JPH0532447B2 - - Google Patents

Info

Publication number
JPH0532447B2
JPH0532447B2 JP4037885A JP4037885A JPH0532447B2 JP H0532447 B2 JPH0532447 B2 JP H0532447B2 JP 4037885 A JP4037885 A JP 4037885A JP 4037885 A JP4037885 A JP 4037885A JP H0532447 B2 JPH0532447 B2 JP H0532447B2
Authority
JP
Japan
Prior art keywords
furnace
furnace temperature
temperature
billet
temperature setting
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
JP4037885A
Other languages
Japanese (ja)
Other versions
JPS61199017A (en
Inventor
Satoshi Kohama
Nobunori Wakamya
Makoto Tsuruta
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric 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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP4037885A priority Critical patent/JPS61199017A/en
Publication of JPS61199017A publication Critical patent/JPS61199017A/en
Publication of JPH0532447B2 publication Critical patent/JPH0532447B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は連続式加熱炉の制御方法に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] This invention relates to a method of controlling a continuous heating furnace.

〔従来の技術〕[Conventional technology]

従来、加熱炉内の鋼片の焼き上げ温度の計算機
制御は、例えば特開昭56−75527号公報に示され
ているように鋼片の装入から抽出までの炉内の各
位置における鋼片温度を、炉内温度分布を基に鋼
片のサイズ、物性値、及び実積在炉時間により伝
熱計算によつて決定し、ある昇温パターンに従う
ように炉内温度を設定する方法が採られている。
Conventionally, computer control of the baking temperature of a steel billet in a heating furnace has been carried out by controlling the temperature of the steel billet at each position in the furnace from charging to extraction, as shown in, for example, Japanese Patent Application Laid-open No. 75527/1983. is determined by heat transfer calculation based on the temperature distribution in the furnace, the size of the steel billet, physical property values, and actual furnace time, and a method is adopted in which the temperature in the furnace is set to follow a certain temperature increase pattern. ing.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

上記のような従来の連続式加熱炉の制御方法で
は、加熱炉に装入される鋼片は、サイズ、物性
値、加熱鋼種(鋼片の抽出温度上・下限、均熱度
制限)の組み合わせでグループにまとめられてい
るが、炉内の鋼片グループは多品種少生産により
数10種にまたがることがあり、例え省エネルギー
等の観点から各々の鋼片の好ましい昇温パターン
が求まつたとしても、その通りに各鋼片を焼き上
げるのは困難であつた。
In the conventional continuous heating furnace control method described above, the steel billet charged into the heating furnace is controlled by a combination of size, physical properties, and type of steel to be heated (upper/lower limits of extraction temperature of the steel billet, limits on soaking degree). However, due to high-mix, low-volume production, there may be several dozen types of billet groups in the furnace, and even if a preferable temperature increase pattern for each billet could be determined from the perspective of energy saving, etc. However, it was difficult to bake each piece of steel exactly as specified.

この発明はかかる問題点を解決するためになさ
れたもので、炉内の様々な鋼片を、各々の昇温パ
ターンに沿つて平均的あるいはある鋼片を優先的
に焼き上げることが可能な炉温設定値を決定する
ことができる連続式加熱炉の制御方法を得ること
を目的とする。
This invention was made to solve this problem, and the purpose of this invention is to set the furnace temperature at which various steel pieces in the furnace can be fired on average or preferentially according to each temperature increase pattern. The purpose of this invention is to obtain a control method for a continuous heating furnace that can determine set values.

〔問題点を解決するための手段〕[Means for solving problems]

この発明に係る連続式加熱炉の制御方法は、炉
内の様々な鋼片を各々の昇温パターンに沿つて平
均的あるいはある鋼片を優先的に焼き上げるため
に、各鋼片の炉温設定値に炉温設定用重み係数を
乗じ加重平均した値を設定炉温とするようにした
ものである。
The method for controlling a continuous heating furnace according to the present invention is to set the furnace temperature of each steel billet in order to bake various steel billets in the furnace averagely or preferentially to a certain steel billet in accordance with each temperature increase pattern. The value is multiplied by a weighting coefficient for furnace temperature setting, and the weighted average value is set as the set furnace temperature.

〔作用〕[Effect]

この発明においては、各鋼片の炉温設定値に炉
温設定用重み係数を乗じ加重平均した値を設定炉
温とするようにしているので、炉内の様々な鋼片
グループを、目標とする昇温パターンで平均的に
あるいはある鋼片について優先的に焼き上げるこ
とが可能となる。
In this invention, the furnace temperature set value of each slab is multiplied by the furnace temperature setting weighting coefficient and the weighted average value is set as the set furnace temperature. It becomes possible to bake evenly or preferentially a certain piece of steel using a temperature increase pattern.

〔実施例〕〔Example〕

以下この発明の制御方法について説明する。加
熱炉を第1図に示す様に炉長方向にj個に分割
し、実績燃料流量を基にして、発熱、ふく射、対
流、熱移動を考慮した熱バランス式をたて、非定
常の非線形連立方程式をニユートン法にて収束計
算させ、炉温分布が求まる。
The control method of the present invention will be explained below. As shown in Figure 1, the heating furnace is divided into j parts in the furnace length direction, and based on the actual fuel flow rate, a heat balance formula that takes into account heat generation, radiation, convection, and heat transfer is created, and an unsteady nonlinear The simultaneous equations are convergently calculated using Newton's method, and the furnace temperature distribution is determined.

この温度を基に炉内に存在する全鋼材について
公知の伝熱差分方程式を解いて鋼片温度を求め
る。省エネルギーなどの観点から求められた昇温
パターンを基に目標温度が決定されると、それぞ
れの鋼片に対するある位置においての炉温設定値
が、前述の現状の鋼片温度、目標温度などから決
定され得るであろう。こうして、鋼片1本毎の必
要とされるある位置における炉温設定値は求まつ
たが一般に加熱炉においては燃料流量制御装置は
各制御帯にしかついていず、鋼片各々の必要とさ
れる設定温度は各制御帯を分割したゾーンについ
ての設定値にすぎない。そこで以下の様にして、
この設定値を制御用温度計の存在するゾーンの設
定値に換算する必要がある。
Based on this temperature, a known heat transfer difference equation is solved for all the steel materials present in the furnace to determine the temperature of the steel billet. Once the target temperature is determined based on the temperature increase pattern determined from the viewpoint of energy saving, etc., the furnace temperature setting value at a certain position for each billet is determined from the above-mentioned current billet temperature, target temperature, etc. could be done. In this way, the required furnace temperature setting value for each billet at a certain position was determined, but in general, in a heating furnace, the fuel flow control device is only attached to each control zone, and the required furnace temperature setting value for each billet is determined. The set temperature is just a set value for each zone into which each control band is divided. So, do the following,
It is necessary to convert this set value to the set value of the zone where the control thermometer is located.

TgA′=TgA+(Tg(j)−Tg(k)) …(1) 但し、 TgA′:換算された設定炉温 Tg(j):炉温設定用ゾーンの炉内温度 Tg(k):炉温設定用ゾーンを含む制御帯の制御
用温度計の存在するゾーンの炉内温度 上記式(1)において、()内は炉温分布が前述で
判明しているので、設定値に対する補正項に対応
し、こうする事によつてある鋼片に対する必要炉
温が確実に得られるわけである。前述の方法によ
つて鋼片各々の炉温設定値は決定されたが、この
設定値を基に、各制御帯に対する設定値を以下の
式によつて求める。
T gA ′=T gA + (T g (j)−T g (k)) …(1) However, T gA ′: Converted set furnace temperature T g (j): Inside of the furnace in the furnace temperature setting zone Temperature T g (k): Furnace temperature in the zone where the control thermometer is located in the control zone including the furnace temperature setting zone In the above equation (1), the values in parentheses indicate the furnace temperature distribution determined above. Therefore, it corresponds to the correction term for the set value, and by doing so, the necessary furnace temperature for a certain slab can be reliably obtained. The furnace temperature setting value for each steel billet was determined by the method described above, and based on this setting value, the setting value for each control band was determined by the following formula.

Tgk=Σc(i)TgA′(i)/Σc(i) …(2) ここで、c(i)は各々の鋼片に対する焼上げ用重
み係数であり、c(i)をすべて同じにすると各々の
鋼片は目標温度に平均的に焼き上がるであろう
し、操業上、ある鋼片を優先的に焼き上げようと
するならばその鋼片に関するc(i)の重みを高める
事で実現可能となる。第2図はこの状態を示す。
T gk = Σc(i)T gA ′(i)/Σc(i) …(2) Here, c(i) is the weighting coefficient for baking for each steel slab, and if c(i) is the same for all If you do so, each billet will be baked to the target temperature on average, and if you want to bake a certain billet preferentially during operation, you can achieve this by increasing the weight of c(i) for that billet. It becomes possible. FIG. 2 shows this state.

次に、この発明の一実施例に基づく加熱炉制御
について第3図を参照して説明する。
Next, heating furnace control based on an embodiment of the present invention will be explained with reference to FIG.

第3図において、101は加熱炉、102は操
業情報管理部、103は燃料流量制御部、104
は熱電対などの炉温測定部、105はバーナ、1
06は炉温設定機能部である。炉温設定機能部1
06は大きく4つの機能に分離され、現状温度計
算1、将来温度計算2、昇温パターン計算3、炉
温設定計算4である。1,2のロジツクはほぼ同
じロジツクを持つていて、炉温及び鋼片温度、鋼
片移動計算機能を有している。まず操業情報管理
部102と燃料流量制御部103とからの鋼片情
報及び実績燃料流量を入力として炉温設定機能部
106内の現状温度計算1によつて現状の炉温及
び鋼片温度を計算する。これらを基に将来の炉温
及び鋼片温度を予測し、昇温パターン計算3では
省エネルギーなどを考慮して昇温パターンを決定
し、1,2,3の計算結果を入力として炉温設定
計算4によつて炉温設定値を決める。こうして炉
温設定機能部106は、決定された設定値を燃料
流量制御部103に与え、炉温測定部104がそ
の設定値になる様にバーナ105によつて加熱さ
れ燃料流量は調節される。
In FIG. 3, 101 is a heating furnace, 102 is an operation information management section, 103 is a fuel flow control section, and 104
1 is a furnace temperature measuring part such as a thermocouple, 105 is a burner, 1
06 is a furnace temperature setting function section. Furnace temperature setting function section 1
06 is roughly divided into four functions: current temperature calculation 1, future temperature calculation 2, temperature increase pattern calculation 3, and furnace temperature setting calculation 4. Logics 1 and 2 have almost the same logic, and have functions for calculating furnace temperature, billet temperature, and billet movement. First, the current furnace temperature and billet temperature are calculated by the current temperature calculation 1 in the furnace temperature setting function section 106 by inputting the billet information and actual fuel flow rate from the operation information management section 102 and the fuel flow rate control section 103. do. Based on these, predict the future furnace temperature and billet temperature, and in temperature increase pattern calculation 3, determine the temperature increase pattern taking into consideration energy saving, etc., and calculate the furnace temperature setting using the calculation results of 1, 2, and 3 as input. 4 to determine the furnace temperature setting. In this way, the furnace temperature setting function section 106 gives the determined set value to the fuel flow rate control section 103, and the furnace temperature measurement section 104 is heated by the burner 105 and the fuel flow rate is adjusted so as to reach the set value.

〔発明の効果〕〔Effect of the invention〕

この発明は以上説明したとおり、各鋼片の炉温
設定値に炉温設定用重み係数を乗じ加重平均した
値を設定炉温とするようにしているので、炉内の
様々な鋼片グループを目標とする昇温パターンで
平均的あるいはある鋼片について優先的に焼き上
げることができる等の効果がある。
As explained above, in this invention, the furnace temperature setting value of each slab is multiplied by the weighting coefficient for furnace temperature setting, and the weighted average value is set as the set furnace temperature. There are effects such as being able to bake averagely or preferentially a certain piece of steel with a targeted temperature increase pattern.

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

第1図は加熱炉の炉温計算ゾーン分割を示す概
略図、第2図は炉温設定値の補正値決定概念図、
第3図はこの発明の一実施態様を示す全体構成図
である。 1……現状温度計算、2……将来温度計算、3
……昇温パターン計算、4……炉温設定計算、1
06……炉温設定機能部。
Figure 1 is a schematic diagram showing the division of furnace temperature calculation zones in the heating furnace, Figure 2 is a conceptual diagram of determining the correction value for the furnace temperature set value,
FIG. 3 is an overall configuration diagram showing one embodiment of the present invention. 1...Current temperature calculation, 2...Future temperature calculation, 3
... Temperature increase pattern calculation, 4 ... Furnace temperature setting calculation, 1
06... Furnace temperature setting function section.

Claims (1)

【特許請求の範囲】 1 複数のゾーンによつて構成される連続式加熱
炉において、上記各ゾーンの炉温及び炉内の鋼片
温度をそれぞれ計算する機能を備え、炉内の複数
の鋼片を省エネルギー等の観点から求められた各
鋼片の昇温パターンに沿つて平均的あるいは所要
の鋼片について優先的に焼き上げるために、各鋼
片の炉温設定値に炉温設定用重み係数を乗じ加重
平均した値を設定炉温とすることを特徴とする連
続式加熱炉の制御方法。 2 各鋼片の炉温設定値を決定するために、制御
用温度計の位置と鋼片の炉温設定用位置とを考慮
しその位置の設定炉温を換算し直して各鋼片の新
たな炉温設定値とすることを特徴とする特許請求
の範囲第1項記載の連続式加熱炉の制御方法。
[Scope of Claims] 1. A continuous heating furnace composed of a plurality of zones, which has a function of calculating the furnace temperature of each zone and the temperature of the steel pieces in the furnace, and In order to bake on average or preferentially the required number of billets according to the temperature increase pattern of each billet determined from the viewpoint of energy saving, etc., a weighting coefficient for furnace temperature setting is added to the furnace temperature setting value of each billet. A control method for a continuous heating furnace, characterized in that a multiplicative weighted average value is set as a set furnace temperature. 2. In order to determine the furnace temperature setting value for each slab, the position of the control thermometer and the furnace temperature setting position of the slab are taken into consideration, and the furnace temperature setting at that position is reconverted and the new furnace temperature for each slab is determined. A method for controlling a continuous heating furnace according to claim 1, characterized in that the furnace temperature is set to a set value.
JP4037885A 1985-02-27 1985-02-27 Method for controlling continuous heating furnace Granted JPS61199017A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4037885A JPS61199017A (en) 1985-02-27 1985-02-27 Method for controlling continuous heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4037885A JPS61199017A (en) 1985-02-27 1985-02-27 Method for controlling continuous heating furnace

Publications (2)

Publication Number Publication Date
JPS61199017A JPS61199017A (en) 1986-09-03
JPH0532447B2 true JPH0532447B2 (en) 1993-05-17

Family

ID=12578985

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4037885A Granted JPS61199017A (en) 1985-02-27 1985-02-27 Method for controlling continuous heating furnace

Country Status (1)

Country Link
JP (1) JPS61199017A (en)

Also Published As

Publication number Publication date
JPS61199017A (en) 1986-09-03

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