JP2829148B2 - Atmosphere flow control device and control method in continuous annealing furnace - Google Patents

Atmosphere flow control device and control method in continuous annealing furnace

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Publication number
JP2829148B2
JP2829148B2 JP7631591A JP7631591A JP2829148B2 JP 2829148 B2 JP2829148 B2 JP 2829148B2 JP 7631591 A JP7631591 A JP 7631591A JP 7631591 A JP7631591 A JP 7631591A JP 2829148 B2 JP2829148 B2 JP 2829148B2
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JP
Japan
Prior art keywords
atmosphere
gas
zone
galvanic
flow
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 - Lifetime
Application number
JP7631591A
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Japanese (ja)
Other versions
JPH04311532A (en
Inventor
健一 八ケ代
政義 水口
泰光 近藤
洋一 財前
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
Nippon Steel Corp
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Publication date
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Priority to JP7631591A priority Critical patent/JP2829148B2/en
Publication of JPH04311532A publication Critical patent/JPH04311532A/en
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Publication of JP2829148B2 publication Critical patent/JP2829148B2/en
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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は連続焼鈍炉における雰囲
気流れ制御装置および制御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 an apparatus and a method for controlling an atmosphere flow in a continuous annealing furnace.

【0002】[0002]

【従来の技術】例えばストリップの連続焼鈍炉は、加熱
帯、均熱帯、冷却帯を連設されたものや、加熱帯、脱炭
帯、還元帯および冷却帯を連設されたものなどがある。
それぞれの帯域では所望の雰囲気ガスとされ、連続焼鈍
あるいは連続脱炭焼鈍が行われる。
2. Description of the Related Art For example, a continuous annealing furnace for a strip includes a heating zone, a soaking zone, and a cooling zone connected in series, and a heating zone, a decarburization zone, a reduction zone, and a cooling zone connected in series. .
In each zone, a desired atmosphere gas is set, and continuous annealing or continuous decarburizing annealing is performed.

【0003】表面性状を特に厳しく管理する必要がある
ストリップや、脱炭を必要とするものや更には鋼板表面
の酸化層を管理する必要があるストリップを連続焼鈍す
る場合には、例えば加熱帯、脱炭帯、還元帯各帯は所定
雰囲気例えば露点を特定範囲に維持されまた雰囲気ガス
組成中の特定成分は常に一定濃度に保持する等、前記各
帯域の処理目的に応じたものにする必要がある。
[0003] When continuously annealing strips requiring particularly strict control of the surface properties, strips requiring decarburization, and strips requiring control of an oxide layer on the surface of a steel sheet, for example, a heating zone, Each zone of the decarburization zone and the reduction zone must have a predetermined atmosphere, for example, a dew point is maintained in a specific range, and a specific component in the atmosphere gas composition is always kept at a constant concentration. is there.

【0004】かかることから、連続焼鈍炉における各帯
の境界には雰囲気仕切りが設けられ、炉内の雰囲気ガス
の混合を防ぐような提案がなされている。例えば特開昭
63−24038号公報では帯域境界に設けたシールボ
ックスに、搬送ロールに対向してシール体を昇降自在に
設け、シール体をストリップ板面に接触させて帯域間の
シールを行っている。雰囲気仕切りにより帯域間での雰
囲気混合が抑制されるが、シールロール等の経時劣化等
により依然として混じり合いがあり完全防止は出来ない
というのが実情である。
[0004] Therefore, it has been proposed to provide an atmosphere partition at the boundary of each zone in the continuous annealing furnace to prevent mixing of the atmosphere gas in the furnace. For example, in Japanese Patent Application Laid-Open No. 63-24038, a seal box provided at a zone boundary is provided with a seal body capable of moving up and down opposite to a transport roll, and the seal body is brought into contact with a strip plate surface to seal between zones. I have. Although the atmosphere partition suppresses the atmosphere mixing between the zones, the fact is that the mixing still occurs due to the deterioration of the seal roll and the like with the passage of time and the complete prevention cannot be performed.

【0005】また、連続焼鈍では炉内雰囲気ガスの露点
制御がなされている。例えば特開平2−80511号公
報では加湿ガスと乾ガスを混じえた混合ガスの合計流量
設定値とその露点温度および炉内雰囲気ガスの露点設定
値とから、加湿ガスと乾ガスの混合比を求めて各ガスの
流量を制御することにより、炉内雰囲気ガスの露点を制
御することが提案されている。これによると露点の制御
が正確になされ効果があるといわれている。
[0005] In the continuous annealing, the dew point of the atmosphere gas in the furnace is controlled. For example, in Japanese Patent Application Laid-Open No. 2-80511, a mixing ratio of a humidifying gas and a dry gas is determined from a total flow rate set value of a mixed gas obtained by mixing a humidified gas and a dry gas, a dew point temperature thereof, and a dew point set value of a furnace atmosphere gas. It has been proposed to control the dew point of the atmosphere gas in the furnace by controlling the flow rate of each gas. According to this, it is said that the control of the dew point is accurately performed, which is effective.

【0006】[0006]

【発明が解決しようとする課題】雰囲気仕切りの設定や
露点制御等により、炉内雰囲気の制御に一定の効果があ
るが、しかし、ストリップを連続焼鈍した際には脱炭が
ストリップの位置より不十分であったり、またストリッ
プに形成される酸化層が厚みむらや酸化量不足あるいは
過多を生じることがある。このような現象は製品板の品
質或いは表面性状やその後に形成された表面被膜に大き
く影響するから、かかる現象の発生を防ぐ必要がある。
本発明は被焼鈍ストリップに例えば均一な酸化層を板全
般にわたり形成し、また脱炭の位置による不良等が生じ
ない連続焼鈍を行うことを目的とする。
The setting of the atmosphere partition and the control of the dew point have a certain effect on the control of the furnace atmosphere. However, when the strip is continuously annealed, the decarburization is less than the strip position. In some cases, the thickness of the oxidized layer formed on the strip may be insufficient, and the thickness of the oxidized layer may be insufficient or the amount of oxidation may be insufficient or excessive. Since such a phenomenon greatly affects the quality or surface properties of a product plate and a subsequently formed surface coating, it is necessary to prevent the occurrence of such a phenomenon.
An object of the present invention is to form, for example, a uniform oxide layer on a strip to be annealed, over the entire plate, and to perform continuous annealing in which defects due to decarburization positions do not occur.

【0007】[0007]

【課題を解決するための手段】本発明者達は連続焼鈍に
おける前記脱炭や酸化層形成および表面性状等の均一化
とを図るべく検討したところ、炉内雰囲気ガスの流れが
大きく影響することをつきとめ、帯域内での雰囲気ガス
の流れを一定化するとよいことを知見した。本発明はは
この知見に基ずきなされたもので、その要旨は、雰囲気
仕切りで区画された複数の帯域を設けた連続焼鈍炉にお
ける雰囲気流れを制御するにあたり、帯域内に検流ガス
を注入する装置と、帯域の前部および後隣接帯域との雰
囲気仕切り部から流出雰囲気排気に混じる検流ガス濃度
を検出する装置と、帯域への雰囲気供給ガス量検出器
と、前記帯域内への注入検流ガス量と当該帯域前部の検
流ガス濃度検出器からの検出値と、後隣接帯域の雰囲気
仕切り部からの検流ガス濃度検出器の検出値を入力し帯
域の前流れおよび後流れ雰囲気流量を演算する装置と、
前記演算装置からの雰囲気前流流量と後流流量を比べそ
の差と許容値を比較し炉内雰囲気ガス流れを制御する装
置とからなることを特徴とする連続焼鈍炉における雰囲
気流れ制御装置とその制御方法にある。
Means for Solving the Problems The inventors of the present invention have studied to make the decarburization, the formation of the oxide layer, and the uniformity of the surface properties and the like in the continuous annealing, and found that the flow of the atmosphere gas in the furnace has a great effect. It was found that the flow of the atmosphere gas in the zone should be kept constant. The present invention is based on this finding, and the gist of the present invention is to control the atmosphere flow in a continuous annealing furnace provided with a plurality of zones partitioned by an atmosphere partition, and to inject a galvanic gas into the zone. , A device for detecting the concentration of a galvanic gas mixed with the exhaust gas discharged from the atmosphere partition between the front and rear adjacent zones of the zone, an atmosphere supply gas amount detector for the zone, and injection into the zone. Enter the detection gas volume, the detection value from the detection gas concentration detector in the front part of the zone, and the detection value of the detection gas concentration detector from the atmosphere partition part in the rear adjacent zone, and enter the pre-flow and post-flow in the zone. A device for calculating the atmospheric flow rate,
An atmosphere flow control device in a continuous annealing furnace, comprising: a device for comparing a difference and an allowable value between the atmosphere upstream flow rate and the downstream flow rate from the arithmetic unit and controlling the furnace atmosphere gas flow; and In the control method.

【0008】以下、本発明について一実施例に基づき図
面を参照して詳細に説明する。図面において、1は連続
焼鈍炉で、該炉はこの実施例では加熱帯2、均熱帯3、
徐冷帯4、および冷却帯5が設けられている。雰囲気仕
切り6は均熱帯3と徐冷帯4の間、徐冷帯4と冷却帯5
の間に設けられ、帯域内雰囲気ガスを仕切りしている。
Hereinafter, the present invention will be described in detail based on an embodiment with reference to the drawings. In the drawing, 1 is a continuous annealing furnace, which in this embodiment is a heating zone 2, a soaking zone 3,
A slow cooling zone 4 and a cooling zone 5 are provided. The atmosphere partition 6 is located between the solitary zone 3 and the slow cooling zone 4, and between the slow cooling zone 4 and the cooling zone 5.
And partition the atmosphere gas in the zone.

【0009】7は雰囲気ガス供給装置で、前記雰囲気仕
切り6で仕切られた各帯内にそれぞれ設けられている。
8は加熱帯2の前部に設けられた雰囲気排出口であり、
この実施例では加熱帯2が連続焼鈍炉1の最前部である
から該前部には雰囲気仕切りはなく、これに替えて雰囲
気排出口8が設けられている。9は雰囲気仕切り6部に
設けられている仕切り部雰囲気排出口である。これらに
は開閉調整器10がそれぞれ設けられ排気口の開閉度を
調整し排出流量を制御する。
Reference numeral 7 denotes an atmosphere gas supply device, which is provided in each zone partitioned by the atmosphere partition 6.
Reference numeral 8 denotes an atmosphere outlet provided at the front of the heating zone 2,
In this embodiment, since the heating zone 2 is the foremost part of the continuous annealing furnace 1, there is no atmosphere partition at the front part, and an atmosphere discharge port 8 is provided instead. Reference numeral 9 denotes a partition atmosphere discharge port provided in the atmosphere partition 6. These are provided with opening / closing regulators 10, respectively, for controlling the degree of opening / closing of the exhaust port and controlling the discharge flow rate.

【0010】11は検流ガス供給装置で、炉内雰囲気ガ
ス流れを検出するために検流ガス例えばストリップや他
のガスと反応しないHe等が供給される。該検流ガス供
給装置11はこの実施例は均熱帯3と徐冷帯4に設けて
いる例であり、その設置は任意の帯域にできる。
Reference numeral 11 denotes a galvanic gas supply device for supplying a galvanic gas, for example, He or the like which does not react with a strip or other gas, in order to detect a flow of the atmosphere gas in the furnace. The galvanic gas supply device 11 is an example in which the present embodiment is provided in the soaking zone 3 and the slow cooling zone 4, and the installation can be performed in any zone.

【0011】12は加熱帯2前部の雰囲気排出口8から
排出する雰囲気に混じる検流ガス濃度を検出する装置
で、例えば質量分析計等が採用される。12aは仕切り
部雰囲気排出口9から流出する雰囲気に混じる検流ガス
濃度検出装置である。
Reference numeral 12 denotes a device for detecting the concentration of a galvanic gas mixed with the atmosphere discharged from the atmosphere discharge port 8 at the front of the heating zone 2, and employs, for example, a mass spectrometer. Reference numeral 12a denotes a galvanic gas concentration detecting device which mixes with the atmosphere flowing out from the partition atmosphere discharge port 9.

【0012】13は炉内雰囲気ガスの前流れ・後流れ流
量を演算するとともに雰囲気流れを制御する演算装置
で、この実施例では検流ガス供給装置11からの加熱帯
2と均熱帯3内に注入された全ガス量VT 、あるいは検
流ガス流量VHEと、検流ガス濃度検出装置12からの加
熱帯前部より排気雰囲気ガスの検流ガス濃度C1 とか
ら、帯域の前流れ雰囲気流量V1と後流れ雰囲気流量V
2 を下記(1)式により演算し、また前記全ガス量
T 、あるいは検流ガス流量VHEと、検流ガス濃度検出
装置12aからの均熱帯3と徐冷帯4間の仕切り部雰囲
気排出口9における検流ガス濃度検出値C2 から加・均
熱帯2,3の後流れ雰囲気流量V2 と前流れ雰囲気流量
1 を下記(2)式により演算する。 V1 =(VHE/C1 ) −VHE,V2 =VT −V1 ・・・・・・(1) V2 =(VHE/C2 ) −VHE,V1 =VT −V2 ・・・・・・(2) 次いで前流れ雰囲気流量V1 と後流れ雰囲気流量V2
比べその差異と、設定あるいは学習による許容値と比較
し、許容値以下になるように雰囲気排出口8、仕切り部
雰囲気排出口9の開閉制御信号を出力する。前記開閉制
御信号により開閉調整器10の開閉度が制御され、本実
施例では加熱・均熱帯2,3内の雰囲気流れは全て加熱
帯前部側に向かうようにする。
Numeral 13 denotes an arithmetic unit for calculating the flow rate of the upstream and downstream flows of the atmospheric gas in the furnace and controlling the atmospheric flow. In this embodiment, the arithmetic unit 13 is located within the heating zone 2 and the soaking zone 3 from the galvanic gas supply device 11. From the total gas amount V T injected or the flow rate of the detected gas V HE and the detected gas concentration C 1 of the exhaust gas from the front of the heating zone from the detected gas concentration detector 12, the atmosphere in the upstream of the zone is determined. Flow rate V 1 and after-flow atmosphere flow rate V
2 is calculated by the following equation (1), and the total gas amount V T or the galvanic gas flow rate V HE and the atmosphere of the partition between the isotropy zone 3 and the slow cooling zone 4 from the galvanic gas concentration detecting device 12a. From the detected gas concentration C 2 at the discharge port 9, the after-flow atmosphere flow rate V 2 and the before-flow atmosphere flow rate V 1 are calculated by the following equation (2). V 1 = (V HE / C 1) -V HE, V 2 = V T -V 1 ······ (1) V 2 = (V HE / C 2) -V HE, V 1 = V T −V 2 (2) Next, the flow rate of the upstream flow rate V 1 is compared with the flow rate of the downstream flow rate V 2, and the difference is compared with an allowable value obtained by setting or learning. An opening / closing control signal for the outlet 8 and the partition atmosphere outlet 9 is output. The opening / closing degree of the opening / closing regulator 10 is controlled by the opening / closing control signal, and in the present embodiment, all the atmosphere flows in the heating / uniform tropics 2 and 3 are directed to the front side of the heating zone.

【0013】次ぎに制御方法について述べる。ストリッ
プは連続焼鈍炉1に加熱帯2側から通板され矢印の方向
に走行し焼鈍される。この実施例では加熱帯2、均熱帯
3には湿潤ガス例えばH2 ,N2 が供給されストリップ
は脱炭され、また該ストリップは板表面に酸化層が生じ
る。徐冷帯4ではドライガスにより冷却と酸化層への還
元作用をしている。
Next, the control method will be described. The strip is passed through the continuous annealing furnace 1 from the heating zone 2 side, travels in the direction of the arrow, and is annealed. In this embodiment, the heating zone 2 and the soaking zone 3 are supplied with a humid gas such as H 2 , N 2 and the strip is decarburized, and the strip has an oxide layer on the plate surface. In the slow cooling zone 4, cooling is performed by the dry gas and a reducing action to the oxide layer is performed.

【0014】ところで、炉内雰囲気ガス流れ、この実施
例では一方向化するように以下のようにする。連続され
ている加熱帯2、均熱帯3に検流ガスHeを注入し、徐
冷帯4には検流ガスHeを注入しない。この際、加熱帯
2、均熱帯3は湿潤ガスが、徐冷帯4にはドライガスが
供給されていて、雰囲気仕切り6は閉じられている。均
熱帯3から加熱帯前部側に流れる炉内雰囲気ガスは雰囲
気排出口8から炉外に流出するが、そのガス中の検流ガ
ス濃度C1 を検流ガス濃度検出装置12で検出する。
By the way, the atmosphere gas flow in the furnace, in this embodiment, is made as follows so as to be unidirectional. The galvanic gas He is injected into the continuous heating zone 2 and the soaking zone 3, and the galvanic gas He is not injected into the slow cooling zone 4. At this time, the heating zone 2 and the soaking zone 3 are supplied with wet gas, and the slow cooling zone 4 is supplied with dry gas, and the atmosphere partition 6 is closed. The atmosphere gas in the furnace flowing from the soaking zone 3 to the front side of the heating zone flows out of the furnace from the atmosphere discharge port 8, and the galvanic gas concentration C 1 in the gas is detected by the galvanic gas concentration detection device 12.

【0015】一方、徐冷帯4との境界の雰囲気仕切り6
側に流れる雰囲気ガス中の検流ガス濃度C2 は検流ガス
濃度検出装置12aで検出する。また加熱帯2、均熱帯
3に注入した検流ガスHeの量VHEは検流ガス供給装置
11から判明する。
On the other hand, the atmosphere partition 6 at the boundary with the slow cooling zone 4
Galvanometric gas concentration C 2 of the atmospheric gas flowing in the side is detected by galvanometric gas concentration detecting device 12a. Further, the amount V HE of the galvanic gas He injected into the heating zone 2 and the soaking zone 3 is known from the galvanic gas supply device 11.

【0016】前記検流ガス濃度検出値C1 ,C2 と検流
ガスVHEが演算装置13に入力され、前記式の演算がな
され、該帯2,3での前流れ雰囲気流量V1 と後流れ雰
囲気流量V2 を比べその差異値と、予め定めた許容値あ
るいは学習される許容値と比較し、差異値が大きいとき
は雰囲気の後流れが多いことで被焼鈍ストリップ対して
好ましくないから、雰囲気仕切り6の閉じ度を強め後流
れを減少させ可及的に前流れとする。
[0016] The galvanometer gas concentration detection value C 1, C 2 and galvanometric gas V HE is input to the arithmetic unit 13, the arithmetic of the equation is made, the pre-flow atmosphere flow rate V 1 of the in the band 2,3 Compare the after-flow atmosphere flow rate V 2 and compare the difference value with a predetermined allowable value or an allowable value to be learned. If the difference value is large, the after-flow of the atmosphere is large, which is not preferable for the strip to be annealed. Then, the degree of closure of the atmosphere partition 6 is increased to reduce the after-flow and make it as forward as possible.

【0017】このようにすることで、加熱帯2、均熱帯
3の雰囲気ガス流れは前流れとなり、被焼鈍ストリップ
はむらなく脱炭および酸化層が形成される。また、徐冷
帯4における雰囲気ガス流れを制御する場合は、当該徐
冷帯4に検流ガスを注入し、一方隣接の均熱帯3と冷却
帯5には検流ガスは注入せず、その後の制御は前述と同
様にすることがなされる。
By doing so, the atmosphere gas flow in the heating zone 2 and the soaking zone 3 becomes a pre-flow, and the strip to be annealed is uniformly decarburized and an oxide layer is formed. When controlling the atmosphere gas flow in the slow cooling zone 4, a galvanic gas is injected into the slow cooling zone 4, while a galvanic gas is not injected into the adjacent solitary zone 3 and the cooling zone 5. Is performed in the same manner as described above.

【0018】[0018]

【発明の効果】以上のように本発明によると、連続焼鈍
炉における炉内雰囲気ガスの流れが制御でき特に流れ向
きを一定化できるので、被焼鈍ストリップの炭素除去、
酸化層形成、還元等が安定してなされる。
As described above, according to the present invention, the flow of the atmosphere gas in the furnace in the continuous annealing furnace can be controlled, and particularly the flow direction can be made constant.
Oxide layer formation, reduction, etc. are performed stably.

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

【図1】本発明の一実施例を示す図。 1 連続焼鈍炉 2 加熱帯 3 均熱帯 4 徐冷帯 5 冷却帯 6 雰囲気仕切
り 7 雰囲気ガス供給装置 8 雰囲気排出
口 9 仕切り部雰囲気排出口 10 開閉調整器 11 検流ガス供給装置 12 検流ガス濃
度検出装置 12a 検流ガス濃度検出装置 13 演算装置
FIG. 1 is a diagram showing one embodiment of the present invention. DESCRIPTION OF SYMBOLS 1 Continuous annealing furnace 2 Heating zone 3 Uniform tropical zone 4 Slow cooling zone 5 Cooling zone 6 Atmosphere partition 7 Atmospheric gas supply device 8 Atmospheric discharge port 9 Partition section atmosphere discharge port 10 Opening / closing regulator 11 Detector gas supply device 12 Detector gas concentration Detector 12a Galvanic gas concentration detector 13 Arithmetic unit

───────────────────────────────────────────────────── フロントページの続き (72)発明者 財前 洋一 福岡県北九州市戸畑区飛幡町1番1号 新日本製鐵株式会社 八幡製鐵所内 (56)参考文献 特開 平2−236229(JP,A) 特開 昭62−250129(JP,A) 特開 昭57−63641(JP,A) 特開 昭53−22131(JP,A) (58)調査した分野(Int.Cl.6,DB名) C21D 1/74,1/76,9/52,9/56──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Yoichi Zaimae 1-1, Hibata-cho, Tobata-ku, Kitakyushu-shi, Fukuoka Nippon Steel Corporation Yawata Works (56) References JP-A-2-236229 (JP, A) JP-A-62-250129 (JP, A) JP-A-57-63641 (JP, A) JP-A-53-22131 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) ) C21D 1 / 74,1 / 76,9 / 52,9 / 56

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 雰囲気仕切りで区画された複数の帯域を
設け、雰囲気ガスが供給される連続焼鈍炉における炉内
雰囲気流れを制御する装置において、帯域内に検流ガス
を注入する装置と、帯域の前部および後隣接帯域との雰
囲気仕切り部から流出雰囲気排気に混じる検流ガス濃度
を検出する装置と、帯域への雰囲気供給ガス量検出器
と、前記帯域内への注入検流ガス量と当該帯域前部の検
流ガス濃度検出器からの検出値と、後隣接帯域の雰囲気
仕切り部からの検流ガス濃度検出器の検出値を入力し帯
域の前流れおよび後流れ雰囲気流量を演算する装置と、
前記演算装置からの雰囲気前流流量と後流流量を比べそ
の差異と許容値を比較し炉内雰囲気ガス流れを制御する
装置とからなることを特徴とする連続焼鈍炉における雰
囲気流れ制御装置。
1. A device for providing a plurality of zones partitioned by an atmosphere partition and controlling an atmosphere flow in a furnace in a continuous annealing furnace to which an atmosphere gas is supplied, wherein: a device for injecting a galvanic gas into the zone; A device for detecting the concentration of the galvanic gas mixed with the exhaust gas discharged from the atmosphere partitioning portion between the front and rear adjacent zones, an atmosphere supply gas amount detector for the zone, and an amount of the gas to be injected into the zone. The detection value from the galvanic gas concentration detector in the front part of the zone and the detection value from the galvanic gas concentration detector from the atmosphere partition part in the rear adjacent zone are input to calculate the upstream and downstream atmosphere flow rates in the zone. Equipment and
An atmosphere flow control device for a continuous annealing furnace, comprising: a device for comparing a difference between an upstream flow rate and a downstream flow rate of the atmosphere from the arithmetic unit and an allowable value to control the atmosphere gas flow in the furnace.
【請求項2】 雰囲気仕切りで区画された複数の帯域を
設けた連続焼鈍炉における炉内雰囲気流れを制御するに
あたり、帯域内に検流ガスを雰囲気ガス供給と別系統ま
たは共に注入し、帯域の前部から流出する検流ガス濃度
と後隣接帯域との雰囲気仕切り部から流出する検流ガス
濃度をそれぞれ検出し、該前方および後方の検流ガス濃
度検出値と帯域への検流ガス供給量から帯域内の雰囲気
前流流量と後流流量を演算し、その差異値と設定あるい
は学習される許容値と比較し、その大小により帯域の前
部あるいは後部の雰囲気排出口の開閉度を制御すること
を特徴とする連続焼鈍炉における雰囲気流れ制御方法。
2. In controlling a furnace atmosphere flow in a continuous annealing furnace provided with a plurality of zones partitioned by an atmosphere partition, a test gas is injected into the zone in a separate system or together with an atmosphere gas supply, The concentration of the galvanic gas flowing out of the front and the concentration of the galvanic gas flowing out of the atmosphere partition between the rear adjacent zone are detected, respectively, and the detected values of the galvanic gas concentrations at the front and rear and the amount of the galvanic gas supplied to the band are detected. Calculates the upstream flow rate and the downstream flow rate of the atmosphere in the zone, compares the difference value with the set or learned allowable value, and controls the degree of opening and closing of the atmosphere outlet at the front or rear of the zone according to the magnitude. Atmosphere flow control method in a continuous annealing furnace characterized by the above-mentioned.
JP7631591A 1991-04-09 1991-04-09 Atmosphere flow control device and control method in continuous annealing furnace Expired - Lifetime JP2829148B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7631591A JP2829148B2 (en) 1991-04-09 1991-04-09 Atmosphere flow control device and control method in continuous annealing furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7631591A JP2829148B2 (en) 1991-04-09 1991-04-09 Atmosphere flow control device and control method in continuous annealing furnace

Publications (2)

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JPH04311532A JPH04311532A (en) 1992-11-04
JP2829148B2 true JP2829148B2 (en) 1998-11-25

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