JPH05247529A - Continuous decarburization annealing method of grain-oriented silicon sheet - Google Patents
Continuous decarburization annealing method of grain-oriented silicon sheetInfo
- Publication number
- JPH05247529A JPH05247529A JP32314891A JP32314891A JPH05247529A JP H05247529 A JPH05247529 A JP H05247529A JP 32314891 A JP32314891 A JP 32314891A JP 32314891 A JP32314891 A JP 32314891A JP H05247529 A JPH05247529 A JP H05247529A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- partial pressure
- gas
- grain
- reaction
- 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.)
- Withdrawn
Links
Landscapes
- Manufacturing Of Steel Electrode Plates (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、炉内反応を効率的に且
つ安定的に行わしめる方向性電磁鋼板の連続脱炭焼鈍方
法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a continuous decarburizing and annealing method for grain-oriented electrical steel sheets which enables an in-furnace reaction to be carried out efficiently and stably.
【0002】[0002]
【従来の技術】ストリップ、例えば所定の板厚に冷間圧
延された方向性電磁鋼板は脱炭焼鈍される。該脱炭焼鈍
では、鋼中の炭素が除かれるとともに、鋼板表面に酸化
層が形成され、その鋼板に塗布される焼鈍分離剤と酸化
層が仕上焼鈍過程で反応しグラス被膜が形成される。2. Description of the Related Art Strips, such as grain-oriented electrical steel sheets cold-rolled to a predetermined thickness, are decarburized and annealed. In the decarburization annealing, carbon in the steel is removed, an oxide layer is formed on the surface of the steel sheet, and the annealing separator applied to the steel sheet and the oxide layer react in the finish annealing process to form a glass film.
【0003】脱炭焼鈍過程におけるこれらの脱炭、酸素
付加反応は、炉内に湿潤水素ガスを供給し、これにスト
リップを連続的に加熱、通板することで成され、各々の
反応は次に示すように炉内雰囲気中の水分と鋼板の接触
により生じる。 C+H2 O →CO+H2 Si+H2 O→SiO2 +2H2 該反応により鋼中の炭素は所定の値以下に下げる必要が
あり、また良好な製品のグラス被膜を得るためには酸素
付加量を所定の値とする必要があるが、このように反応
を狙い通りに、且つ安定して生じさせるためには、反応
に必要である雰囲気中の水分分圧を可能な目標の値に安
定して保つことが重要である。These decarburization and oxygen addition reactions in the decarburization annealing process are performed by supplying moist hydrogen gas into the furnace and continuously heating and stripping the strip, and each reaction is carried out as follows. As shown in Fig. 5, it is caused by the contact between the water in the furnace atmosphere and the steel sheet. C + H 2 O → CO + H 2 Si + H 2 O → SiO 2 + 2H 2 Due to the reaction, the carbon in the steel needs to be lowered to a predetermined value or less, and in order to obtain a glass film of a good product, the oxygen addition amount is set to a predetermined value. It is necessary to set a value, but in order to produce the reaction in a targeted and stable manner in this way, the water partial pressure in the atmosphere required for the reaction must be kept stable at a possible target value. is important.
【0004】こうした鋼板近傍の雰囲気中の水分のコン
トロールと安定化を図る方法として、従来から各種の方
法が提案されている。例えば、実開昭62−3381号
公報には炉内ストリップ近傍に雰囲気ガスを直接吹き付
けるパイプを配し、反応の安定化を図ることが可能であ
ることが開示されている。Various methods have heretofore been proposed as methods for controlling and stabilizing moisture in the atmosphere near the steel sheet. For example, Japanese Utility Model Laid-Open No. 62-3381 discloses that it is possible to stabilize the reaction by providing a pipe for directly blowing an atmospheric gas in the vicinity of the strip in the furnace.
【0005】[0005]
【発明が解決しようとする課題】しかしながら、このよ
うな現状の脱炭焼鈍方法においても雰囲気中の水分のコ
ントロールと安定化を達成するためには不充分である。
特に炉内反応により消費される炉内の雰囲気中の水分量
に比較して、供給ガス中の水分は十分に多いとは言え
ず、炉内の雰囲気ガス中水分の分圧は供給ガスの水分分
圧に比較して低下してしまうのが実状であり、鋼板の反
応性が変動すると炉内の露点も変動を生じる等不安定な
反応状態にあるのが実態である。更には、鋼板の反応状
態は炉長方向に変化しており、これに対して炉内への雰
囲気ガス及び、それに含まれる水分は、現状各ゾーンへ
均一に供給されているため、雰囲気ガス中の水分分圧は
炉長方向に分布を持つ状態となっており、先に述べた反
応の不安定性を一層助長する傾向にある。However, even such a current decarburization annealing method is insufficient for controlling and stabilizing the water content in the atmosphere.
In particular, compared to the amount of water in the atmosphere in the furnace consumed by the reaction in the furnace, it cannot be said that the water in the supply gas is sufficiently large, and the partial pressure of the water in the atmosphere gas in the furnace is The actual situation is that the pressure decreases compared to the partial pressure, and when the reactivity of the steel sheet changes, the dew point in the furnace also changes, which is an unstable reaction state. Furthermore, the reaction state of the steel sheet changes in the furnace length direction, whereas the atmospheric gas and moisture contained in the furnace are currently uniformly supplied to each zone. The partial pressure of water has a distribution in the furnace length direction, and tends to further promote the instability of the reaction described above.
【0006】[0006]
【課題を解決するための手段】本発明は、炉内で生じて
いる脱炭,酸化付加反応の不安定性、特に鋼板の反応状
態が焼鈍が進行するに従い変化するのに対し、現状各ゾ
ーンへの雰囲気ガス及び水分供給が一定であることに起
因して生じる炉内長手方向の水分分圧の分布を解消し、
反応の一層の安定化とコントロール化を図ることが可能
な脱炭焼鈍方法を提供するものである。According to the present invention, the instability of the decarburization and oxidative addition reactions occurring in the furnace, especially the reaction state of the steel sheet changes as the annealing progresses, whereas the present situation is Eliminates the distribution of water partial pressure in the longitudinal direction of the furnace caused by the constant supply of atmospheric gas and water,
It is intended to provide a decarburizing annealing method capable of further stabilizing the reaction and controlling the reaction.
【0007】すなわち本発明の要旨は、現状炉長方向に
複数に区切られた各ゾーンに加湿ガスを均一に供給して
いるのに対し、鋼板の脱炭,酸化反応の進行に伴う雰囲
気中水分の消費量の変化に対応して、一定の水分分圧に
加湿したガスの供給量を各ゾーンごとに調整する方法、
あるいは一定量供給しているガスの加湿水分量を各ゾー
ン毎に調整する方法であり、これらの何れかの方法を用
いて焼鈍炉内長手方向の水分分圧がほぼ一定となるよう
コントロールすることにある。That is, the gist of the present invention is that the humidifying gas is uniformly supplied to each zone divided into a plurality in the furnace length direction, whereas the moisture content in the atmosphere accompanying the progress of decarburization and oxidation reaction of the steel sheet. A method of adjusting the supply amount of gas humidified to a constant water partial pressure for each zone in response to changes in the consumption amount of
Alternatively, it is a method of adjusting the moisturizing water content of the gas being supplied at a fixed amount for each zone, and using any of these methods, control the water partial pressure in the longitudinal direction in the annealing furnace to be almost constant. It is in.
【0008】本発明について、図を用いて詳細に説明す
る。図1,図2は、本発明における脱炭焼鈍炉への雰囲
気ガス供給方法を模式的に示したものである。焼鈍炉1
の炉長方向に複数に分割された各ゾーンへ加湿器6,
7,8により加湿されたガスが供給される。炉内のガス
は、鋼板2に対抗して炉の前方へと流れ、排気ブリダー
3より排出される。鋼板2は炉内に入ると同時に、所定
の温度にまで加熱され、雰囲気中の水分との接触により
脱炭および酸化反応が始まる。これらの反応は反応開始
時において多量に反応し、多量の水分を消費するが反応
の進行とともに次第に反応量は減少し、水分の消費量も
少なくなる。The present invention will be described in detail with reference to the drawings. 1 and 2 schematically show a method for supplying an atmospheric gas to a decarburization annealing furnace according to the present invention. Annealing furnace 1
Humidifier to each zone divided into multiple in the furnace length direction
Gas humidified by 7, 8 is supplied. The gas in the furnace flows against the steel plate 2 toward the front of the furnace and is discharged from the exhaust bladder 3. At the same time as the steel sheet 2 enters the furnace, it is heated to a predetermined temperature, and when it comes into contact with moisture in the atmosphere, decarburization and oxidation reactions start. These reactions react in a large amount at the start of the reaction and consume a large amount of water, but the reaction amount gradually decreases as the reaction progresses, and the water consumption also decreases.
【0009】これらの反応による水分の消費量に対し
て、現状供給している雰囲気ガス中の水分量は、先述の
如く十分に多いとは言えず、供給ガスの水分分圧に比較
して炉内雰囲気中の水分分圧は低下することとなる。図
3は、炉内の雰囲気中の水分分圧の炉長方向分布を、現
状の操業方法Bと本発明Aとにおいて比較して示したも
のである。現状の炉長方向各ゾーンへの雰囲気ガス及び
水分量を均一に供給する方法においては、先に述べた反
応の炉長方向の不均一性に起因して点線Bのように炉前
部において水分分圧が低く、後部において高いといった
水分分圧の分布が生じることとなる。このような水分分
圧の分布中を経て処理された鋼板は、特に酸化反応にお
いて複雑な反応挙動を示し、これを推定,制御すること
は非常に困難である。The amount of water in the atmosphere gas currently being supplied is not sufficiently large as described above with respect to the amount of water consumed by these reactions. The water partial pressure in the internal atmosphere will decrease. FIG. 3 shows the distribution of water partial pressure in the furnace atmosphere in the furnace length direction in comparison between the current operating method B and the present invention A. In the current method of uniformly supplying the atmospheric gas and the amount of water to each zone in the furnace length direction, due to the nonuniformity of the reaction in the furnace length direction as described above, the water content in the front part of the furnace as shown by the dotted line B A distribution of water partial pressure is generated such that the partial pressure is low and the partial pressure is high in the rear part. A steel sheet treated through such a distribution of water partial pressure exhibits complicated reaction behavior particularly in an oxidation reaction, and it is very difficult to estimate and control this.
【0010】本発明者らは、炉内反応、特に酸化反応を
制御するためには炉内の雰囲気中水分分圧を炉長方向に
おいて可能な限り一定とし、反応の単純化を図ることが
重要と考え、2つの方法で具現化した。図1,2中4
は、炉内の水分分圧を測定する露点計であり、これによ
り炉長方向に水分分圧の分布状態を把握,コントロール
する。すなわち、図1は、加湿器6により一定水分分圧
に加湿し多ガスを露点計4により把握した炉内の反応状
態に応じてバルブ5により適正に分配(炉前部に多量
に、炉後部に少量に供給)し炉長方向の水分分圧の分布
を一定とする方法を示したものである。更に、図2は、
一例として7,8と2機の加湿器を用い、露点計4によ
り把握した炉内の反応状態に応じて各加湿器の水分加湿
量を適正に調整し炉長方向の水分分圧の分布を一定とす
る方法を示したものである。In order to control the reaction in the furnace, particularly the oxidation reaction, the present inventors make it important to keep the water partial pressure in the atmosphere of the furnace as constant as possible in the furnace length direction to simplify the reaction. I realized it in two ways. 4 in Figures 1 and 2
Is a dew point meter that measures the water partial pressure in the furnace, which allows the distribution state of the water partial pressure to be grasped and controlled in the furnace length direction. That is, FIG. 1 shows that the humidifier 6 humidifies the gas to a constant water partial pressure, and multiple gases are properly distributed by the valve 5 according to the reaction state in the furnace as grasped by the dew point meter 4 (a large amount in the front part of the furnace, a large amount in the rear part of the furnace). This is a method of making the distribution of the water partial pressure in the furnace length direction constant by supplying a small amount to the furnace. Furthermore, FIG.
As an example, using 7, 8 and 2 humidifiers, the moisture humidification amount of each humidifier is properly adjusted according to the reaction state in the furnace as grasped by the dew point meter 4, and the distribution of moisture partial pressure in the furnace length direction is calculated. This is a method of making the value constant.
【0011】これら供給ガス量の分配、及び供給ガスの
加湿量の調整の何れかの方法を用いることにより図3
中、実線Aに示したように炉長方向に一定の水分分圧,
分布を得ることが可能となり、反応の安定化,制御化に
大きな効果がある。By using any of these methods of distributing the supply gas amount and adjusting the humidification amount of the supply gas, FIG.
Medium, as shown by the solid line A, a constant water partial pressure in the furnace length direction,
It is possible to obtain a distribution, which is very effective in stabilizing and controlling the reaction.
【0012】[0012]
【発明の効果】以上述べたように、本発明によれば脱炭
焼鈍炉内の炉長方向の水分分圧の分圧を一定とすること
が可能となり、雰囲気の安定化に大きな効果がある。こ
の一定の水分分圧の雰囲気をベースに、炉内での脱炭,
酸化反応のコントロールをより高精度に行うことが可能
となり、狙い通りの中間品質を持った脱炭焼鈍板を得ら
れるようになることから、方向性電磁鋼板の製品の磁
性,被膜の向上に大きな効果がある。As described above, according to the present invention, the partial pressure of the water partial pressure in the furnace length direction in the decarburization annealing furnace can be made constant, which is very effective in stabilizing the atmosphere. . Decarburization in the furnace, based on the atmosphere of this constant moisture partial pressure,
It is possible to control the oxidation reaction with higher precision, and it is possible to obtain a decarburized annealed plate with the desired intermediate quality, which is a major improvement in the magnetic properties and coatings of grain-oriented electrical steel products. effective.
【図1】本発明による雰囲気ガス供給方法を示す模式図FIG. 1 is a schematic diagram showing an atmospheric gas supply method according to the present invention.
【図2】本発明による他の雰囲気ガス供給方法を示す模
式図FIG. 2 is a schematic diagram showing another atmospheric gas supply method according to the present invention.
【図3】焼鈍炉内の水分分圧の分布状態を従来法と本発
明とで比較して示す図。FIG. 3 is a diagram showing a distribution state of water partial pressure in an annealing furnace in comparison between a conventional method and the present invention.
1:焼鈍炉 2:鋼板 3:排気ブリーダー 4:露点計 5:流調バルブ 6,7,8:ガス加湿器 1: Annealing furnace 2: Steel plate 3: Exhaust bleeder 4: Dew point meter 5: Flow control valve 6, 7, 8: Gas humidifier
───────────────────────────────────────────────────── フロントページの続き (72)発明者 宮本 秀 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 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Hide Miyamoto 1-1, Toibata-cho, Tobata-ku, Kitakyushu-shi, Fukuoka New Nippon Steel Co., Ltd. Yawata Works
Claims (1)
長方向に複数に分割されたゾーンを持ち各ゾーンへ雰囲
気ガスを供給する焼鈍炉において、連続脱炭焼鈍するに
あたり、各ゾーンの炉内雰囲気ガス中の水分分圧がほぼ
一定となるように、各ゾーンへの加湿ガスの供給量、及
び各ゾーンへの供給ガスの加湿水分分圧を制御すること
を特徴とする方向性電磁鋼板の連続脱炭焼鈍方法。1. A continuous decarburizing annealing of a grain-oriented electrical steel sheet after cold rolling in a furnace having a plurality of zones in the furnace length direction and supplying an atmospheric gas to each zone. The directionality characterized by controlling the amount of humidified gas supplied to each zone and the humidified water partial pressure of the supplied gas to each zone so that the partial pressure of water in the furnace atmosphere gas is almost constant. Continuous decarburization annealing method for electrical steel sheets.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32314891A JPH05247529A (en) | 1991-12-06 | 1991-12-06 | Continuous decarburization annealing method of grain-oriented silicon sheet |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32314891A JPH05247529A (en) | 1991-12-06 | 1991-12-06 | Continuous decarburization annealing method of grain-oriented silicon sheet |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05247529A true JPH05247529A (en) | 1993-09-24 |
Family
ID=18151623
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32314891A Withdrawn JPH05247529A (en) | 1991-12-06 | 1991-12-06 | Continuous decarburization annealing method of grain-oriented silicon sheet |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH05247529A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013112823A (en) * | 2011-11-25 | 2013-06-10 | Jfe Steel Corp | Method and apparatus for controlling dew-point temperature |
KR20220114115A (en) * | 2021-02-08 | 2022-08-17 | 송형석 | Decarburization method of steel for manufacturing blades used in die cutting and device thereof |
-
1991
- 1991-12-06 JP JP32314891A patent/JPH05247529A/en not_active Withdrawn
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013112823A (en) * | 2011-11-25 | 2013-06-10 | Jfe Steel Corp | Method and apparatus for controlling dew-point temperature |
KR20220114115A (en) * | 2021-02-08 | 2022-08-17 | 송형석 | Decarburization method of steel for manufacturing blades used in die cutting and device thereof |
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