JPH08199324A - Steel plate temperature control method in alloying furnace - Google Patents

Steel plate temperature control method in alloying furnace

Info

Publication number
JPH08199324A
JPH08199324A JP7006626A JP662695A JPH08199324A JP H08199324 A JPH08199324 A JP H08199324A JP 7006626 A JP7006626 A JP 7006626A JP 662695 A JP662695 A JP 662695A JP H08199324 A JPH08199324 A JP H08199324A
Authority
JP
Japan
Prior art keywords
temperature
plate temperature
heating zone
heating
side plate
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Withdrawn
Application number
JP7006626A
Other languages
Japanese (ja)
Inventor
Youichi Shimonosono
陽一 下之薗
Takashi Sasahara
隆志 笹原
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
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 Steel Corp filed Critical Nippon Steel Corp
Priority to JP7006626A priority Critical patent/JPH08199324A/en
Publication of JPH08199324A publication Critical patent/JPH08199324A/en
Withdrawn legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

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  • Coating With Molten Metal (AREA)
  • Heat Treatment Of Strip Materials And Filament Materials (AREA)

Abstract

(57)【要約】 【目的】 合金化炉において、加熱帯入側板温あるいは
加熱帯出側板温を放射温度計や伝熱計算によらないで求
めるとともに、保熱帯出側板温を加熱帯出側板温とみな
してフィードバック制御する場合に、運転条件が変わっ
た時にも有効となる加熱帯出側板温により鋼板温度が制
御できる方法を提供するものである。 【構成】 合金化炉において、加熱帯入側板温あるいは
加熱帯出側板温を誘導加熱ヒーターのインピーダンスか
ら求めて、各誘導加熱ヒーターの投入電力を求めて鋼板
温度を制御するものである。
(57) [Summary] [Purpose] In the alloying furnace, the heating zone inlet side plate temperature or the heating zone outlet side plate temperature is obtained without using a radiation thermometer or heat transfer calculation, and the heat retaining zone outlet side plate temperature is determined as the heating zone outlet side plate temperature. It is intended to provide a method capable of controlling the steel plate temperature by the heating zone outlet side plate temperature, which is effective even when the operating conditions are changed, in the case of performing the feedback control as it is. [Structure] In an alloying furnace, a heating zone entrance side plate temperature or a heating zone exit side plate temperature is obtained from the impedance of an induction heating heater, and the input power of each induction heating heater is obtained to control the steel sheet temperature.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本願発明は、連続式溶融亜鉛メッ
キ鋼板製造設備において、誘導式加熱炉とヒーター式保
熱炉を用いて合金メッキ鋼板を製造する場合の鋼板の温
度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 a method for controlling the temperature of a steel sheet when an alloy-plated steel sheet is produced using an induction heating furnace and a heater-type heat-retaining furnace in a continuous hot-dip galvanized steel sheet production facility. is there.

【0002】[0002]

【従来の技術】合金亜鉛メッキ鋼板は、耐食性、塗装
性、プレス成形性などに優れていることから、自動車用
鋼板や家電用鋼板などに用いられている。合金亜鉛メッ
キ鋼板は、鋼板を溶融亜鉛浴に通し、亜鉛浴の直上に設
置されたワイピング装置で適正なメッキ厚みに調整した
後、加熱帯で500〜550°C程度に加熱し、さらに
保熱帯で等温維持することによってメッキ層を鉄と亜鉛
の合金層にすることによって製造するのが一般的であ
る。
2. Description of the Related Art Galvanized steel sheets are used as steel sheets for automobiles, steel sheets for home appliances, etc. because they are excellent in corrosion resistance, paintability and press formability. For alloy galvanized steel sheets, pass the steel sheet through a hot dip zinc bath, adjust the plating thickness to an appropriate level with a wiping device installed directly above the zinc bath, then heat to about 500 to 550 ° C in a heating zone, and further preserve the heat. It is generally manufactured by making the plating layer an alloy layer of iron and zinc by keeping the temperature isothermal.

【0003】このプロセスで重要な点は、合金層の合金
不足や過合金を防ぐために亜鉛メッキ鋼板の温度を制御
してメッキ層の合金化度を適正な範囲に制御することで
ある。
An important point in this process is to control the temperature of the galvanized steel sheet in order to prevent alloy shortage and overalloying of the alloy layer to control the alloying degree of the plated layer within an appropriate range.

【0004】従来、合金化炉はガス燃焼加熱方式が用い
られており、ガス燃焼加熱方式の場合、鋼板温度は炉温
を調節することによって制御され、その方法は既に確立
している。
Conventionally, the alloy combustion furnace uses a gas combustion heating method. In the case of the gas combustion heating method, the temperature of the steel sheet is controlled by adjusting the furnace temperature, and the method has already been established.

【0005】近年、急速加熱による品質向上と環境保護
の観点から誘導加熱方式への移行が試みられつつある。
In recent years, there has been an attempt to shift to an induction heating method from the viewpoint of quality improvement by rapid heating and environmental protection.

【0006】例えば、特開平3ー199365号公報に
は、誘導加熱方式と直火.加熱方式との併用によって、
鋼板を加熱する際の合金化炉の板温制御技術が開示され
ている。前記公報に開示されている技術について、図5
を用いて説明すると、焼鈍炉21から出た鋼板20は、
亜鉛浴ポット22に入り亜鉛が付着され、ポット22か
ら引上げられ、ワイピングノズル23により亜鉛の付着
量が調整され、合金化炉の加熱帯24、保持帯25、冷
却帯26を通って鋼板表面に合金層を形成させるもので
ある。合金化炉のうち、加熱帯24は、誘導加熱方式の
第1加熱帯27、次いで直火加熱方式の第2加熱帯28
からなるものである。そして、誘導加熱方式の第1加熱
帯27で設定値になるように電力あるいは電圧を調整
し、直火加熱方式の第2加熱帯28で炉温設定値になる
ように炉温を調節するものである。
For example, Japanese Patent Laid-Open No. 3-199365 discloses an induction heating method and an open flame. By combining with the heating method,
A plate temperature control technique of an alloying furnace when heating a steel plate is disclosed. Regarding the technology disclosed in the above publication, FIG.
The steel plate 20 discharged from the annealing furnace 21 is
Zinc enters the zinc bath pot 22, is attached with zinc, is pulled up from the pot 22, the amount of zinc attached is adjusted by the wiping nozzle 23, and passes through the heating zone 24, holding zone 25, and cooling zone 26 of the alloying furnace to reach the steel plate surface. An alloy layer is formed. In the alloying furnace, the heating zone 24 includes a first heating zone 27 of an induction heating system and then a second heating zone 28 of an open flame heating system.
It consists of Then, the electric power or voltage is adjusted so that the first heating zone 27 of the induction heating system reaches the set value, and the furnace temperature is adjusted so that the second heating zone 28 of the direct heating system reaches the furnace temperature set value. Is.

【0007】[0007]

【発明が解決しようとする課題】前記の誘導加熱方式の
場合、鋼板温度は関数P=F(t、w、s、ΔT)/E
FFによって求められる電力を投入することによって制
御される(t=板厚、w=板幅、s=ラインスピード、
ΔT=昇温量、EFF=加熱効率)。しかしながら、こ
れには次の問題がある。
In the case of the above induction heating method, the steel plate temperature is a function P = F (t, w, s, ΔT) / E.
It is controlled by turning on the electric power calculated by the FF (t = plate thickness, w = plate width, s = line speed,
ΔT = amount of temperature rise, EFF = heating efficiency). However, this has the following problems.

【0008】(1) この関数中の昇温量は、加熱帯出
側における目標板温と加熱帯入側板温との差であるの
で、昇温量の算出には加熱帯入側板温を正確に得る必要
がある。ところが、放射温度計による方法は、亜鉛の飛
散による放射温度計レンズ面の曇りや鋼板の低放射率に
起因する放射エネルギーの減衰によって測定が困難であ
る。
(1) Since the temperature rise amount in this function is the difference between the target plate temperature on the heating zone exit side and the heating zone entrance side plate temperature, the heating zone entrance side plate temperature must be accurately calculated to calculate the temperature rise amount. Need to get However, the method using a radiation thermometer is difficult to measure due to the clouding of the lens surface of the radiation thermometer due to the scattering of zinc and the attenuation of the radiation energy due to the low emissivity of the steel sheet.

【0009】また、亜鉛浴から加熱帯までの空走区間で
の自然冷却とワイピングエアーによる冷却を考慮して計
算で求める方法は、熱伝達関数の設定が難しく、この方
法にも難がある。
Further, the method of calculating by taking into consideration the natural cooling in the idle running section from the zinc bath to the heating zone and the cooling by wiping air is difficult to set the heat transfer function, and this method is also difficult.

【0010】(2) さらに、前記関数で求められた電
力は、加熱効率や常数が運転条件によって多少異なるた
め、加熱帯出側板温を検出し目標板温と比較して、偏差
があれば投入電力を補正する必要がある。しかしなが
ら、加熱帯出側の鋼板は合金化過程であり、鋼板の放射
率が大幅に変化するため、放射温度計による測定は困難
である。
(2) Further, since the heating efficiency and constants of the electric power obtained by the above function are slightly different depending on the operating conditions, the heating zone outlet side plate temperature is detected and compared with the target plate temperature. Need to be corrected. However, the steel sheet on the heating zone exit side is in the process of alloying, and the emissivity of the steel sheet changes significantly, so it is difficult to measure with a radiation thermometer.

【0011】したがって、放射率変動の少ない保熱帯出
側で板温を測定し、その板温を加熱帯出側板温とみなす
方法が考えられる(通常、運転条件として加熱帯出側板
温と保熱帯出側板温は同じにするため、保熱帯目標炉温
は加熱帯出側目標板温と同一値に設定する)が、しかし
ながら、板幅やラインスピード等の運転条件が変わった
ときは保熱帯の熱容量が大きいため、炉温の応答時間の
遅れによって保熱帯出側板温が変動し、保熱帯出側板温
≠加熱帯出側板温となり、保熱帯出側板温を加熱帯出側
板温と見なして投入電力の補正をすることができないと
いう問題がある。
Therefore, a method is conceivable in which the plate temperature is measured on the heat retaining side outlet side where the emissivity fluctuation is small, and the plate temperature is regarded as the heating zone outlet side plate temperature (normally, the heating zone outlet side plate temperature and the heat retaining side outlet plate are operating conditions. Since the temperature is the same, the target temperature of the heat retaining zone is set to the same value as the target plate temperature on the heating zone exit side. However, when the operating conditions such as width and line speed change, the heat capacity of the heat retaining zone is large. Therefore, the warming tropical outlet side plate temperature fluctuates due to the delay in the response time of the furnace temperature, and the warming tropical outlet side plate temperature ≠ the heating zone outgoing side plate temperature. There is a problem that you can not.

【0012】そこで、本願発明は、上記問題点を解決す
るために、合金化炉において、加熱帯入側板温あるいは
加熱帯出側板温を放射温度計や伝熱計算によらないで求
めるとともに、保熱帯出側板温を加熱帯出側板温とみな
してフィードバック制御する場合に、運転条件が変わっ
た時にも有効となる加熱帯出側板温により鋼板温度が制
御できる方法を提供するものである。
Therefore, in order to solve the above-mentioned problems, the present invention finds a heating zone inlet side plate temperature or a heating zone outlet side plate temperature in an alloying furnace without using a radiation thermometer or heat transfer calculation. Provided is a method of controlling a steel plate temperature by the heating zone outlet side plate temperature which is effective even when the operating conditions are changed, when the outlet side plate temperature is regarded as the heating zone outlet side plate temperature for feedback control.

【0013】[0013]

【課題を解決するための手段】本願発明は、合金化炉に
おいて、加熱帯入側板温あるいは加熱帯出側板温を誘導
加熱ヒーターのインピーダンスから求めて、各誘導加熱
ヒーターの投入電力を求めて鋼板温度を制御するもので
ある。
According to the present invention, in an alloying furnace, the heating zone inlet side plate temperature or the heating zone outlet side plate temperature is obtained from the impedance of the induction heating heater, and the input power of each induction heating heater is obtained to obtain the steel sheet temperature. Is to control.

【0014】[0014]

【作用】誘導加熱ヒーターのインピーダンスから求めら
れた加熱帯入側板温あるいは加熱帯出側板温を利用して
投入電力を求めることにより、誘導加熱ヒーターに投入
される電力の正確さを向上させる事ができる。
[Function] The accuracy of the electric power supplied to the induction heating heater can be improved by calculating the input electric power by using the heating zone entrance side plate temperature or the heating zone exit side plate temperature obtained from the impedance of the induction heating heater. .

【0015】また、運転条件の変動によって保熱帯出側
板温が変動しても、計算によって求めた加熱帯出側板温
を加熱帯出側実績板温として用いることによって正確な
フィードバック制御が維持できる。
Even if the warming tropical outlet side plate temperature fluctuates due to changes in operating conditions, accurate feedback control can be maintained by using the heating zone outlet side plate temperature calculated as the heating zone outlet side actual plate temperature.

【0016】[0016]

【実施例】本願発明の実施例を図1を用いて説明する。Embodiment An embodiment of the present invention will be described with reference to FIG.

【0017】亜鉛ポット1へ連続的に送り込まれた鋼板
2には溶融亜鉛3が被覆され、亜鉛浴の直上に設置され
たワイピング装置4で適正なメッキ厚みに調整された
後、加熱帯5で500〜550°C程度に加熱され、さ
らに保熱帯6で等温維持されることによってメッキ層が
鉄と亜鉛の合金層になる。
The steel sheet 2 continuously fed to the zinc pot 1 is coated with molten zinc 3 and adjusted to an appropriate plating thickness by a wiping device 4 installed immediately above the zinc bath, and then heated by a heating zone 5. The plating layer becomes an alloy layer of iron and zinc by being heated to about 500 to 550 ° C. and being kept isothermally in the heat retaining zone 6.

【0018】本願発明においては、鋼板2は、加熱帯5
において誘導加熱され、保熱帯6においてはヒーターで
保熱されるものである。そして、亜鉛ポット1保熱帯6
及び保熱帯出側にはそれぞれ温度検出器8、9、11が
設けられ、誘導加熱ヒーターは投入電力制御装置7で制
御される。また、保熱帯のヒーター12は炉温調節計1
0で制御される。
In the present invention, the steel plate 2 is the heating zone 5
Induction heating is carried out at 1, and heat is held by a heater at the heat retaining zone 6. And a zinc pot 1 a warming 6
Further, temperature detectors 8, 9 and 11 are respectively provided on the outlet side of the warming zone and the induction heating heater is controlled by the input power control device 7. In addition, the heater 12 of the warming zone is the furnace temperature controller 1
It is controlled by 0.

【0019】誘導加熱方式の加熱帯5には、必要数の誘
導加熱ヒーター(IH)がNo.1〜No.nまで設け
てあり、各ヒータは投入電力制御装置により、供給電力
が制御され、板温が制御される。
In the induction heating type heating zone 5, a required number of induction heating heaters (IH) No. 1 to No. n heaters are provided, and the supply power of each heater is controlled by the input power control device to control the plate temperature.

【0020】本願発明においては、加熱帯入側板温及び
加熱帯出側板温を誘導加熱ヒーター(IH)のインピー
ダンスによって求めるが、これに関し、図2を参照し
て、板温と誘導加熱ヒーターのインピーダンスの関係に
ついて説明する。
In the present invention, the heating zone entrance side plate temperature and the heating zone exit side plate temperature are determined by the impedance of the induction heating heater (IH). In this regard, referring to FIG. 2, the plate temperature and the impedance of the induction heating heater The relationship will be described.

【0021】図2から明らかなとおり、n段目の誘導加
熱ヒーター部の平均板温Tn(°C)は、誘導加熱ヒー
ターのインピーダンスZ(Ω)(=供給電圧/電流)と
相関関係にある。このことに着目し、誘導加熱ヒーター
のインピーダンスから加熱帯入側板温(TIACT)及び加
熱帯出側板温(TOACT)を、式1及び式2から求めるこ
とができる。
As is apparent from FIG. 2, the average plate temperature Tn (° C) of the n-th induction heating heater section is correlated with the impedance Z (Ω) (= supply voltage / current) of the induction heating heater. . Focusing on this fact, the heating zone entry side temperature from the impedance of the induction heater to (T IACT) and heated home use plate temperature (T OACT), can be obtained from Equation 1 and Equation 2.

【0022】式1 TIACT=Tn−Pn(Tn+1−Tn)/(Pn+Pn
+1) 式2 TOACT=Tn+Pn(Tn−Tn−1)/(Pn+Pn
−1) ここで、 TIACT:加熱帯入側板温 TOACT:加熱帯出側板温 Tn :n段目の誘導加熱ヒーター部の平均板温 Pn :n段目の誘導加熱ヒーターへの投入電力 上記の式から、加熱帯入側板温は、第1段目と第2段目
の誘導加熱ヒーターのインピーダンスを求め、予め採取
しておいたインピーダンスー板温特性より、各段の誘導
加熱ヒーター部の板温を求め、誘導加熱ヒーター間の板
温差から1段目ヒーターの昇温量を算出し、それを第1
段目の板温から減することによって加熱帯入側板温を求
めることができる。
Formula 1 T IACT = Tn-Pn (Tn + 1-Tn) / (Pn + Pn
+1) Formula 2 T OACT = Tn + Pn (Tn-Tn-1) / (Pn + Pn
Here -1), T IACT: heating zone entry side temperature T OACT: heating home use plate temperature Tn: n-th stage of the induction heater of the average metal temperature Pn: input power above into the n-th stage of the induction heater From the equation, the heating zone entrance side plate temperature is obtained by calculating the impedance of the induction heating heaters of the first and second stages, and the plate of the induction heating heater part of each stage is obtained from the impedance-plate temperature characteristics collected in advance. Calculate the temperature, calculate the temperature rise of the first stage heater from the plate temperature difference between the induction heating heaters,
The heating zone entrance side plate temperature can be obtained by subtracting the plate temperature from the step.

【0023】同様に加熱帯出側板温も式2により求める
ことができる。
Similarly, the heating zone outlet side plate temperature can be obtained by the equation (2).

【0024】こうしてインピーダンスー板温特性から、
誘導加熱ヒーターのインピーダンスを測定することによ
り加熱帯入側板温又は加熱帯出側板温を正確に求めるこ
とができ、その結果、誘導加熱ヒーターの投入電力を正
確に得ることができる。
Thus, from the impedance-plate temperature characteristics,
By measuring the impedance of the induction heater, the heating zone entrance side plate temperature or the heating zone exit side plate temperature can be accurately obtained, and as a result, the input power of the induction heating heater can be obtained accurately.

【0025】そして、前記投入電力は、次式により求め
ることができる(図3参照)。
Then, the input power can be obtained by the following equation (see FIG. 3).

【0026】まず、処理材条件によるベース電力(TP
B)の計算が行われる。
First, the base power (TP
The calculation of B) is performed.

【0027】式3 TPB=J×t×W×ρ×Q×103/EFF ここで、 t:板厚(mm) W:板幅(mm) ρ:鋼板の比重(kg/mm3) Q:鋼板の比熱(kw・sec/kg・°C) EFF:加熱効率(板厚・板幅の関数) J:常数 ベース電力が計算されると、次いで、次式により運転条
件による投入電力計算が行われる。
Formula 3 TPB = J × t × W × ρ × Q × 10 3 / EFF where, t: plate thickness (mm) W: plate width (mm) ρ: specific gravity of steel plate (kg / mm 3 ) Q : Specific heat of steel plate (kw · sec / kg · ° C) EFF: Heating efficiency (function of plate thickness / plate width) J: Constant When the base power is calculated, then the input power is calculated according to the operating conditions by the following formula. Done.

【0028】式4 Ptw=TPB×S(TOTAR−TIACT)/60+K[k
W] ここで、 S:ラインスピード(m/min) TOTAR:目標板温(°C) TIACT:加熱帯入側板温(°C) K:補正電力(kW) 前記計算により得られた電力を投入し、補正電力Kの計
算を次式により行なう。
Equation 4 Ptw = TPB × S (T OTAR −T IACT ) / 60 + K [k
W] Here, S: Line speed (m / min) T OTAR : Target plate temperature (° C) T IACT : Heating zone entrance side plate temperature (° C) K: Corrected power (kW) Power obtained by the above calculation Then, the correction power K is calculated by the following equation.

【0029】式5 K=TPB×S×(TOTAR−TOACT)/60 ここで、 TOACT:加熱帯出側板温(°C) 式4及び式5を繰り返すことにより加熱帯目標板温と実
績板温の偏差より投入電力の補正量を算出し、修正す
る。
Formula 5 K = TPB × S × (T OTAR −T OACT ) / 60 where T OACT : Heating zone outlet side plate temperature (° C) By repeating the equations 4 and 5, the heating zone target plate temperature and actual result are obtained. The correction amount of input power is calculated from the deviation of the plate temperature and corrected.

【0030】次に、前記の板温を利用して、運転条件が
変動した場合の制御について、図4を用いて説明する。
Next, the control when the operating conditions are changed by using the above plate temperature will be described with reference to FIG.

【0031】加熱帯出側板温TOACTとして保熱帯出側板
温(の区間)を使ってフィードバック制御するもの
で、前述の方法で誘導加熱ヒータのインピーダンスから
加熱帯出側板温を求めておき、運転条件が変動し保熱帯
炉温が変動し目標炉温±aから外れたときには、加熱帯
出側実績板温を保熱帯出側板温から、前記の方法で求め
た板温に切り替え(の区間)、保熱帯炉温が目標炉温
±aに戻ったとき加熱帯出側実績板温を保熱帯出側板温
に(の区間)切り替える。この時、加熱帯目標板温と
実績板温の偏差より投入電力の補正量を算出し、修正す
る。
The heating zone outlet side plate temperature T OACT is subjected to feedback control using the warming zone outlet side plate temperature (section), and the heating zone outlet side plate temperature is obtained from the impedance of the induction heater by the above-mentioned method. When the temperature of the heat retaining zone fluctuates and deviates from the target furnace temperature ± a, the actual strip temperature on the heating zone outlet side is switched from the heat retaining zone outlet side temperature to the sheet temperature obtained by the above method (section), heat retaining zone When the furnace temperature returns to the target furnace temperature ± a, the heating zone outlet-side actual plate temperature is switched to the heat retention outlet-side plate temperature (section). At this time, the correction amount of the input power is calculated and corrected from the deviation between the heating zone target plate temperature and the actual plate temperature.

【0032】[0032]

【発明の効果】板温を正確に制御することが可能とな
る。
The plate temperature can be accurately controlled.

【0033】本願発明は、誘導加熱ヒータのインピーダ
ンスから誘導加熱ヒーターの板温を求めた加熱帯入側あ
るいは加熱帯出側の板温を利用して鋼板温度を制御する
ので、正確なフィードバック制御ができ、また、運転条
件の変動によって保熱帯出側板温が変化しても、前記イ
ンピーダンスから求めた加熱帯出側板温を加熱帯出側実
績板温として適用することによって正確なフィードバッ
ク制御が維持できる。
In the present invention, the steel plate temperature is controlled by utilizing the plate temperature on the heating zone entrance side or the heating zone exit side, which is obtained from the impedance of the induction heating heater, so that accurate feedback control can be performed. Further, even if the warming tropical outlet side plate temperature changes due to changes in operating conditions, accurate feedback control can be maintained by applying the heating zone outlet side plate temperature obtained from the impedance as the heating zone outlet side actual plate temperature.

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

【図1】本願発明に適用される合金化炉の概略図。FIG. 1 is a schematic view of an alloying furnace applied to the present invention.

【図2】インピーダンスと板温の関係図。FIG. 2 is a diagram showing the relationship between impedance and plate temperature.

【図3】投入電力の計算手順を示す図。FIG. 3 is a diagram showing a calculation procedure of input power.

【図4】本願発明を運転条件変動時に適用した場合の目
標板温の変化図。
FIG. 4 is a graph showing changes in target plate temperature when the present invention is applied when operating conditions change.

【図5】従来の合金化炉の概略図。FIG. 5 is a schematic view of a conventional alloying furnace.

【符号の説明】[Explanation of symbols]

1、22 亜鉛ポット 2、20 鋼板 3、22
亜鉛浴 4、23 ワイピング装置 5、24 加熱帯
6、25 保熱帯 7 投入電力制御装置 8、9、11 温度検出器
10 保熱帯炉温調節計 12 保熱帯ヒーター
21 焼鈍炉 26 冷却帯 27 誘導加熱方式の第1加熱帯 28 直火加熱方
式の第2加熱帯
1,22 Zinc pot 2,20 Steel plate 3,22
Zinc bath 4,23 Wiping device 5,24 Heating zone
6,25 Heat insulation 7 Input power control device 8, 9, 11 Temperature detector
10 Heat-retaining furnace temperature controller 12 Heat-retaining heater
21 annealing furnace 26 cooling zone 27 first heating zone of induction heating system 28 second heating zone of direct flame heating method

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 合金化炉の誘導加熱ヒーターからなる加
熱帯に投入する電力により鋼板温度を制御する方法にお
いて、 各段の誘導加熱ヒーターのインピーダンスを求め、 相関関係にあるインピーダンスー板温特性より、各段の
誘導加熱ヒーターの板温を求め、 相隣る誘導加熱ヒーター間の板温差から各段の昇温量を
算出し、 前記昇温量と相隣る誘導加熱ヒーターの板温との減算又
は加算から加熱帯入側あるいは加熱帯出側の板温を求
め、 前記加熱帯入側あるいは加熱帯出側の板温を用いて投入
電力を求めることを特徴とする鋼板温度を制御する方
法。
1. A method of controlling a steel sheet temperature by electric power supplied to a heating zone composed of an induction heating heater of an alloying furnace, wherein the impedance of the induction heating heater at each stage is obtained, and the impedance plate temperature characteristic is correlated. , The plate temperature of the induction heating heater of each stage is calculated, and the heating amount of each stage is calculated from the plate temperature difference between the adjacent induction heating heaters. A method for controlling a steel sheet temperature, which comprises obtaining the plate temperature on the heating zone entrance side or the heating zone exit side from subtraction or addition, and obtaining the input power using the plate temperature on the heating zone entrance side or the heating zone exit side.
【請求項2】 合金化炉の誘導加熱ヒーターからなる加
熱帯に投入する電力により鋼板温度を制御する方法にお
いて、加熱帯出側板温として保熱帯出側板温を用い、こ
れをフィードバックして鋼板温度を制御するにあたり、
保熱帯炉温が目標炉温範囲から外れたとき加熱帯出側実
績板温を保熱帯出側板温から請求項1で求められた加熱
帯出側板温に切り替え、保熱帯炉温が目標炉温範囲に戻
ったとき加熱帯出側実績板温を保熱帯出側板温に切り替
えることを特徴とする鋼板温度を制御する方法。
2. A method of controlling a steel sheet temperature by electric power applied to a heating zone composed of an induction heating heater of an alloying furnace, wherein a warming temperature outgoing side sheet temperature is used as a heating zone outgoing side sheet temperature, and this is fed back to determine the steel sheet temperature. In controlling
When the warming zone temperature is out of the target furnace temperature range, the heating zone outlet side actual plate temperature is switched from the warming zone outlet side plate temperature to the heating zone outlet side plate temperature obtained in claim 1, and the warming zone furnace temperature falls within the target furnace temperature range. A method for controlling a steel plate temperature, characterized in that the actual strip temperature on the outlet side of the heating zone is switched to the strip temperature on the heat retaining side when returning.
JP7006626A 1995-01-19 1995-01-19 Steel plate temperature control method in alloying furnace Withdrawn JPH08199324A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7006626A JPH08199324A (en) 1995-01-19 1995-01-19 Steel plate temperature control method in alloying furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7006626A JPH08199324A (en) 1995-01-19 1995-01-19 Steel plate temperature control method in alloying furnace

Publications (1)

Publication Number Publication Date
JPH08199324A true JPH08199324A (en) 1996-08-06

Family

ID=11643580

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7006626A Withdrawn JPH08199324A (en) 1995-01-19 1995-01-19 Steel plate temperature control method in alloying furnace

Country Status (1)

Country Link
JP (1) JPH08199324A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6114675A (en) * 1997-12-05 2000-09-05 Mitsubishi Heavy Industries, Ltd. Alloying system and heating control device for high grade galvanized steel sheet
JP2008119417A (en) * 2006-11-16 2008-05-29 Matsushita Electric Ind Co Ltd Induction heating rice cooker

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6114675A (en) * 1997-12-05 2000-09-05 Mitsubishi Heavy Industries, Ltd. Alloying system and heating control device for high grade galvanized steel sheet
JP2008119417A (en) * 2006-11-16 2008-05-29 Matsushita Electric Ind Co Ltd Induction heating rice cooker

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