JP2906901B2 - Metal strip heating method in continuous metal strip processing line with direct-fired heating furnace - Google Patents

Metal strip heating method in continuous metal strip processing line with direct-fired heating furnace

Info

Publication number
JP2906901B2
JP2906901B2 JP3623393A JP3623393A JP2906901B2 JP 2906901 B2 JP2906901 B2 JP 2906901B2 JP 3623393 A JP3623393 A JP 3623393A JP 3623393 A JP3623393 A JP 3623393A JP 2906901 B2 JP2906901 B2 JP 2906901B2
Authority
JP
Japan
Prior art keywords
zone
direct
metal strip
pass
combustion
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
JP3623393A
Other languages
Japanese (ja)
Other versions
JPH06228658A (en
Inventor
宏次 大森
弘 澤田
孝哉 清家
清生 大森
直人 北川
秀峰 小林
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
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 Nippon Kokan Ltd filed Critical Nippon Kokan Ltd
Priority to JP3623393A priority Critical patent/JP2906901B2/en
Publication of JPH06228658A publication Critical patent/JPH06228658A/en
Application granted granted Critical
Publication of JP2906901B2 publication Critical patent/JP2906901B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

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

【0001】[0001]

【産業上の利用分野】この発明は、直火式加熱炉を有す
る金属帯連続処理ラインにおける金属帯加熱方法に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for heating a metal strip in a continuous metal strip processing line having a direct-fired heating furnace.

【0002】[0002]

【従来の技術】連続焼鈍炉等の金属帯の連続処理ライン
に設けられた直火式加熱炉では、各ゾーン毎の負荷設定
或いは各パス毎のパス入側又はパス出側の目標温度にな
るように、プリセット及び又はフィードバック加熱され
ていた。また1パスの炉の場合少なくとも最終ゾーンを
還元加熱ゾーンとし、2パスの炉の場合少なくとも2パ
ス目の最終ゾーンを還元加熱にしていた。更に2パス以
上の炉ではパス間のロール室での金属帯の酸化によるピ
ックアップを防止するために、ロール室の前即ち各パス
の最終ゾーンを還元加熱ゾーンとする技術があった。
2. Description of the Related Art In a direct-fired heating furnace provided in a continuous processing line for a metal strip such as a continuous annealing furnace, a load is set for each zone or a target temperature of a pass entrance side or a pass exit side of each pass is set. As such, the presets and / or feedback were heated. In the case of a one-pass furnace, at least the last zone is a reduction heating zone, and in the case of a two-pass furnace, at least the last zone of the second pass is reduction heating. Further, in a furnace having two or more passes, there is a technique in which a reduction heating zone is provided in front of the roll chamber, that is, the last zone of each pass in order to prevent pick-up due to oxidation of the metal band in the roll chamber between passes.

【0003】[0003]

【発明が解決しようとする課題】以上のような方法で
は、加熱負荷の設定、直火還元加熱ゾーンに入る金属帯
の温度、直火還元加熱バーナの形式と加熱温度が合致す
れば、酸化もなく、ロール室でのピックアップ発生を防
止できるものであった。しかしこの直火式加熱炉を含め
炉設備全体では金属帯最大熱処理量に対応できるように
設備設計されているために、金属帯の熱処理量が比較的
小さい場合、各パス入り側部分に設置してある加熱バー
ナは未燃焼状態となり、その領域を通過する金属帯は各
パス出側部分に設置してある加熱バーナの燃焼排ガスに
より加熱されることになる。
In the above-described method, if the setting of the heating load, the temperature of the metal zone entering the direct fire reduction heating zone, and the type of the direct fire reduction heating burner and the heating temperature match, the oxidation will be reduced. Thus, the occurrence of pickup in the roll chamber could be prevented. However, since the entire furnace equipment, including this direct-fired heating furnace, is designed to support the maximum heat treatment amount of the metal strip, if the heat treatment amount of the metal strip is relatively small, install it at each pass entry side. The heated burner is in an unburned state, and the metal strip passing through the area is heated by the combustion exhaust gas of the heating burner installed at each pass outlet side.

【0004】この時上記排ガスによる金属帯表面の酸化
は板温550℃以上で著しく、直火式加熱炉の最終ゾー
ンに設置された還元式加熱バーナで加熱しても金属帯表
面は酸化された状態で直火式加熱炉から排出され、該直
火式加熱炉に連接されたラジアントチューブ或いは電気
ヒータ等を用いた間接加熱炉或いは均熱炉において雰囲
気ガス中の水素濃度を増して、金属帯表面の還元を行う
必要があった。
At this time, the oxidation of the surface of the metal strip by the exhaust gas was remarkable at a plate temperature of 550 ° C. or more, and the surface of the metal strip was oxidized even when heated by a reduction heating burner installed in the last zone of the direct-fired heating furnace. The hydrogen concentration in the atmosphere gas is increased in an indirect heating furnace or a soaking furnace using a radiant tube or an electric heater connected to the direct-fired heating furnace and discharged from the direct-fired heating furnace in a state. The surface had to be reduced.

【0005】一方近年の製品の多様化(多品種、多サイ
ズ)、小ロット化に伴い、連続熱処理設備内にある金属
帯は複数種のものがある場合があり、その場合金属帯の
熱処理量はそのうち最も熱処理量の小さな金属によっ
て制約されるため、上記の金属帯表面の酸化が頻発して
発生するという問題があった。
On the other hand, with the recent diversification of products (multiple types, multiple sizes) and smaller lots, there are cases where there are a plurality of types of metal strips in the continuous heat treatment equipment. Is limited by the metal band having the smallest heat treatment amount, and thus there is a problem that oxidation of the surface of the metal band occurs frequently.

【0006】本発明は従来技術の以上のような問題に鑑
み創案されたもので、複数パスを有する直火式加熱炉に
おいて、ロール室及び直火式加熱炉出口で無酸化状態の
金属帯表面が得られるようにし、以てロール室及び直火
式加熱炉以降の炉に設置したロールへのピックアップを
防止するものである。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems of the prior art. In a direct-fired heating furnace having a plurality of passes, a non-oxidized metal strip surface is provided at a roll chamber and a direct-fired heating furnace outlet. Thus, pickup on a roll installed in a roll chamber and a furnace after the direct-fired heating furnace is prevented.

【0007】[0007]

【課題を解決するための手段】そのため本発明は、複数
パスを有し、それぞれのパスの各ゾーンには複数個の直
火加熱バーナを備え、少なくとも最終パスの最終ゾーン
は直火還元加熱ゾーンとし、金属帯の熱処理量の変化に
応じて生じる直火式加熱炉の総燃焼量の変化に対応させ
ながら最終パスから順に燃焼量を高くして各パスにお
ける燃焼量合計を決定すると共に、各パスの燃焼量合計
の範囲内で、隣接するゾーン相互のうち、後ゾーンの燃
焼量を前ゾーン以上にする傾斜加熱を行い、少なくとも
板温が高温域となる燃焼ゾーン以降に、未燃焼ゾーンを
形成させないように燃焼流量を調整したことを基本的特
徴としている。
Means for Solving the Problems] Therefore the present invention includes a plurality
It has a plurality of direct fire heating burners in each zone of each pass, and at least the final zone of the last pass is a direct fire reduction heating zone, and the direct fire generated according to the change in the heat treatment amount of the metal strip. while corresponding to the change in the total amount of combustion formula furnace, the final pass by increasing the combustion amount in the order and determines the combustion amount total in each pass, within the combustion amount totals for each path, adjacent zones mutually Of the rear zone fuel
Perform inclined heating to make the amount of firing more than the previous zone, at least
After the combustion zone where the plate temperature is high,
The basic feature is that the combustion flow rate is adjusted so that it is not formed .

【0008】[0008]

【作用】以上の構成では、金属帯の熱処理量の変化に応
じて直火式加熱炉の総燃焼量を変化させることで、その
サイズに合った加熱量を該金属帯に与え、またこの総燃
焼量の変化に対応させながら最終パスから燃焼量を順に
高くして各パスにおける燃焼量合計を決定すること、及
び各パスの燃焼量合計の範囲内で、隣接するゾーン相互
のうち、後ゾーンの燃焼量を前ゾーン以上にする傾斜加
熱を行い、少なくとも板温が高温域となる燃焼ゾーン以
降に、未燃焼ゾーンを形成させないように燃焼流量を調
整したことによって、全工程における加熱処理バランス
を取りつつ、金属帯を直火式加熱炉の出口から入口に向
けて連続的に加熱した時、金属帯表面の酸化が著しい高
温域で未燃焼状態となる加熱を行なうバーナが存在しな
くなり、また金属帯は低い温度から加熱開始されること
になる。そのために、たとえ加熱開始される前に未燃焼
状態の加熱バーナの領域を金属帯が通過する状態が発生
しても金属帯表面の酸化は非常に軽微となる。
In the above construction, by changing the total combustion amount of the direct-fired heating furnace in accordance with the change in the heat treatment amount of the metal strip, a heating amount suitable for the size is given to the metal strip. determining a combustion quantity total in turn increased to each pass the combustion amount from the final pass while corresponding to the change of the combustion amount, and within a range of combustion rate sum of each path, adjacent zones mutually
Out of the front zone, the amount of combustion
Heat is applied to at least the combustion zone where the plate temperature is in the high temperature range.
Lower the combustion flow rate so that no unburned zone is formed.
By the integer, while keeping the heat treatment balance in the entire process, when continuously heated toward the inlet of the metal strip from the exit of the direct flame heating furnace, unburned in significant high temperature range is oxidation of the metal strip surface burner is not present to perform the heating as the state and the metal strip will be initiated heated from low have temperature. For this reason, even if a state occurs in which the metal band passes through the region of the unburned heating burner before the start of heating, the oxidation of the metal band surface is very slight.

【0009】[0009]

【実施例】図1は金属帯1の連続焼鈍炉に設けられた直
火式加熱炉2における設備構成を示しており、以下2パ
スを有する直火式加熱炉2にて行われる本発明法の一実
施例に係る該金属帯1の加熱方法につき説明する。
FIG. 1 shows the construction of a direct-fired heating furnace 2 provided in a continuous annealing furnace for a metal strip 1, and the method of the present invention carried out in a direct-fired heating furnace 2 having two passes. A method of heating the metal strip 1 according to one embodiment will be described.

【0010】同図に示すように、炉外或いは予熱帯から
繋帯3aを経由した金属帯1はまず1パス目の直火式加
熱炉2a(#1〜#4ゾーン)に配置した加熱バーナ8
で加熱され、一旦繋帯3bを通り、2パス目の直火式加
熱炉2b(#5〜#8ゾーン)に配置した加熱バーナ8
で更に加熱された後、繋帯3cを通ってラジアントチュ
ーブ、電気ヒータ等により加熱、均熱保持する加熱帯或
いは均熱帯へ搬送され、焼鈍される。
As shown in FIG. 1, a metal strip 1 from outside the furnace or from a pre-tropical zone via a tie 3a is first heated by a heating burner disposed in a direct-fired heating furnace 2a (zones # 1 to # 4) in the first pass. 8
The heating burner 8 is disposed in the direct-fired heating furnace 2b (# 5 to # 8 zones) of the second pass, once passing through the tie 3b.
Is further heated through the tie 3c, and is conveyed to a heating zone or a solitary zone where the radiant tube, an electric heater or the like is used to heat and maintain a uniform temperature, and is annealed.

【0011】この金属帯1に所定の熱処理を施すため
に、規格、鋼種等からそのヒートパターンを金属帯条件
設定器12にて求め、図2に示すように、このヒートパ
ターンより直火式加熱炉2b出口の金属帯1の温度目標
値Taimを金属帯目標温度設定器11で決定し、その
値を金属帯温度調節器6に設定する。
In order to perform a predetermined heat treatment on the metal strip 1, its heat pattern is determined by a metal strip condition setting device 12 from a standard, a steel type, etc., and as shown in FIG. A target temperature Taim of the metal strip 1 at the outlet of the furnace 2b is determined by the target temperature setter 11 for metal strip, and the value is set in the temperature controller 6 for metal strip.

【0012】この金属帯温度調整器6では、直火式加熱
炉2b出口に設置した板温計5にて金属帯1の温度を計
測した現在の値Tactを入力し、その測定値Tact
と前記温度目標値Taimの比較を行い、直火式加熱炉
の総燃焼流量(操作量)Qaimを計算する。その操作
量とヒートパターンや金属帯サイズの金属帯条件から#
1〜#8ゾーンの各ゾーン毎に燃料流量目標値Qιai
m(ι=1〜8)を図3に示すような燃焼負荷パターン
から燃焼制御演算器7a〜7hで求めると共に、実際に
計測している(図1では省略)燃料流量の現在の測定値
Qιact(ι=1〜8)とその目標値Qιaimとを
比較して、ブロワ回転数或いは弁開度等の制御を行い、
各ゾーン(ι=1〜8)の燃料流量の調整を行なう。一
方使用している燃料の理論空気量と目標空気比とから各
ゾーン(ι=1〜8)毎の燃焼空気流量目標値Gιai
mを演算し、実際に各ゾーン毎に計測している(図1で
は省略)燃焼空気流量の測定値Gιactとこの目標値
Gιaimとを比較して、各ゾーン毎にブロワ回転数或
いは弁開度等の制御を行なって燃焼空気流量を調整す
る。
In the metal zone temperature controller 6, a current value Tact obtained by measuring the temperature of the metal zone 1 with a sheet thermometer 5 installed at the outlet of the direct-fired heating furnace 2b is input, and the measured value Tact
Is compared with the temperature target value Taim, and the total combustion flow rate (operating amount) Qaim of the direct-fired heating furnace is calculated. From the amount of operation and the heat band and the metal band condition of the metal band size #
Fuel flow target value Qιai for each of zones 1 to # 8
m (ι = 1 to 8) is obtained from the combustion load pattern as shown in FIG. 3 by the combustion control calculators 7a to 7h, and is actually measured (omitted in FIG. 1). (Ι = 1 to 8) and its target value Qιaim to control the blower rotation speed or the valve opening, etc.
The fuel flow rate in each zone (ι = 1 to 8) is adjusted. On the other hand, based on the theoretical air amount of the fuel used and the target air ratio, the target value of the combustion air flow rate Gιai for each zone (ι = 1 to 8)
m is calculated and actually measured for each zone (not shown in FIG. 1). The measured value Gιact of the combustion air flow rate is compared with this target value Gιaim, and the blower rotation speed or valve opening is set for each zone. And the like to adjust the combustion air flow rate.

【0013】ここで本実施例における燃焼負荷パターン
を前記図3を用いて説明する。1パス目の出口#4ゾー
ン及び2パス目の出口#8ゾーンは直火式加熱炉の総燃
料流量Qaim(操作量)に拘らず最小燃料流量以上で
燃焼させている。この操作量Qaimの増加に応じて2
パス目の出口の#8ゾーンより1パス目の入口の#1ゾ
ーンまで、隣接するゾーン相互のうち、後ゾーンの燃焼
量が前ゾーン以上となる傾斜加熱の燃焼負荷パターンを
保有している。
Here, the combustion load pattern in this embodiment will be described with reference to FIG. The exit # 4 zone of the first pass and the exit # 8 zone of the second pass burn at the minimum fuel flow rate or more regardless of the total fuel flow rate Qaim (operating quantity) of the direct-fired heating furnace. According to the increase of the operation amount Qim, 2
From the # 8 zone at the exit of the pass to the # 1 zone at the entrance of the first pass , the combustion of the rear zone among the adjacent zones
It has a combustion load pattern of inclined heating in which the amount is equal to or greater than the previous zone .

【0014】次に図4と図5及び図6を用いて本発明法
の第2実施例につき説明する。前記実施例の図1の構成
との違いは、前記実施構成では直火式加熱炉2bの出口
のみに設置した1つの金属帯温度調節器6で直火式加熱
炉全体の燃焼制御を行なっていたのに対し、図4に示す
本実施例構成では直火式加熱炉2a、2bの各パスの出
口に設置した夫々の金属帯温度調節器6aと6bによっ
て、各パスの直火式加熱炉を夫々燃焼制御している点で
ある。
Next, a second embodiment of the method of the present invention will be described with reference to FIG. 4, FIG. 5, and FIG. The difference from the configuration of FIG. 1 of the embodiment is that in the above-described embodiment, the combustion control of the entire direct-fired heating furnace is performed by one metal zone temperature controller 6 installed only at the outlet of the direct-fired heating furnace 2b. On the other hand, in the configuration of the present embodiment shown in FIG. 4, the direct-fired heating furnaces 2a and 2b are provided at the exits of the respective paths with the metal zone temperature controllers 6a and 6b, respectively. Are respectively controlled by combustion.

【0015】図4の設備構成と図5及び図6の制御フロ
ーに示されるように、1パス目の直火式加熱炉2aの出
口の金属帯1の温度目標値Taim1は#1〜#8ゾー
ンの各ゾーン毎の燃料流量を計測(図4では省略)した
測定値の和Qactを総燃料流量演算器10で求め、こ
の総燃料流量Qactより1パス目出口の金属帯目標温
度Taim1を図7に示すような金属帯目標温度設定パ
ターンから金属帯目標温度設定器11aで決定し、その
値を金属帯温度調節器6aに設定する。以降図8に基づ
く#1〜#4ゾーンの各ゾーン毎の燃料流量目標演算か
ら燃料流量調整及び燃焼空気流量調整までの方法は前述
した第1実施例と同じである。
As shown in the equipment configuration of FIG. 4 and the control flows of FIGS. 5 and 6, the target temperature Taim1 of the metal strip 1 at the outlet of the direct-fired heating furnace 2a in the first pass is # 1 to # 8. The total Qact of measured values obtained by measuring the fuel flow rate for each of the zones (omitted in FIG. 4) is obtained by the total fuel flow rate calculator 10, and the metal zone target temperature Taiim1 at the outlet of the first pass is calculated from the total fuel flow rate Qact. The target temperature setting unit 11a determines the target temperature from the metal band target temperature setting pattern shown in FIG. 7 and sets the value in the metal band temperature controller 6a. Hereinafter, the method from the fuel flow target calculation for each of the zones # 1 to # 4 based on FIG. 8 to the fuel flow rate adjustment and the combustion air flow rate adjustment is the same as in the first embodiment described above.

【0016】又2パス目の直火式加熱炉2bの出口の金
属帯温度目標値の決定から各ゾーン毎の燃料流量調節及
び燃焼空気流量調節までの方法も、前述した第1実施例
の場合と同様な方法で行われる。
The method from the determination of the target temperature of the metal zone at the outlet of the direct-fired heating furnace 2b in the second pass to the adjustment of the fuel flow rate and the combustion air flow rate for each zone is also the same as that of the first embodiment. Is performed in the same manner as described above.

【0017】ここで本実施例における金属帯目標温度設
定パターンについて図7を用いて説明する。この金属帯
目標温度設定パターンは、2パス目の#5〜#8ゾーン
の最大燃料流量の合計値と1パス目の出口の#4ゾーン
の最小燃料流量との和Qcと総燃料流量Qactとを比
較し、Qc>Qactとなる条件では、即ち2パス目全
ゾーンが最大燃料流量に到達するまでは金属帯目標温度
Taim1は400℃以下に設定し、逆にQc≦Qac
tとなる条件では、即ち2パス目全ゾーンが最大燃料流
量に到達した以降は金属帯目標温度Taim1は250
℃以上550℃以下の範囲で総燃料流量Qactの経過
に応じて目標温度Taim1を変化させている。この温
度設定パターンはヒートパターン、金属帯サイズを考慮
して複数のパターンが用意されている。
Here, the metal band target temperature setting pattern in this embodiment will be described with reference to FIG. This metal zone target temperature setting pattern is a sum Qc of the total value of the maximum fuel flow rates in zones # 5 to # 8 in the second pass and the minimum fuel flow rate in zone # 4 of the exit in the first pass, and the total fuel flow rate Qact. Under the condition that Qc> Qact, that is, until the entire zone in the second pass reaches the maximum fuel flow rate, the metal zone target temperature Taim1 is set to 400 ° C. or less, and conversely, Qc ≦ Qac
Under the condition t, that is, after all the zones in the second pass reach the maximum fuel flow rate, the metal zone target temperature Taim1 is 250
The target temperature Taim1 is changed in the range of not less than 550 ° C. and not more than 550 ° C. according to the progress of the total fuel flow rate Qact. As the temperature setting pattern, a plurality of patterns are prepared in consideration of a heat pattern and a metal band size.

【0018】以上のような方法を用いて鋼帯(炭素0.
04%の低炭素アルミキルド鋼)の加熱実験をした結果
を下記表1に示す。
Using the above method, a steel strip (carbon 0.
Table 1 shows the results of a heating experiment conducted on a low-carbon aluminum killed steel (04%).

【0019】[0019]

【表1】 [Table 1]

【0020】この実験では2パスを有する直火式加熱炉
が用いられており、1パス目は#1〜#4ゾーンで構成
され、#1〜#3ゾーンは非還元型加熱バーナが、又#
4ゾーンは還元型加熱バーナが用いられると共に、2パ
ス目は#5〜#8ゾーンで構成され、#5〜#7ゾーン
は非還元型加熱バーナが、更に#8ゾーンは還元型バー
ナが用いられ、空気比が0.86〜0.96の範囲に調
整されて行なわれている。
In this experiment, a direct-fired heating furnace having two passes is used. The first pass is composed of # 1 to # 4 zones, the # 1 to # 3 zones are non-reduction type heating burners, and #
In the fourth zone, a reduction heating burner is used, and in the second pass, zones # 5 to # 8 are used. In zones # 5 to # 7, a non-reduction heating burner is used. In the zone # 8, a reduction burner is used. The air ratio is adjusted in the range of 0.86 to 0.96.

【0021】鋼帯温度が500℃以上の高温域で鋼帯が
未燃焼ゾーンを通過するような加熱を実施した従来の方
法では、直火式加熱炉の出口で鋼帯表面の色が青色若し
くは濃紺色を呈し、酸化が観察されるのに対し、本実施
例では直火式加熱炉の出口においても無酸化状態で鋼帯
の加熱が終了しているのが観察された。
In the conventional method in which the steel strip is heated such that the steel strip passes through the unburned zone in a high temperature range of 500 ° C. or higher, the color of the steel strip surface is blue or blue at the outlet of the direct-fired heating furnace. In contrast to the dark blue color and oxidation observed, in this example, it was observed that the heating of the steel strip was completed in the non-oxidized state even at the outlet of the direct-fired heating furnace.

【0022】[0022]

【発明の効果】以上詳述した本発明法によれば、複数パ
スを有する直火式加熱炉において直火式加熱炉出口にお
いて無酸化状態の金属帯表面が得られるようになり、そ
の結果パスとパスを結ぶ繋帯に配置したロールへのピッ
クアップの発生も防止できるようになる。
According to the method of the present invention described in detail above, a non-oxidized metal strip surface can be obtained at the outlet of the direct heating furnace in the direct heating furnace having a plurality of passes. It is also possible to prevent occurrence of pickup on a roll arranged on a tie connecting the path and the path.

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

【図1】本発明法の実施が行われた2パスの直火式加熱
炉の側面図である。
FIG. 1 is a side view of a two-pass direct-fired heating furnace in which the method of the present invention is performed.

【図2】上記構成で行われた本発明法の制御フローを示
すフローチャート図である。
FIG. 2 is a flowchart showing a control flow of the method of the present invention performed with the above configuration.

【図3】本実施例で行われた加熱バーナの燃焼負荷パタ
ーンを示すグラフである。
FIG. 3 is a graph showing a combustion load pattern of a heating burner performed in the present embodiment.

【図4】本発明法の第2実施例が行われた2パスの直火
式加熱炉の側面図である。
FIG. 4 is a side view of a two-pass direct-fired heating furnace in which a second embodiment of the method of the present invention is performed.

【図5】上記構成で行われた本発明法の制御フローを示
すフローチャート図である。
FIG. 5 is a flowchart showing a control flow of the method of the present invention performed in the above configuration.

【図6】同じく上記構成で行われた本発明法の制御フロ
ーを示すフローチャート図である。
FIG. 6 is a flowchart showing a control flow of the method of the present invention performed in the same configuration.

【図7】本実施例における1パス目の出口の金属帯目標
温度設定パターンを示すグラフである。
FIG. 7 is a graph showing a metal band target temperature setting pattern at the exit of the first pass in the present embodiment.

【図8】本実施例における加熱バーナの燃焼負荷パター
ンを示すグラフである。
FIG. 8 is a graph showing a combustion load pattern of a heating burner in the present embodiment.

【符号の説明】[Explanation of symbols]

1 金属帯 2a、2b 直火式加熱炉 3a、3b、3c 繋帯 4 ロール 5、5a、5b 板温計 6、6a、6b 金属帯温度調節器 7a〜7h 燃焼制御演算器 8 直火式加熱バーナ 9 流量調整弁 10 総燃料流量演算器 11、11a、11b 金属帯目標温度設定器 12 金属帯条件設定器 DESCRIPTION OF SYMBOLS 1 Metal strip 2a, 2b Direct-fired heating furnace 3a, 3b, 3c Connecting 4 Roll 5, 5a, 5b Sheet thermometer 6, 6a, 6b Metal-zone temperature controller 7a-7h Combustion control calculator 8 Direct-fired heating Burner 9 Flow control valve 10 Total fuel flow calculator 11, 11a, 11b Metal band target temperature setting device 12 Metal band condition setting device

───────────────────────────────────────────────────── フロントページの続き (72)発明者 大森 清生 東京都千代田区丸の内一丁目1番2号 日本鋼管株式会社内 (72)発明者 北川 直人 東京都千代田区丸の内一丁目1番2号 日本鋼管株式会社内 (72)発明者 小林 秀峰 東京都千代田区丸の内一丁目1番2号 日本鋼管株式会社内 (56)参考文献 特開 昭54−83608(JP,A) (58)調査した分野(Int.Cl.6,DB名) C21D 1/52,9/52 C21D 9/56,11/00 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Kiyoo Omori 1-1-2 Marunouchi, Chiyoda-ku, Tokyo Nippon Kokan Co., Ltd. (72) Inventor Naoto Kitagawa 1-1-2 Marunouchi, Chiyoda-ku, Tokyo Japan Inside Kokan Co., Ltd. (72) Inventor Hidemine Kobayashi 1-2-1, Marunouchi, Chiyoda-ku, Tokyo Japan Kokan Co., Ltd. (56) References JP-A-54-83608 (JP, A) (58) Fields investigated Int.Cl. 6 , DB name) C21D 1 / 52,9 / 52 C21D 9 / 56,11 / 00

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 複数パスを有し、それぞれのパスの各ゾ
ーンには複数個の直火加熱バーナを備え、少なくとも最
終パスの最終ゾーンは直火還元加熱ゾーンとし、金属帯
の熱処理量の変化に応じて生じる直火式加熱炉の総燃焼
量の変化に対応させながら最終パスから順に燃焼量を
高くして各パスにおける燃焼量合計を決定すると共に、
各パスの燃焼量合計の範囲内で、隣接するゾーン相互の
うち、後ゾーンの燃焼量を前ゾーン以上にする傾斜加熱
を行い、少なくとも板温が高温域となる燃焼ゾーン以降
に、未燃焼ゾーンを形成させないように燃焼流量を調整
したことを特徴とする直火式加熱炉を有する金属帯連続
処理ラインにおける金属帯加熱方法。
The present invention has a plurality of passes, a plurality of direct heat heating burners in each zone of each pass, and a direct heat reduction heating zone at least in a final zone of a final pass, and a change in heat treatment amount of a metal strip. While corresponding to the change in the total combustion amount of the direct-fired heating furnace generated according to the above, the combustion amount is sequentially increased from the final pass to determine the total combustion amount in each pass,
Within the total combustion volume of each pass ,
Of which, inclined heating to make the combustion amount in the rear zone higher than that in the front zone
And at least after the combustion zone where the plate temperature is in the high temperature range.
The combustion flow rate so that no unburned zone is formed
A method for heating a metal strip in a continuous metal strip processing line having a direct-fired heating furnace.
JP3623393A 1993-02-02 1993-02-02 Metal strip heating method in continuous metal strip processing line with direct-fired heating furnace Expired - Lifetime JP2906901B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3623393A JP2906901B2 (en) 1993-02-02 1993-02-02 Metal strip heating method in continuous metal strip processing line with direct-fired heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3623393A JP2906901B2 (en) 1993-02-02 1993-02-02 Metal strip heating method in continuous metal strip processing line with direct-fired heating furnace

Publications (2)

Publication Number Publication Date
JPH06228658A JPH06228658A (en) 1994-08-16
JP2906901B2 true JP2906901B2 (en) 1999-06-21

Family

ID=12464061

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3623393A Expired - Lifetime JP2906901B2 (en) 1993-02-02 1993-02-02 Metal strip heating method in continuous metal strip processing line with direct-fired heating furnace

Country Status (1)

Country Link
JP (1) JP2906901B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111630192A (en) * 2018-02-22 2020-09-04 杰富意钢铁株式会社 Method for heating steel sheet in continuous annealing and continuous annealing apparatus

Also Published As

Publication number Publication date
JPH06228658A (en) 1994-08-16

Similar Documents

Publication Publication Date Title
JP2906901B2 (en) Metal strip heating method in continuous metal strip processing line with direct-fired heating furnace
JP4987689B2 (en) Direct-fired type roller hearth continuous heat treatment furnace
JP3356595B2 (en) Heating furnace combustion control method
JP2020128832A (en) Continuous heat treatment furnace
JP4223238B2 (en) Steel strip heating temperature control method
JP3328471B2 (en) Heating furnace combustion control method
CN108645233B (en) A method of it reduces and heats the time to be rolled
JP7354988B2 (en) Continuous steel heating furnace, air ratio control method for continuous steel heating furnace, and steel manufacturing method
JPH09241761A (en) Method for controlling pressure in continuous annealing furnace
JPH09170749A (en) Heating furnace and its operating method
JP2755089B2 (en) Combustion method for continuous heating furnace with regenerative burner
CN116536506A (en) Furnace pressure control method of atmosphere annealing furnace
CN113801985B (en) Hot-rolled plate blank heating variable-load type burner control method
JPH09280551A (en) Controlling method of combustion of heating furnace
JPH09111350A (en) Continuous heating furnace and operation thereof
JPH06108161A (en) Method for continuously annealing metal strip
JP2005300068A (en) Method for control of oxygen concentration and temperature of exhaust gas from rotary hearth reducing furnace
US3331594A (en) Method and apparatus for scale free heating of metals
JP2733885B2 (en) Continuous heat treatment of steel strip
JPH09173960A (en) Method for continuously drying and baking coating material
USRE26960E (en) Metal heating
JP2002220621A (en) Method for controlling furnace pressure using regenerative burner
JP2014037906A (en) Method for controlling combustion in annealing furnace
JPS5856736B2 (en) Steel strip heating method
JPH10251762A (en) Method for heating steel strip

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 19990302

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080402

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090402

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100402

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100402

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110402

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110402

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120402

Year of fee payment: 13

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130402

Year of fee payment: 14

EXPY Cancellation because of completion of term