JPS6070128A - Method for controlling temperature of strip with continuous annealing furnace - Google Patents

Method for controlling temperature of strip with continuous annealing furnace

Info

Publication number
JPS6070128A
JPS6070128A JP17826883A JP17826883A JPS6070128A JP S6070128 A JPS6070128 A JP S6070128A JP 17826883 A JP17826883 A JP 17826883A JP 17826883 A JP17826883 A JP 17826883A JP S6070128 A JPS6070128 A JP S6070128A
Authority
JP
Japan
Prior art keywords
heating zone
heating
temperature
zone
strip
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
JP17826883A
Other languages
Japanese (ja)
Other versions
JPS634608B2 (en
Inventor
Katsuya Suzuki
勝也 鈴木
Yasuo Ise
伊勢 保夫
Masahiro Shoji
政浩 庄司
Saburo Ito
三郎 伊藤
Akira Yokobari
横張 明
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP17826883A priority Critical patent/JPS6070128A/en
Publication of JPS6070128A publication Critical patent/JPS6070128A/en
Publication of JPS634608B2 publication Critical patent/JPS634608B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21DMODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D9/00Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
    • C21D9/52Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for wires; for strips ; for rods of unlimited length
    • C21D9/54Furnaces for treating strips or wire
    • C21D9/56Continuous furnaces for strip or wire

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Control Of Heat Treatment Processes (AREA)
  • Heat Treatment Of Strip Materials And Filament Materials (AREA)

Abstract

PURPOSE:To prevent temp. deviation of strips with a furnace consisting of a direct fire heating zone having excellent responsiveness and a radiant tube RT heating zone which does not have the excellent responsiveness by increasing preliminarily the temp. of the RT heating zone to a prescribed temp. CONSTITUTION:Plural strips with which heating load is different and which are required to increase the heating load in heating zones are passed through a continuous annealing furnace consisting of a direct fire heating zone 2 having excellent increasing and decreasing characteristics (responsiveness) of furnace temp. The temp. of the zone 3 is increased to the heating temp. which the strips require before the strips arrive at the annealing furnace. On the other hand, the temp. of the zone 2 is decreased by as much as the temp. is increased in the zone 3 so that the temp. of the strips now under annealing is maintained at the prescribed temp. The temp. of the zone 2 is then increased to the heating temp. that the strips require at the point of the time when the strips arrive at the annealing furnace.

Description

【発明の詳細な説明】 この発明は、連続焼鈍炉におけるストリップの板温度制
御方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for controlling the temperature of a strip in a continuous annealing furnace.

ストリップを連続焼鈍するに当フ、ストリップに、酸化
が生ずることのない光輝焼鈍を施すために、連続焼鈍炉
の加熱帯その他必要な炉帯に還元性のガスを流し、かつ
、その熱源として、ラジアントチューブ又は電気ヒータ
を使用することが知られている。このような連続焼鈍炉
の加熱帯は、ストリップへの熱伝達係数が比較的小さい
(30〜40 kA 7m” h℃)ので、生産性を高
めるためには、加熱帯の長さを長くした焼鈍炉を必要と
する。また、加熱帯は、熱容量が大きいために、炉温を
速やかに上昇又は降下させることができず、従って炉温
か設定値になる才でに時間を要する。そのために、現在
処理中のストリップに続いて、ストリップの品種を変更
し、寸法が大幅に異なるストリップ又はヒートサイクル
が大幅に異なるストリップを、連続して処理する際に、
品種変更後のストリップおよび変更前のストリップの相
当量に亘って、加熱帯での板温が適正値から外れた板温
外れが生ずる。
During continuous annealing of the strip, in order to subject the strip to bright annealing that does not cause oxidation, a reducing gas is passed through the heating zone of the continuous annealing furnace and other necessary furnace zones, and as a heat source, It is known to use radiant tubes or electric heaters. Since the heating zone of such a continuous annealing furnace has a relatively small heat transfer coefficient to the strip (30-40 kA 7m" h°C), it is necessary to annealing with a longer heating zone in order to increase productivity. Also, because the heating zone has a large heat capacity, it is not possible to quickly raise or lower the furnace temperature, and therefore it takes time for the furnace temperature to reach the set value. Following the strip being processed, when the strip variety is changed and strips with significantly different dimensions or heat cycles are successively processed,
The strip temperature in the heating zone deviates from the appropriate value for a considerable amount of the strip after the product type change and the strip before the change.

従来、板温外れを防止するためには、品種の変更前後の
ストリップの間に、複数コイルからなる接ぎ材を接続し
、接ぎ材が加熱帯を通過する間に、加熱帯の炉温を適正
値に上昇又は降下する方法が採られている。しかしなが
ら、この方法は、接ぎ材が無駄になって不経済である上
、接ぎ材の接続更して、ストリップの板温を制御し、板
温外れを防止する方法が種々提案されている(特開昭5
1−86009号、特開昭52−28409号、特開昭
52−28412号および特開昭52−29410号)
が、生産速度を低下させることなく、且つ、板温外れが
生ぜずに制御する点において、必ずしも十分とは言えな
かった。
Conventionally, in order to prevent plate temperature deviation, a joint material made of multiple coils was connected between the strips before and after changing the product type, and while the joint material passed through the heating zone, the furnace temperature of the heating zone was adjusted to the appropriate temperature. A method is adopted in which the value increases or decreases. However, this method wastes the joint material and is uneconomical. In addition, various methods have been proposed for connecting the joint material, controlling the strip temperature, and preventing the board temperature from deviating (in particular, Kaisho 5
1-86009, JP-A-52-28409, JP-A-52-28412 and JP-A-52-29410)
However, it was not necessarily sufficient in terms of controlling the production speed without reducing the production speed and without causing deviation in plate temperature.

この発明は、上述の現状に鑑み、ストリップの品種を変
更するに際して、板温外れを生ずることなく、高効率に
焼鈍処理することのできる、連続焼鈍炉におけるストリ
ップの板温制御方法を提供するものであって、加熱帯が
直火加熱帯とラジアントチューブ加熱帯とから構成され
ている連続焼鈍炉に、加熱帯での加熱負荷を増加する必
要がある、加熱負荷の異なる複数種類のストリップを連
続的に通して連続焼鈍するに当り、前記加熱負荷の異な
るストリップが焼鈍炉に到達する前に、前記ラジアント
チューブ加熱帯の炉温を、前記加熱負荷の異なるストリ
ップが必要とする加熱温度まで上昇し、一方、前記直火
加熱帯の炉温を、前記ラジアントチューブ加熱帯の炉温
上昇分だけ降下して、現在焼鈍中のストリップの前記加
熱帯での板温を所定温度に保ち、次いで、前記加熱負荷
の異なるストリップが焼鈍炉に到達した時点で、前記直
火加熱帯の炉温を、前記加熱負荷の異なるス) IJツ
ゾが必要とする温度まで上昇し、かくして、前記加熱負
荷の異なるス) Uツブの前記加熱帯における板温を所
定温度に制御することに特徴を有する。
In view of the above-mentioned current situation, the present invention provides a method for controlling the plate temperature of a strip in a continuous annealing furnace, which allows highly efficient annealing without causing deviation in plate temperature when changing the type of strip. In this continuous annealing furnace, the heating zone is composed of an open flame heating zone and a radiant tube heating zone, and multiple types of strips with different heating loads are continuously applied to the continuous annealing furnace, which requires an increase in the heating load in the heating zone. During continuous annealing throughout the process, before the strips with different heating loads reach the annealing furnace, the furnace temperature of the radiant tube heating zone is increased to the heating temperature required by the strips with different heating loads. , On the other hand, the furnace temperature of the direct fire heating zone is lowered by the furnace temperature increase of the radiant tube heating zone to maintain the plate temperature of the strip currently being annealed in the heating zone at a predetermined temperature; When the strips with different heating loads reach the annealing furnace, the furnace temperature of the direct-fired heating zone is increased to the temperature required by the IJ tube with the different heating loads, thus B) It is characterized in that the plate temperature in the heating zone of the U-tube is controlled to a predetermined temperature.

以下、この発明の方法を詳述する。The method of this invention will be explained in detail below.

第1図は、この発明の板温制御方法に用いられる連続焼
鈍炉の構成例を示したものである。第1図において、■
は与熱帯、2は直火加熱帯、3はRT加熱帯(ラジアン
トチューブ加熱帯)、4はRT均熱帯(ラジアントチュ
ーブ均熱帯)、5は冷却帯、6はシェルフ帯、7は調整
冷却帯であり、ラジアントチューブ帯をRT加熱帯3と
RT均熱帯4とに分け、このRT加熱帯3と直火加熱帯
2とで焼鈍炉の加熱帯を構成している。直火加熱帯2で
の加熱法としては、無酸化炉方式、輝炎輻射管方式等が
ある。なお、第1図は縦型焼鈍炉の構成例を示したが、
横型の焼鈍炉においても、同様な加熱帯構成とする。
FIG. 1 shows an example of the configuration of a continuous annealing furnace used in the plate temperature control method of the present invention. In Figure 1, ■
is the heating zone, 2 is the direct heating zone, 3 is the RT heating zone (radiant tube heating zone), 4 is the RT soaking zone (radiant tube soaking zone), 5 is the cooling zone, 6 is the shelf zone, and 7 is the adjustment cooling zone. The radiant tube zone is divided into an RT heating zone 3 and an RT soaking zone 4, and the RT heating zone 3 and the direct flame heating zone 2 constitute the heating zone of the annealing furnace. Heating methods in the direct flame heating zone 2 include a non-oxidizing furnace method, a bright flame radiation tube method, and the like. Although Fig. 1 shows an example of the configuration of a vertical annealing furnace,
A similar heating zone configuration is used in the horizontal annealing furnace.

第1図および第2図に示すように、連続焼鈍炉に導かれ
たストリップLは、予熱帯1でST、の温度に予熱され
たのち、直火加熱帯2でST、に、そして、RT加熱帯
3でST2の温度に加熱される。次いでストリップLは
、RT均熱帯4でST3の温度に均熱され、冷却帯5で
ST、の温度まで冷却されたのチ、シェルフ帯6でST
、の温度でシェルフ処理が施され、調整冷却帯7でST
、の温度まで調整冷却される。
As shown in FIGS. 1 and 2, the strip L led to the continuous annealing furnace is preheated to a temperature ST in a preheating zone 1, then heated to ST in a direct heating zone 2, and then to RT. It is heated in the heating zone 3 to a temperature of ST2. The strip L is then soaked in an RT soaking zone 4 to a temperature of ST3, cooled in a cooling zone 5 to a temperature of ST, and then in a shelf zone 6 to a temperature of ST.
The shelf treatment is performed at a temperature of , and the ST
, and is cooled down to a temperature of .

上述した連続焼鈍炉において、加熱帯での加熱負荷の異
なるストリップ、すなわち、寸法又はヒートサイクルの
異なるストリップを、連続的に通して焼鈍する際におけ
るストリップの板温制御は、次のようにして行なわれる
。すなわち、加熱帯は、炉温の上昇性および降下性(以
下応答性と称す)に優れた直火加熱帯2と、炉温の応答
性に劣るRT加熱帯3とから構成されているので、加熱
負荷の減少を必要とする場合には、第3図に示すように
、直火加熱帯での板温ST、を例えばST、’に下げて
、RT加熱帯での板温ST2をST2′にすればよい。
In the above-mentioned continuous annealing furnace, strip plate temperature control when continuously annealing strips with different heating loads in the heating zone, that is, strips with different dimensions or heat cycles, is performed as follows. It will be done. That is, the heating zone is composed of the direct-fire heating zone 2, which is excellent in raising and lowering the furnace temperature (hereinafter referred to as responsiveness), and the RT heating zone 3, which is poor in the responsiveness of the furnace temperature. When it is necessary to reduce the heating load, as shown in Fig. 3, the plate temperature ST in the open heating zone is lowered to, for example, ST,', and the plate temperature ST2 in the RT heating zone is reduced to ST2'. Just do it.

一方、加熱負荷の増加を必要とする場合は、ストリツゾ
に酸化が生ずる点から、直火加熱帯での板温上昇には限
界があり、第3図に示すように、直火加熱帯での板温S
T1を例えばST、’に上げて、RT加熱帯での板温S
T2をST2″にすることができない。
On the other hand, when it is necessary to increase the heating load, there is a limit to the increase in plate temperature in the open heating zone because oxidation occurs in the strituzo, and as shown in Figure 3, there is a limit to the increase in plate temperature in the open heating zone. Board temperature S
Raise T1 to, for example, ST,' to increase the plate temperature S in the RT heating zone.
T2 cannot be set to ST2''.

そのために、応答性の劣るRT加熱帯で、板温を高くす
る必要がある。
Therefore, it is necessary to increase the plate temperature in the RT heating zone, which has poor responsiveness.

そこで、この発明では、加熱負荷の増加を次のようにし
て行なう。
Therefore, in the present invention, the heating load is increased as follows.

(1)まず、次に焼鈍すべき加熱負荷の異なるストリッ
プの寸法、ヒートサイクルおよび目標ライン速度より、
前記次のストリップの直火加熱帯での目標板温STI“
およびRT加熱帯での目標板温ST2#を算出し、さら
に、ストリップをこの板温ST2″まで上昇させるのに
必要なRT加熱帯炉温* T2 およびその炉温T−に昇温するまでに要する時間
τを算出する。
(1) First, from the dimensions of the strip with different heating loads to be annealed, the heat cycle and the target line speed,
Target plate temperature STI in the direct flame heating zone of the next strip
and the target plate temperature ST2# in the RT heating zone, and further calculate the RT heating zone furnace temperature* T2 necessary to raise the strip to this plate temperature ST2'' and the time required to raise the temperature to the furnace temperature T-. Calculate the required time τ.

(2) 次に、第4図に示すように、前記次のストリッ
プが焼鈍炉に到達するまでに、RT加熱帯の炉温T2が
前記炉温T2*に上昇するように、前記昇温に要する時
間τをみこしてRT加熱帯の炉温T2を前記炉温T2 
に設定する。RT加熱帯炉温T2は、時間τの経過と共
に徐々に上昇し、時間τの間に前記次のストリップに必
要とされる温度T2*になる。
(2) Next, as shown in FIG. 4, the temperature is increased so that the furnace temperature T2 of the RT heating zone rises to the furnace temperature T2* by the time the next strip reaches the annealing furnace. Taking into account the required time τ, the furnace temperature T2 of the RT heating zone is set to the furnace temperature T2.
Set to . The RT heating zone furnace temperature T2 gradually increases with the passage of time τ and reaches the temperature T2* required for the next strip during time τ.

(3)一方、RT加熱帯炉温T2の上昇によって、現在
焼鈍中のストリップの、RT加熱帯での板温ST2が変
化しないように、RT加熱帯炉温T2の上昇に応じて、
直火加熱帯炉温を徐々に下げて、現在焼鈍中のストリッ
プの直火加熱帯での板温ST、を徐々に下げる。
(3) On the other hand, in order to prevent the plate temperature ST2 of the strip currently being annealed in the RT heating zone from changing due to the increase in the RT heating zone furnace temperature T2, in response to the increase in the RT heating zone furnace temperature T2,
The furnace temperature of the direct flame heating zone is gradually lowered, and the plate temperature ST of the strip currently being annealed in the direct flame heating zone is gradually lowered.

(4) 次いで、前記次のストリップが焼鈍炉に到達し
た時点で、第5図に示すように、直火加熱帯での次のス
トリップの板温を、ST、から上記(1,)でめた板温
S T、”に上昇させれば、前記次のストリップは、板
温か、直火加熱帯でST、”に、RT加熱帯で5T2I
f(に上昇されて、加熱負荷の増加がなされたことにな
る。
(4) Next, when the next strip reaches the annealing furnace, as shown in Fig. 5, the plate temperature of the next strip in the direct-fired heating zone is changed from ST to the temperature specified in (1) above. If the plate temperature is increased to ST, ”, the plate temperature is increased to ST, ” in the open flame heating zone, and 5T2I in the RT heating zone.
This means that the heating load has been increased.

上記(1)〜(4)のような、直火加熱帯およびRT加
熱帯でのストリップの板温制御によれば、予めRT加熱
帯の炉温か、加熱負荷の増加を必要とするストリップが
必要とする温度まで上昇されているので、前記次のスト
リップに対し、適切な焼鈍ができ、かつ、品種変更前の
ストリップに対する焼鈍にも影響を与えることがない。
According to the above (1) to (4), strip temperature control in the direct fire heating zone and RT heating zone requires a strip that requires an increase in the furnace temperature and heating load of the RT heating zone in advance. Since the temperature is raised to the specified temperature, the next strip can be appropriately annealed, and the annealing of the strip before the product type change is not affected.

従って、加熱負荷の増加を必要とするストリップへ品種
を変更するに際し、品種変更前後のストリップに板温外
れが生ずることなく、最大のライン速度で焼鈍できる。
Therefore, when changing the type of strip to one that requires an increase in heating load, the strip can be annealed at the maximum line speed without causing temperature deviation between the strip before and after the type change.

第6図は、この発明を実施するための、焼鈍炉の直火加
熱帯およびRT加熱帯に設けられた、制御システムの構
成例である。第6図において、8は制御装置で、制御装
置8には、直火加熱帯2の出口に設けられた直火加熱帯
出口板温度計9 、 RT加熱帯3の各加熱ゾーンに設
けられた炉温測定熱電対10. 、102・・・10n
およびRT加熱帯3の出口に設けられたRT加熱帯出口
板温度計11の信号が入力され、一方、制御装置8から
は、直火加熱帯板温調節計12′を介して直火加熱帯燃
焼装置12へ、RT加熱帯各加熱ゾーンの炉温調節計1
3.’。
FIG. 6 is a configuration example of a control system provided in a direct-fire heating zone and an RT heating zone of an annealing furnace for carrying out the present invention. In FIG. 6, 8 is a control device, and the control device 8 includes a direct flame heating zone outlet plate thermometer 9 provided at the outlet of the direct flame heating zone 2, and a direct flame heating zone outlet plate thermometer 9 provided in each heating zone of the RT heating zone 3. Furnace temperature measurement thermocouple 10. , 102...10n
A signal from the RT heating zone outlet plate thermometer 11 provided at the outlet of the RT heating zone 3 is inputted, and on the other hand, a signal from the control device 8 is input to the direct flame heating zone via a direct flame heating zone plate temperature controller 12'. Furnace temperature controller 1 for each RT heating zone to combustion device 12
3. '.

13□′・・・、13n′を介してRT加熱帯各加熱ゾ
ーンの燃焼装置13. 、13□・・・、13nへ、必
要な信号を出力する。制御装置8は、連続して通板され
るストリップの寸法、ヒートサイクル、材質およびライ
ン速度を常時管理し、上述した板温制御をする。
13□'..., 13n' to the combustion device 13. of each heating zone of the RT heating zone. , 13□..., 13n. The control device 8 constantly manages the dimensions, heat cycle, material, and line speed of the strip that is continuously passed, and performs the above-mentioned strip temperature control.

この発明は以上のように構成されるので、加熱帯での加
熱負荷を増加する必要があるストリップへ品種を変更す
るに際して、変更前後のストリップに板温外れが生ずる
ことなく、効率良く焼鈍処理をすることができる。
Since the present invention is configured as described above, when changing the type of strip to one that requires an increase in the heating load in the heating zone, the annealing process can be efficiently performed without causing deviation in plate temperature between the strip before and after the change. can do.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、この発明の板温制御方法に用いられる連続焼
鈍炉の構成図、第2図は、第1図の焼鈍炉におけるスト
リップ板温の一例を示すヒートサイクル図、第3図は、
加熱負荷の減少の方法を示すヒートサイクル図、第4図
は、この発明の板温制御方法を示す説明図、第5図は、
第4図の方法におけるヒートサイクル図、第6図は、こ
の発明の方法を実施するための制御システムのブロック
図である。 図面において、 2・・・直火加熱帯、3・・・RT加熱帯、4・・・R
T均熱帯。 出 願 人 日本鋼管株式会社 代 理 人 潮 谷 奈津夫(他2名)第1図  4 第2図 第3図 X1lI勢や
FIG. 1 is a block diagram of a continuous annealing furnace used in the sheet temperature control method of the present invention, FIG. 2 is a heat cycle diagram showing an example of the strip plate temperature in the annealing furnace of FIG. 1, and FIG.
A heat cycle diagram showing a method of reducing the heating load, FIG. 4 is an explanatory diagram showing the plate temperature control method of the present invention, and FIG.
FIG. 4 is a heat cycle diagram for the method, and FIG. 6 is a block diagram of a control system for implementing the method of the present invention. In the drawings, 2...Direct heating zone, 3...RT heating zone, 4...R
T isotropic zone. Applicant: Nippon Kokan Co., Ltd. Agent: Natsuo Shioya (and 2 others) Figure 1 4 Figure 2 Figure 3

Claims (1)

【特許請求の範囲】 加熱帯が直火加熱帯とラジアントチューブ加熱帯とから
構成されている連続焼鈍炉に、加熱帯での加熱負荷を増
加する必要がある、加熱負荷の異なる複数種類のストリ
ップを連続的に通して連続焼鈍するに当り、前記加熱負
荷の異なるストリップが焼鈍炉に到達する前に、前記ラ
ジアントチューブ加熱帯の炉温を、前記加熱負荷の異な
るストリップが必要とする加熱温度まで上昇し、一方、
前記直火加熱帯の炉温を、前記ラジアントチューブ加熱
帯の炉温上昇分だけ降下して、現在焼鈍中のストリップ
の前記加熱帯での板温を所定温度に保ち、次いで、前記
加熱負荷の異々るストリップ 1− が焼鈍炉に到達した時点で、前記直火加熱帯の炉温を、
前記加熱負荷の異なるス) リップが必要とする温度ま
で上昇し、かくして、前記加熱負荷の異なるストリップ
の前記加熱帯における板温を所定温度に制御することを
特徴とする連続焼鈍炉におけるストリップの板温制御方
法。
[Scope of Claims] A continuous annealing furnace in which the heating zone is composed of a direct flame heating zone and a radiant tube heating zone, and a plurality of types of strips with different heating loads, which require an increase in the heating load in the heating zone. During continuous annealing, the furnace temperature of the radiant tube heating zone is raised to the heating temperature required by the strips with different heating loads before the strips with different heating loads reach the annealing furnace. rise, while
The furnace temperature of the direct fire heating zone is lowered by the increase in furnace temperature of the radiant tube heating zone to maintain the plate temperature in the heating zone of the strip currently being annealed at a predetermined temperature, and then the heating load is reduced. When the different strips 1- reach the annealing furnace, the furnace temperature of the direct-fired heating zone is set to
A strip plate in a continuous annealing furnace characterized in that the temperature of the strip in the heating zone of the strip with different heating loads is increased to a required temperature, and thus the plate temperature in the heating zone of the strip with different heating loads is controlled to a predetermined temperature. Temperature control method.
JP17826883A 1983-09-28 1983-09-28 Method for controlling temperature of strip with continuous annealing furnace Granted JPS6070128A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17826883A JPS6070128A (en) 1983-09-28 1983-09-28 Method for controlling temperature of strip with continuous annealing furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17826883A JPS6070128A (en) 1983-09-28 1983-09-28 Method for controlling temperature of strip with continuous annealing furnace

Publications (2)

Publication Number Publication Date
JPS6070128A true JPS6070128A (en) 1985-04-20
JPS634608B2 JPS634608B2 (en) 1988-01-29

Family

ID=16045509

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17826883A Granted JPS6070128A (en) 1983-09-28 1983-09-28 Method for controlling temperature of strip with continuous annealing furnace

Country Status (1)

Country Link
JP (1) JPS6070128A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH046224A (en) * 1990-04-24 1992-01-10 Kawasaki Steel Corp Method for controlling temperature of continuous annealing furnace
JPH06184647A (en) * 1992-12-18 1994-07-05 Sumitomo Metal Ind Ltd Plate temperature control method in continuous furnace

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH046224A (en) * 1990-04-24 1992-01-10 Kawasaki Steel Corp Method for controlling temperature of continuous annealing furnace
JPH06184647A (en) * 1992-12-18 1994-07-05 Sumitomo Metal Ind Ltd Plate temperature control method in continuous furnace

Also Published As

Publication number Publication date
JPS634608B2 (en) 1988-01-29

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