JP2009235463A - Apparatus and method for continuously heating metal strip - Google Patents

Apparatus and method for continuously heating metal strip Download PDF

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JP2009235463A
JP2009235463A JP2008081241A JP2008081241A JP2009235463A JP 2009235463 A JP2009235463 A JP 2009235463A JP 2008081241 A JP2008081241 A JP 2008081241A JP 2008081241 A JP2008081241 A JP 2008081241A JP 2009235463 A JP2009235463 A JP 2009235463A
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flow rate
metal strip
mixing device
air
fuel gas
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Akihiro Nagahiro
昭浩 永廣
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JFE Steel Corp
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JFE Steel Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an apparatus and a method for continuously heating a metal strip which change oxidation and reduction in comparatively freely and in a wide range, according to the metal strip to be heated. <P>SOLUTION: Burner equipment 6 to be used in at least a downstream side in a direct fired heating furnace 2, has constitution in which premixed gas obtained by premixing fuel gas with air for combustion by a mixing device 7, is jetted from a nozzle 17. A flow rate detector and a flowing rate regulating valve are each arranged in fuel-system piping 9 for supplying the fuel gas into the mixing device 7, and in air-system piping 8 for supplying the air for combustion into the mixing device 7, and the flowing rate regulating valve is controlled so as to obtain the air ratio set according to the metal strip to be heated. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、連続焼鈍ラインや連続溶融亜鉛メッキラインなどの設備に設けられる、金属帯の連続加熱装置及び連続加熱方法に関する。   The present invention relates to a continuous heating apparatus and continuous heating method for a metal strip provided in facilities such as a continuous annealing line and a continuous hot dip galvanizing line.

従来の連続加熱装置としては、例えば特許文献1に記載の装置がある。この装置では、直火式加熱炉の最終ゾーンの加熱用として、予混合方式であるプレミックスバーナー設備を使用する。
この特許文献1に記載のプレミックスバーナー設備は、次のようになっている。
燃焼用空気を燃焼用空気配管を通じてミキシングバルブに供給すると共に、燃焼用空気配管には、空気コントロールバルブを介装しておく。また、燃料ガスを、燃料用ガス配管を通じてミキシングバルブに供給すると共に、その燃料用ガス配管に対し当該燃料用ガス配管内の圧が燃焼用空気配管と同圧となるように、ゼロバランスドレギュレータを介装しておく。
As a conventional continuous heating apparatus, there is an apparatus described in Patent Document 1, for example. In this apparatus, a premix burner facility that is a premixing system is used for heating the final zone of the direct-fired heating furnace.
The premix burner facility described in Patent Document 1 is as follows.
Combustion air is supplied to the mixing valve through the combustion air pipe, and an air control valve is interposed in the combustion air pipe. In addition, the fuel gas is supplied to the mixing valve through the fuel gas pipe, and the zero-balanced regulator is set so that the pressure in the fuel gas pipe is the same as that of the combustion air pipe. I will intervene.

そして、空気比設定値になるように空気比調節器でミキシングバルブのモーターをフィードバック制御して、ミキシングバルブにおける、燃料ガスと燃焼用空気との開口比を変化させることで空気比を一定に制御する。また、燃焼量の増減は、燃焼用空気配管に設置されている空気コントロールバルブを制御して行っていた。
なお、従来、直火加熱炉の最終ゾーンを還元域に制御している。
特許第2741617号公報
Then, feedback control of the mixing valve motor is performed with the air ratio adjuster so that the air ratio setting value is obtained, and the air ratio is controlled to be constant by changing the opening ratio between the fuel gas and the combustion air in the mixing valve. To do. In addition, the amount of combustion was increased or decreased by controlling an air control valve installed in the combustion air piping.
Conventionally, the final zone of the direct-fired heating furnace is controlled to the reduction zone.
Japanese Patent No. 2741617

しかし、上記従来例の構成にあっては、空気比を、ミキシングバルブの燃料ガスと燃焼用空気の開口比によって機械的に決めている要素が大きい。このため、オンラインによって、空気比を比較的自由に且つ広範囲に変更することが困難であった。
このため、連続加熱装置で加熱する金属帯の酸化還元を、加熱される金属帯に要求される性状に応じて広範囲に対応することが出来なかった。
本発明は、上記のような点に着目してなされたもので、加熱する金属帯に応じて、酸化還元を比較的自由に且つ広範囲に変更可能な金属帯の連続加熱装置及び方法を提供することを課題とする。
However, in the configuration of the above-described conventional example, there are many factors that mechanically determine the air ratio based on the opening ratio between the fuel gas of the mixing valve and the combustion air. For this reason, it has been difficult to change the air ratio relatively freely and in a wide range online.
For this reason, the oxidation-reduction of the metal strip heated by the continuous heating apparatus cannot be applied in a wide range according to the properties required for the heated metal strip.
The present invention has been made by paying attention to the above points, and provides a continuous heating apparatus and method for a metal strip in which oxidation and reduction can be changed relatively freely and in a wide range according to the metal strip to be heated. This is the issue.

上記課題を解決するために、本発明のうち請求項1に記載した発明は、連続して搬送される金属帯を加熱する直火式加熱炉を備えた連続加熱装置であって、
直火式加熱炉内の少なくとも下流側で使用するバーナー設備を、燃料ガスと酸素含有ガスとを予めミキシング装置で混合した予混合ガスをノズルから噴射させて燃焼する構成とすると共に、上記ミキシング装置に燃料ガスを供給する燃料系配管、及び上記ミキシング装置に酸素含有ガスを供給する空気系配管のそれぞれに、流量検出器及び流量調節弁を設け、加熱する金属帯に対応して設定された空気比となるように、上記流量検出器からの信号に基づき流量調節弁を制御する制御装置を備えたことを特徴とするものである。
In order to solve the above-mentioned problems, the invention described in claim 1 of the present invention is a continuous heating apparatus including a direct-fired heating furnace that heats a continuously conveyed metal strip,
Burner equipment used at least downstream in the direct-fired heating furnace is configured to inject and burn a premixed gas in which a fuel gas and an oxygen-containing gas are mixed in advance by a mixing device, and the mixing device. Air set to correspond to the metal strip to be heated by providing a flow rate detector and a flow rate control valve on each of the fuel system piping for supplying fuel gas to the air system piping for supplying oxygen-containing gas to the mixing device. A control device is provided for controlling the flow rate control valve based on a signal from the flow rate detector so as to obtain a ratio.

次に、請求項2に記載した発明は、連続して搬送される金属帯を直火式加熱炉で連続して加熱する金属帯の連続加熱方法であって、
直火式加熱炉内の少なくとも下流側での加熱を、燃料ガスと酸素含有ガスとを予めミキシング装置で混合した予混合ガスをノズルから噴出させて燃焼する構成とすると共に、上記ミキシング装置に供給する燃料ガス及び酸素含有ガスを個別の流量調節弁で調節し、加熱する金属帯に対応して設定された空気比となるように、上記流量調節弁を制御することを特徴とするものである。
Next, the invention described in claim 2 is a method for continuously heating a metal strip in which a continuously transported metal strip is continuously heated in a direct-fired heating furnace,
Heating at least downstream in the direct-fired heating furnace is configured such that a premixed gas in which fuel gas and oxygen-containing gas are mixed in advance by a mixing device is jetted from the nozzle and burned, and supplied to the mixing device. The fuel gas and the oxygen-containing gas are adjusted by individual flow rate control valves, and the flow rate control valve is controlled so that the air ratio is set corresponding to the metal band to be heated. .

本発明によれば、ゼロバランスドレギュレータを使用する代わりに、燃料ガス配管系統及び燃焼用空気配管系統に各々流量調節弁と流量検出器を設けることによって、各系統での流量調節を個別に可能とする。そして、各系統の流量検出器からの流量実績値に基づいて各流量調節弁を動作させることで空気比制御を行わせる。これによって、ミキシング装置に供給する燃料ガスと酸素含有ガスの流量を個別に調整可能とする結果、対応とする金属帯に合わせて、空気比制御が、比較的自由に且つ広範囲に変更することを可能となる。   According to the present invention, instead of using a zero-balanced regulator, by providing a flow control valve and a flow detector in each of the fuel gas piping system and the combustion air piping system, it is possible to individually control the flow rate in each system. And And air ratio control is performed by operating each flow control valve based on the flow actual value from the flow detector of each system. As a result, the flow rates of the fuel gas and oxygen-containing gas supplied to the mixing device can be individually adjusted. As a result, the air ratio control can be changed relatively freely and in a wide range according to the corresponding metal band. It becomes possible.

また、燃料ガスと酸素含有ガスをミキシング装置で予混合してノズルに供給するので、燃料ガスと酸素含有ガスとを均一に予混合可能となる。このため、炉内の酸化還元状態のばらつきを、その分、抑えることが出来る。すなわち目的とする酸化還元状態への安定した制御が可能となる。
すなわち、操業に応じて、直火式加熱炉内を酸化雰囲気にしたり還元雰囲気にしたりすることが容易にできる。
Further, since the fuel gas and the oxygen-containing gas are premixed by the mixing device and supplied to the nozzle, the fuel gas and the oxygen-containing gas can be premixed uniformly. For this reason, the variation in the oxidation-reduction state in the furnace can be suppressed accordingly. That is, stable control to the target oxidation-reduction state is possible.
That is, according to the operation, it is possible to easily make the inside of the direct-fired heating furnace into an oxidizing atmosphere or a reducing atmosphere.

次に、本発明の実施形態について図面を参照しつつ説明する。
図1は、本実施形態に係る連続加熱装置を備えた金属帯の連続処理ラインの一部を示す模式図である。なお、連続処理ラインとしては、連続焼鈍ラインや連続溶融亜鉛メッキラインを例示することが出来る。
また、金属帯として鋼帯を例示するが、他の金属帯であっても良い。
Next, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a schematic view showing a part of a continuous treatment line for a metal strip provided with a continuous heating apparatus according to this embodiment. In addition, as a continuous processing line, a continuous annealing line and a continuous hot dip galvanizing line can be illustrated.
Moreover, although a steel strip is illustrated as a metal strip, other metal strips may be used.

(構成)
連続して搬送されてくる鋼帯1が、直火式加熱炉2で連続して加熱された後に、後工程に連続して搬送される。
上記直火式加熱炉2内は、例えば鋼帯1の搬送方向に沿って例えば4つのゾーンに区画され、各ゾーン毎に配置したバーナー装置3〜6で、各ゾーンの雰囲気状態を制御しつつ鋼帯1を加熱する。
(Constitution)
The steel strip 1 that is continuously conveyed is continuously heated in the direct-fired heating furnace 2 and then continuously conveyed to the subsequent process.
The direct-fired heating furnace 2 is divided into, for example, four zones along the conveying direction of the steel strip 1, for example, and burner devices 3 to 6 arranged for each zone are used to control the atmosphere state of each zone. The steel strip 1 is heated.

本実施形態では、例えば第1ゾーン〜第3ゾーンまでは、ノズルミックス(ノズル内で混合する方式)のバーナー設備3〜5を使用し、設定された空気比として、目的の酸化還元雰囲気にして鋼帯1の加熱を行う。
また、最終ゾーンである第4ゾーンでは、プレミックスのバーナー設備6を採用する。その第4ゾーンのバーナー設備の構成は、図2に示すような構成となっている。
In this embodiment, for example, from the first zone to the third zone, the nozzle mix (mixing method in the nozzle) burner equipment 3 to 5 is used, and the target air-reduction atmosphere is set as the set air ratio. The steel strip 1 is heated.
In the fourth zone, which is the final zone, a premix burner facility 6 is employed. The configuration of the burner facility in the fourth zone is as shown in FIG.

即ち、ミキシング装置7に対して燃焼用空気系配管8の下流端と、燃料系配管9の下流端が連通している。これによって、ミキシング装置7に対し、酸素含有ガスとしての燃焼用空気と、燃料ガスとを供給可能となっている。
上記燃焼用空気系配管8の途中には、流量調節弁10が介装し、その流量調節弁10の上流側には、流量検出器としての流量発信器11を設ける。流量発信器11は、検出信号を計装用コントローラ15に出力する。また、流量調節弁10は、計装用コントローラ15からの指令に応じた流量となるように調整する。
That is, the downstream end of the combustion air system pipe 8 and the downstream end of the fuel system pipe 9 communicate with the mixing device 7. As a result, combustion air as an oxygen-containing gas and fuel gas can be supplied to the mixing device 7.
A flow rate control valve 10 is interposed in the middle of the combustion air system pipe 8, and a flow rate transmitter 11 as a flow rate detector is provided upstream of the flow rate control valve 10. The flow rate transmitter 11 outputs a detection signal to the instrumentation controller 15. Further, the flow rate adjusting valve 10 adjusts the flow rate according to a command from the instrumentation controller 15.

同様に、燃料系配管9の途中には、流量調節弁12が介装し、その流量調節弁12の上流側には、流量検出器としての流量発信器13を設ける。流量発信器13は、検出信号を計装用コントローラ15に出力する。また、流量調節弁12は、計装用コントローラ15からの指令に応じた流量となるように調整する。
ミキシング装置7は、供給された燃料用ガスと燃焼用空気とを混合する混合室を備え、混合室で混合されてなる予混合ガスを配管を介してノズルヘッダ16に供給し、ノズルヘッダ16に連通するノズル17から加熱炉2内に上記予混合ガスを噴射して加熱する。混合室は、配管よりも開口断面の大きな室である。
Similarly, a flow rate adjusting valve 12 is interposed in the middle of the fuel system pipe 9, and a flow rate transmitter 13 as a flow rate detector is provided upstream of the flow rate adjusting valve 12. The flow rate transmitter 13 outputs a detection signal to the instrumentation controller 15. Further, the flow rate adjusting valve 12 adjusts the flow rate according to a command from the instrumentation controller 15.
The mixing device 7 includes a mixing chamber for mixing the supplied fuel gas and combustion air, and supplies the premixed gas mixed in the mixing chamber to the nozzle header 16 via a pipe. The premixed gas is injected into the heating furnace 2 from the communicating nozzle 17 and heated. The mixing chamber is a chamber having a larger opening cross section than the pipe.

符号18は、ノズルへの予混合ガス供給経路に設けた圧力計である。この圧力計18はインターロックのために設けてある。設定圧力以下を検出したら、バーナーを停止する。
また、直火式加熱炉2の出側には、加熱炉2から出る鋼帯1の温度を測定する温度計18が配置されている。この温度計18は、例えば放射温度計で構成する。温度計18は、計測した温度信号を計装用コントローラ15に出力する。
Reference numeral 18 denotes a pressure gauge provided in the premixed gas supply path to the nozzle. The pressure gauge 18 is provided for interlock. When the pressure below the set pressure is detected, stop the burner.
A thermometer 18 for measuring the temperature of the steel strip 1 exiting from the heating furnace 2 is disposed on the exit side of the direct-fired heating furnace 2. The thermometer 18 is composed of a radiation thermometer, for example. The thermometer 18 outputs the measured temperature signal to the instrumentation controller 15.

計装用コントローラ15には、鋼種の変更の度に、加熱する鋼種に対応する空気比設定値が入力される。なお、鋼種(金属帯の性状)に応じて空気比を決定したテーブルを備え、そのテーブルを参照して、加熱する鋼帯1の空気比設定値を決定する。
その計装用コントローラ15は、制御部を構成し、設定計器部15A、燃料ガス流量調整部15B、及び燃焼用空気流量調整部15Cを備える。
An air ratio set value corresponding to the steel type to be heated is input to the instrumentation controller 15 every time the steel type is changed. In addition, the table which determined the air ratio according to steel types (the property of a metal strip) is provided, and the air ratio setting value of the steel strip 1 to be heated is determined with reference to the table.
The instrumentation controller 15 constitutes a control unit, and includes a setting instrument unit 15A, a fuel gas flow rate adjustment unit 15B, and a combustion air flow rate adjustment unit 15C.

設定計器部15Aは、入力した空気比設置値及び温度信号に基づき、燃焼ガスの流量及び燃焼用空気の流量を決定し、その流量指令を、それぞれ燃料ガス流量調整部15B、及び燃焼用空気流量調整部15Cに出力する。空気比は、あくまで、空気比設置値で決定される。温度信号では、加熱量が調整される。即ち、供給流量の増減が調整される。
燃料ガス流量調整部15Bは、流量発信器13からの信号に基づき流量実績値を演算し、その演算値に基づき、設定計器部15Aからの信号に応じた燃料ガスの流量をミキシング装置7に供給するように、流量調節弁12を調節する。
The setting instrument unit 15A determines the flow rate of the combustion gas and the flow rate of the combustion air based on the input air ratio setting value and the temperature signal, and supplies the flow rate commands to the fuel gas flow rate adjustment unit 15B and the combustion air flow rate, respectively. Output to the adjustment unit 15C. The air ratio is determined only by the air ratio installation value. In the temperature signal, the heating amount is adjusted. That is, the increase or decrease of the supply flow rate is adjusted.
The fuel gas flow rate adjusting unit 15B calculates the actual flow rate value based on the signal from the flow rate transmitter 13, and supplies the fuel gas flow rate according to the signal from the set instrument unit 15A to the mixing device 7 based on the calculated value. The flow rate control valve 12 is adjusted so as to achieve this.

燃焼用空気流量調整部15Cは、流量発信器11からの信号に基づき流量実績値を演算し、その演算値に基づき、設定計器部15Aからの信号に応じた燃焼用空気の流量をミキシング装置7に供給するように、流量調節弁10を調節する。
ここで、計装用コントローラ15は、第1ゾーンから第3ゾーンのバーナー設備3〜5の空気比も、鋼種に応じて予め設定した空気比となるように制御する。なお、第1ゾーンから第3ゾーンのバーナー設備3〜5も上記バーナー設備6と同様な構成としても良い。
The combustion air flow rate adjusting unit 15C calculates the actual flow rate value based on the signal from the flow rate transmitter 11, and based on the calculated value, the combustion air flow rate adjusting unit 15C mixes the flow rate of the combustion air according to the signal from the set instrument unit 15A. The flow control valve 10 is adjusted so that
Here, the instrumentation controller 15 controls the air ratios of the burner facilities 3 to 5 from the first zone to the third zone so that the air ratio is set in advance according to the steel type. In addition, the burner equipment 3-5 of the 1st zone to the 3rd zone is good also as a structure similar to the said burner equipment 6. FIG.

(作用効果)
上記構成の連続加熱装置にあっては、連続して搬送されてくる鋼帯1の鋼種が代わっても、空気比を、その鋼種に適した値に、比較的自由に且つ広範囲に変更することが可能となる。
今までであれば、直火式加熱炉2の最終ゾーンを還元雰囲気となるように空気比を制御しているが、本実施形態では、鋼種に応じて、直火式加熱炉2の最終ゾーンを還元雰囲気としたり、酸化雰囲気としたりすることが可能となる。
なお、還元雰囲気とする場合には、例えば空気比設定値を0.85等に調整する。一方、酸化雰囲気とする場合には、例えば空気比設定値を1.2等に調整する。
(Function and effect)
In the continuous heating device having the above-described configuration, even if the steel type of the steel strip 1 that is continuously conveyed changes, the air ratio can be changed relatively freely and over a wide range to a value suitable for the steel type. Is possible.
Until now, the air ratio is controlled so that the final zone of the direct-fired heating furnace 2 becomes a reducing atmosphere, but in the present embodiment, the final zone of the direct-fired heating furnace 2 according to the steel type. Can be made a reducing atmosphere or an oxidizing atmosphere.
In the case of a reducing atmosphere, for example, the air ratio set value is adjusted to 0.85 or the like. On the other hand, in the case of an oxidizing atmosphere, for example, the air ratio set value is adjusted to 1.2 or the like.

このように空気比を比較的広範囲に且つ自由に変更することは、上述した従来のプレミックスバーナーでは、困難であったが、本実施形態の連続加熱装置では、比較的自由に可能となる。
また、ミキシング装置7で、燃焼ガスと燃焼用空気とを予混合してからノズル17に供給している。ミキシング装置7で予混合することで、燃焼ガスと燃焼用空気との混合を均一に近い状態とすることが可能となる。このため、ノズル17から噴射する予混合ガスのバラツキを、その分低減し、安定して還元雰囲気若しくは酸化雰囲気とすることが可能となる。
In this way, changing the air ratio in a relatively wide range and freely has been difficult with the above-described conventional premix burner, but with the continuous heating apparatus of this embodiment, it is relatively freely possible.
Further, the mixing device 7 premixes the combustion gas and the combustion air before supplying them to the nozzle 17. By premixing with the mixing device 7, the mixing of the combustion gas and the combustion air can be made nearly uniform. For this reason, the variation of the premixed gas injected from the nozzle 17 can be reduced by that amount, and a reducing atmosphere or an oxidizing atmosphere can be established stably.

以上のように、操業に応じて、直火式加熱炉2の最終ゾーンを酸化雰囲気にしたり還元雰囲気にしたりすることが容易にできる。
例えば、Siなどの酸化されやすい成分を含有する鋼種の場合には、加熱によってSiの酸化物等が鋼帯1表面に形成されることで、後工程の処理品質に影響がでる場合がある。このような場合には、酸化、還元の条件を厳しくして制御する必要が生じ、本願発明を好適に適用できる。
すなわち、本実施形態の連続加熱装置は、プレミックスバーナーの空気比制御を比較的自由に且つ広範囲に変更することが可能であるので、鋼種に応じて、直火式加熱炉2の最終ゾーンを酸化雰囲気にしたり還元雰囲気にしたりすることが容易となり、操業効率を落とす事なく対応することが可能である。
As described above, the final zone of the direct heating furnace 2 can be easily changed to an oxidizing atmosphere or a reducing atmosphere according to the operation.
For example, in the case of a steel type containing an easily oxidizable component such as Si, the treatment quality of the subsequent process may be affected by the formation of Si oxide or the like on the surface of the steel strip 1 by heating. In such a case, it is necessary to control under strict oxidation and reduction conditions, and the present invention can be suitably applied.
That is, the continuous heating apparatus of the present embodiment can change the air ratio control of the premix burner relatively freely and over a wide range, so that the final zone of the direct heating furnace 2 is set according to the steel type. It is easy to make an oxidizing atmosphere or a reducing atmosphere, and it is possible to cope without reducing the operation efficiency.

本発明に基づく実施形態に係る加熱装置を示す模式図である。It is a schematic diagram which shows the heating apparatus which concerns on embodiment based on this invention. 本発明に基づく実施形態に係るバーナー設備を説明する図である。It is a figure explaining the burner installation which concerns on embodiment based on this invention.

符号の説明Explanation of symbols

1 鋼帯(金属帯)
2 直火式加熱炉
6 バーナー設備
7 ミキシング装置
8 空気系配管
8 燃焼用空気系配管
9 燃料系配管
10 流量調節弁
11 流量発信器
12 流量調節弁
13 流量発信器
15 計装用コントローラ
15A 設定計器
15C 燃焼用空気流量調整部
15B 燃料ガス流量調整部
17 ノズル
1 Steel strip (metal strip)
2 Direct-fired heating furnace 6 Burner equipment 7 Mixing device 8 Air system piping 8 Combustion air system piping 9 Fuel system piping 10 Flow rate control valve 11 Flow rate transmitter 12 Flow rate control valve 13 Flow rate transmitter 15 Instrumentation controller 15A Setting meter 15C Combustion air flow rate adjustment unit 15B Fuel gas flow rate adjustment unit 17 Nozzle

Claims (2)

連続して搬送される金属帯を加熱する直火式加熱炉を備えた連続加熱装置であって、
直火式加熱炉内の少なくとも下流側で使用するバーナー設備を、燃料ガスと酸素含有ガスとを予めミキシング装置で混合した予混合ガスをノズルから噴射させて燃焼する構成とすると共に、上記ミキシング装置に燃料ガスを供給する燃料系配管、及び上記ミキシング装置に酸素含有ガスを供給する空気系配管のそれぞれに、流量検出器及び流量調節弁を設け、
加熱する金属帯に対応して設定された空気比となるように、上記流量検出器からの信号に基づき流量調節弁を制御する制御装置を備えたことを特徴とする金属帯の連続加熱装置。
A continuous heating device equipped with a direct-fired heating furnace that heats a continuously conveyed metal strip,
Burner equipment used at least downstream in the direct-fired heating furnace is configured to inject and burn a premixed gas in which a fuel gas and an oxygen-containing gas are mixed in advance by a mixing device, and the mixing device. A flow rate detector and a flow rate control valve are provided in each of the fuel system piping for supplying the fuel gas to the air system piping for supplying the oxygen-containing gas to the mixing device,
A continuous heating device for a metal band, comprising a control device for controlling a flow rate adjusting valve based on a signal from the flow rate detector so as to obtain an air ratio set corresponding to the metal band to be heated.
連続して搬送される金属帯を直火式加熱炉で連続して加熱する金属帯の連続加熱方法であって、
直火式加熱炉内の少なくとも下流側での加熱を、燃料ガスと酸素含有ガスとを予めミキシング装置で混合した予混合ガスをノズルから噴出させて燃焼する構成とすると共に、上記ミキシング装置に供給する燃料ガス及び酸素含有ガスを個別の流量調節弁で調節し、加熱する金属帯に対応して設定された空気比となるように、上記流量調節弁を制御することを特徴とする金属帯の連続加熱方法。
It is a continuous heating method of a metal strip that continuously heats a metal strip that is continuously conveyed in a direct-fired heating furnace,
Heating at least downstream in the direct-fired heating furnace is configured such that a premixed gas in which fuel gas and oxygen-containing gas are mixed in advance by a mixing device is jetted from the nozzle and burned, and supplied to the mixing device. Adjusting the fuel gas and the oxygen-containing gas with an individual flow control valve, and controlling the flow control valve so as to obtain an air ratio set corresponding to the metal strip to be heated. Continuous heating method.
JP2008081241A 2008-03-26 2008-03-26 Apparatus and method for continuously heating metal strip Pending JP2009235463A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010202959A (en) * 2009-03-06 2010-09-16 Jfe Steel Corp Continuous hot dip galvanizing device and method for producing hot dip galvanized steel sheet

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02259009A (en) * 1989-03-31 1990-10-19 Nkk Corp Method for controlling air ratio in direct firing type heating furnace
JPH08176679A (en) * 1994-12-27 1996-07-09 Nkk Corp Continuous heating of steel strip and device therefor
JPH11279659A (en) * 1998-03-30 1999-10-12 Nkk Corp Directly firing reduction heating of steel strip and directly firing reduction heating device.

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02259009A (en) * 1989-03-31 1990-10-19 Nkk Corp Method for controlling air ratio in direct firing type heating furnace
JPH08176679A (en) * 1994-12-27 1996-07-09 Nkk Corp Continuous heating of steel strip and device therefor
JPH11279659A (en) * 1998-03-30 1999-10-12 Nkk Corp Directly firing reduction heating of steel strip and directly firing reduction heating device.

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010202959A (en) * 2009-03-06 2010-09-16 Jfe Steel Corp Continuous hot dip galvanizing device and method for producing hot dip galvanized steel sheet

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