が低下
し、No.1〜5ゾーンでは平衡乃至は弱脱炭雰囲気になっ
た。その結果、焼鈍前に平均0.3mmの深さに形成されて
いた脱炭層は、焼鈍後には平均0.1mm以下の深さにまで
大幅に減少した。また、表層組織にCによる悪影響は認
められず、一方ススも無くRXガスが有効利用されたこと
も確認された。
As can be seen from FIGS. 2 and 3, the atmosphere in the furnace is
The No. 7 zone located in the middle of the cooling zone shows the strongest carburizing ability, the carburizing ability decreases as it moves away from the No. 7 zone, and the equilibrium or weak decarburizing atmosphere is established in the No. 1 to 5 zones. It was As a result, the decarburized layer that had been formed to an average depth of 0.3 mm before annealing was significantly reduced to an average depth of 0.1 mm or less after annealing. Further, it was also confirmed that the adverse effect of C on the surface layer structure was not observed, while the RX gas was effectively used without soot.

第4図は本発明の第2の方法を実施するのに適した制御
系のブロック図である。
FIG. 4 is a block diagram of a control system suitable for carrying out the second method of the present invention.

炉体1の各ゾーンには、制御弁2を介してRXガスが供給
され、制御弁3を介してNXガスが供給される。また、各
ゾーン雰囲気のCO濃度が計器4にて、O2濃度が計器5に
てそれぞれ測定される。CO濃度を測定する計器4として
は例えば赤外線式CO分析計があり、O2濃度を測定する計
器5としては例えばジルコニア固体電解質を用いた微量
酸素濃度計がある。
RX gas is supplied to each zone of the furnace body 1 through the control valve 2 and NX gas is supplied through the control valve 3. Further, the CO concentration and the O 2 concentration of each zone atmosphere are measured by the measuring instrument 4 and the measuring instrument 5, respectively. The instrument 4 for measuring the CO concentration is, for example, an infrared CO analyzer, and the instrument 5 for measuring the O 2 concentration is, for example, a trace oxygen concentration meter using a zirconia solid electrolyte.

測定されたCO濃度およびO2濃度は、雰囲気ガス供給制御
装置6に入力され、ここで下式によりカーボンポテンシ
ャルPcが算出される。
The measured CO concentration and O 2 concentration are input to the atmospheric gas supply control device 6, where the carbon potential Pc is calculated by the following equation.

Pco :CO濃度 Po2 :微量酸素濃度 K1 :平衡定数 K2 :補正係数 カーボンポテンシャルPc算出値は、当該ゾーンにおける
目標値と比較され、算出値を目標値に一致させるのに必
要な供給量および混合比が得られるように、制御弁2,3
の開度を制御する。これを全てのゾーンについて行い、
且つ焼鈍操業中に繰り返すことにより、炉内長手方向の
一部分のみが浸炭雰囲気とされた浸炭に好適な炉内雰囲
気分布が、操業の全期間を通じて高精度に得られる。
Pco: CO concentration Po 2 : Trace oxygen concentration K 1 : Equilibrium constant K 2 : Correction coefficient The carbon potential Pc calculated value is compared with the target value in the relevant zone, and the supply amount required to match the calculated value with the target value And control valves 2, 3
Control the opening of. Do this for all zones,
Further, by repeating during the annealing operation, a furnace atmosphere distribution suitable for carburizing in which only a part in the furnace longitudinal direction is a carburizing atmosphere can be obtained with high accuracy throughout the operation.

〔発明の効果〕〔The invention's effect〕

以上の説明から明らかなように、本発明の第1の炉内雰
囲気制御方法は、炉内長手方向の中間温度部分のみを浸
炭雰囲気とすることにより、Cの有効利用を図り、ガス
原単位を低減させることができる。また、Cの組織への
悪影響を防ぎ、優れた焼鈍品質を保証する。
As is clear from the above description, the first furnace atmosphere control method of the present invention achieves effective use of C by reducing the gas consumption rate by making only the intermediate temperature portion in the furnace longitudinal direction a carburizing atmosphere. Can be reduced. Further, it prevents the adverse effect of C on the structure and guarantees excellent annealing quality.

本発明の第2の炉内雰囲気制御方法は、炉体長手方向で
のカーボンポンテンシャル分布を高精度に制御すること
により、焼鈍操業の全期間を通じて高精度な雰囲気制御
を可能にする。
The second furnace atmosphere control method of the present invention enables highly accurate atmosphere control throughout the entire annealing operation by controlling the carbon Pontial distribution in the furnace longitudinal direction with high accuracy.

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

第1図(a)および(b)は本発明の第1の方法の実施
例におけるゾーン毎のRXガス比およびガス供給量を示す
図表、第2図および第3図は同じくヒートパターンおよ
びカーボンポテンシャル分布を示す図表、第4図は本発
明の第2の方法を実施するのに適した制御系のブロック
図である。 1:炉体、2,3:制御弁、4,5:計器、6:雰囲気ガス供給制御
装置。
FIGS. 1 (a) and 1 (b) are charts showing the RX gas ratio and gas supply amount for each zone in the embodiment of the first method of the present invention, and FIGS. 2 and 3 are the same heat pattern and carbon potential. FIG. 4 is a block diagram of a control system suitable for carrying out the second method of the present invention. 1: Furnace body, 2, 3: Control valve, 4,5: Instrument, 6: Atmosphere gas supply control device.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】炉体両端が開放され、炉内長手方向の各ゾ
ーン毎に雰囲気ガスが独立供給される間接加熱方式の連
続焼鈍炉において、基本となる雰囲気ガスとしてNXガス
を用いると共に、冷却帯に属し且つ雰囲気温度が浸炭可
能温度となる少なくとも1つのゾーンにNXガスとRXガス
との混合ガスを供給し、当該ゾーンにおける雰囲気ガス
供給量を他のゾーンにおける雰囲気ガス供給量よりも大
として、炉内長手方向の中間温度部分のみを浸炭雰囲気
とすることを特徴とする連続焼鈍炉における炉内雰囲気
制御方法。
1. In an indirect heating type continuous annealing furnace in which both ends of a furnace are opened and an atmospheric gas is independently supplied to each zone in the longitudinal direction of the furnace, NX gas is used as a basic atmospheric gas and cooling is performed. A mixed gas of NX gas and RX gas is supplied to at least one zone that belongs to the zone and the atmospheric temperature is a temperature at which carburization is possible, and the amount of atmospheric gas supplied in that zone is set larger than the amount of atmospheric gas supplied in other zones. A method for controlling an in-furnace atmosphere in a continuous annealing furnace, wherein a carburizing atmosphere is provided only in an intermediate temperature portion in a longitudinal direction of the in-furnace.
【請求項2】請求項1に記載の連続焼鈍炉における炉内
雰囲気制御方法において、炉内長手方向の各ゾーン毎に
炉内雰囲気のO2濃度、CO濃度を測定し、その測定結果よ
り算出した各ゾーンのカーボンポンテンシャルが、あら
かじめ各ゾーンに設定された所定値となるように、混合
ガスの混合比および供給量を制御することを特徴とする
炉内雰囲気制御方法。
2. The furnace atmosphere control method for a continuous annealing furnace according to claim 1, wherein the O 2 concentration and the CO concentration in the furnace atmosphere are measured for each zone in the furnace longitudinal direction and calculated from the measurement results. A method for controlling an atmosphere in a furnace, characterized in that the mixing ratio and the supply amount of the mixed gas are controlled so that the carbon potential of each zone becomes a predetermined value set in advance in each zone.
JP19689290A 1990-07-25 1990-07-25 Atmosphere control method in continuous annealing furnace Expired - Fee Related JPH0717942B2 (en)

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JPH0717942B2 true JPH0717942B2 (en) 1995-03-01

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