JPS5952934B2 - Furnace temperature setting method for continuous annealing equipment heating zone - Google Patents
Furnace temperature setting method for continuous annealing equipment heating zoneInfo
- Publication number
- JPS5952934B2 JPS5952934B2 JP15538679A JP15538679A JPS5952934B2 JP S5952934 B2 JPS5952934 B2 JP S5952934B2 JP 15538679 A JP15538679 A JP 15538679A JP 15538679 A JP15538679 A JP 15538679A JP S5952934 B2 JPS5952934 B2 JP S5952934B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace temperature
- zone
- temperature
- strip
- furnace
- 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
Links
- 238000000137 annealing Methods 0.000 title claims description 26
- 238000010438 heat treatment Methods 0.000 title claims description 22
- 238000000034 method Methods 0.000 title claims description 13
- 230000014509 gene expression Effects 0.000 claims description 16
- 238000010586 diagram Methods 0.000 description 5
- 238000001816 cooling Methods 0.000 description 4
- 238000002791 soaking Methods 0.000 description 4
- 238000001514 detection method Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000013178 mathematical model Methods 0.000 description 1
- 239000002436 steel type Substances 0.000 description 1
Landscapes
- Control Of Heat Treatment Processes (AREA)
- Heat Treatment Of Strip Materials And Filament Materials (AREA)
Description
【発明の詳細な説明】
本発明は、焼鈍条件に応じてゾーンごとの炉温制御系の
設定値を変えることによって、炉出ロストリップ温度を
制御する連続焼鈍設備加熱帯において、炉出ロストリッ
プ温度を目標値にし、かつゾーンごとに炉温を異ならし
めるための炉温設定方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a continuous annealing equipment heating zone in which the furnace exit loss strip temperature is controlled by changing the set value of the furnace temperature control system for each zone according to the annealing conditions. This invention relates to a furnace temperature setting method for setting the temperature to a target value and varying the furnace temperature for each zone.
連続焼鈍設備は、例えば第1図に示すように加熱帯1、
第1均熱帯2、第1冷却帯3、第2均熱帯4及び第2冷
却帯5を設け、薄板コイルの後端と別コイルの先端とを
溶接したストリップ6に例えば第2図に示す如く連続的
な熱サイクルを与えるものである。Continuous annealing equipment includes, for example, a heating zone 1, as shown in FIG.
A first soaking zone 2, a first cooling zone 3, a second soaking zone 4, and a second cooling zone 5 are provided, and a strip 6 in which the rear end of a thin plate coil and the tip of another coil are welded is attached to a strip 6, as shown in FIG. 2, for example. It provides a continuous thermal cycle.
連続焼鈍設備の加熱帯1としては、例えば第3図に示す
ようにサクション形のラジアントチューブ7をたてに並
べ該チューブ7中で燃料ガスを燃焼させてラジアントチ
ューブ7を加熱し、その輻射熱によってラジアントチュ
ーブ7列の間にストリップ6を上下に通過させて、これ
を加熱するものがある。The heating zone 1 of the continuous annealing equipment is, for example, as shown in FIG. There is one that heats the strip 6 by passing it up and down between seven rows of radiant tubes.
この連続焼鈍設備加熱帯1における従来のストリップ温
度制御方法としては、例えば炉内を6群のゾーンに分け
て、各ゾーンごとに炉内雰囲気温度を調節し、この調節
により間接的にストリップ温度を制御している。As a conventional strip temperature control method in the continuous annealing equipment heating zone 1, for example, the inside of the furnace is divided into six groups and the furnace atmosphere temperature is adjusted for each zone, and the strip temperature is indirectly controlled by this adjustment. It's in control.
さらに説明すれば各ゾーンごとに炉温検出器8を設け、
また予じめ炉温設定器9に炉温の目標値を設定しておき
、該検出器8で検出された炉温が炉温設定器9の目標値
となるように炉温調節計10で燃料流量調節計11を制
御している。To explain further, a furnace temperature detector 8 is provided for each zone,
Further, a target value of the furnace temperature is set in the furnace temperature setting device 9 in advance, and the furnace temperature controller 10 is set so that the furnace temperature detected by the detector 8 becomes the target value of the furnace temperature setting device 9. It controls the fuel flow rate controller 11.
上記のような加熱帯1においてストリップが蛇行し、あ
るいは形状が不良であるなどの理由で各ゾーンごとに炉
温を異ならせて温度差をつけ、しかも炉出ロストリップ
温度を変えないで操業する場合がある。Due to reasons such as meandering or poor shape of the strip in heating zone 1 as described above, the furnace temperature is varied for each zone to create a temperature difference, and the furnace is operated without changing the loss strip temperature. There are cases.
この場合、従来は運転員の経験にたよって炉温設定値を
決めていたが、このようにすると運転員の作業が煩雑に
なり、しかも運転員が炉出口にストリップ温度検出器8
の検出値を見なから炉温設定しても運転員の経験やカン
に頼らねばならずスl−IJツブ温度制御精度が悪いな
どの問題があった。In this case, conventionally, the furnace temperature setting value was determined based on the operator's experience, but this would complicate the operator's work.
Even if the furnace temperature is set without looking at the detected value, the operator has to rely on his or her experience and intuition, resulting in problems such as poor control accuracy of the sl-IJ tube temperature.
本発明はこのような事情を考慮してなされたもので、そ
の目的とするところは、各ゾーンごとに炉温を異ならし
める場合、炉温を自動設定することにより、運転員の作
業の軽減化を図るとともに作業ミスをなくし、温度制御
精度を高めて製品品質向上および均一化を図ることがで
きる連続焼鈍設備加熱帯の炉温設定方法を得んとするも
のである。The present invention was made in consideration of these circumstances, and its purpose is to reduce the work of the operator by automatically setting the furnace temperature when the furnace temperature is different for each zone. The present invention aims to provide a method for setting a furnace temperature in a heating zone of continuous annealing equipment, which can eliminate work errors, improve temperature control precision, and improve product quality and uniformity.
すなわち本発明は焼鈍条件に応じてゾーンごとに設置さ
れた炉温調節計の設定値を変えることによって連続焼鈍
設備加熱帯出ロストリップ温度を制御する方法において
、ゾーンごとに炉温に所定の差をつけたい場合には前記
ストリップ温度に応じたゾーンごとに変わらない一定炉
温と焼鈍条件との関係式Aおよび各ゾーンの炉温の前記
一定値からの変化量に対する前記ストリップ温度の変化
量の比すなわち影響係数と焼鈍条件との関係式Bをあら
かじめ求めておき、まず関係式Aを用いて一定炉温を求
め、該一定炉温と必要とする炉温差から前記関係式Bを
用いせ前記ス) IJツブ温度は変えないような該一定
炉温と各ゾーン炉温との差を求め、その差から得た各ゾ
ーンの炉温を炉温調節計に設定することを特徴とする連
続焼鈍設備加熱帯の炉温設定方法である。That is, the present invention is a method for controlling the heating strip temperature of continuous annealing equipment by changing the set value of the furnace temperature controller installed in each zone according to the annealing conditions, and the present invention provides a method for controlling the temperature of the heating strip of the continuous annealing equipment by changing the setting value of the furnace temperature controller installed in each zone according to the annealing conditions. If desired, use the relational expression A between a constant furnace temperature that does not change for each zone according to the strip temperature and annealing conditions, and the ratio of the amount of change in the strip temperature to the amount of change from the constant value in the furnace temperature of each zone. That is, a relational expression B between the influence coefficient and annealing conditions is determined in advance, a constant furnace temperature is first obtained using the relational expression A, and the above-mentioned relational expression B is used from the constant furnace temperature and the required furnace temperature difference. ) Continuous annealing equipment characterized in that the difference between the constant furnace temperature and the furnace temperature of each zone is determined without changing the IJ tube temperature, and the furnace temperature of each zone obtained from the difference is set on a furnace temperature controller. This is a method of setting the furnace temperature of the heating zone.
この場合、上記関係式A、 Bは実績データの整理あ
るいは理論的な熱収支の数式モデルなどによってあらか
じめ求めておけばよい。In this case, the above-mentioned relational expressions A and B may be determined in advance by sorting out actual data or using a theoretical mathematical model of heat balance.
以下本発明方法を第4図に示した実施例にもとづいて説
明する。The method of the present invention will be explained below based on the embodiment shown in FIG.
この例では本発明を実現する主な演算は計算機(ミニコ
ン、マイコン、大型計算機等)によって行なわれるもの
である。In this example, the main operations for realizing the present invention are performed by a computer (minicomputer, microcomputer, large computer, etc.).
図中の記号a、iは計算機12へのインプット信号、記
号ji(i=1〜6)は計算機12からのアウトプット
信号でありその記号内容は以下の通りである。Symbols a and i in the figure are input signals to the computer 12, and symbols ji (i=1 to 6) are output signals from the computer 12, and the contents of the symbols are as follows.
1)インプット
a・・・・・・加熱帯出ロストリップ温度検出器13に
よる検出信号
bl・・・・・・第iゾーン炉温検出器8による検出信
号 (i=1〜6)
C・・・・・・ライン速度検出器14による検出信号d
・・・・・・板厚
e・・・・・・板幅 ・
f・・・・・・鋼種
g・・・・・・焼鈍速度 (目標値)
h・・・・・・加熱帯出ロストリップ温度 (目標値
)
i・・・・・弔標炉温温度差
この場合d−iは各コイルごとに計算機にインプットす
る。1) Input a...Detection signal by the heating strip loss strip temperature detector 13...Detection signal by the i-th zone furnace temperature detector 8 (i=1 to 6) C... ...Detection signal d by line speed detector 14
...Plate thickness e...Plate width f...Steel type g...Annealing speed (target value) h...Heating strip loss strip Temperature (target value) i...Memorial furnace temperature temperature difference In this case, d-i is input into the computer for each coil.
2)アウトプツ1〜
J+・・・・・・炉温設定器9に入力する第五ゾーン炉
温制御系設定値信号
上記焼鈍条件a−41及び第5図に示すような目標炉温
温度差(ΔTz)が計算機12に入力されると、計算機
12は次のようにして各ゾーンの炉温設定値を求める。2) Outputs 1 to J+...Fifth zone furnace temperature control system set value signal input to furnace temperature setting device 9 Target furnace temperature temperature difference (as shown in the above annealing condition a-41 and FIG. 5) When ΔTz) is input to the computer 12, the computer 12 determines the furnace temperature setting value for each zone in the following manner.
まず計算機12には予ヒめ関係式A及びBが入力されて
いる。First, relational expressions A and B are input into the calculator 12 in advance.
関係式Aは下記式で示される。Relational expression A is expressed by the following expression.
Tzo=fC(ts、W5.V5.Ts)又関係式Bは
下記式で示される。Tzo=fC(ts, W5.V5.Ts) Also, relational expression B is expressed by the following expression.
C1=4. (t59w8.v5.Ts)これら関係式
A及びBにおいて、
t5:板厚 0→Ws:板幅
0→v5 ニライン速度
(mpm)T5 :加熱帯出ロス
トIJツブ温度(目標値)(C)Tzi ’第iゾーン
炉温設定値 (0)T2o:各ゾーン一定
にしたときの炉温 (C)fo :各ゾーン一定の
炉温を求める関係式A(0)ΔT :目標炉温温度差
(C)ΔTzi ” l Tzi
−Tzo l (C)(=Oi ) :
第iゾーン炉温の加熱帯出口 (−)ストリップ温度に
及ぼす影響
係数(各ゾーンの炉温の一定
値からの変化量に対するスト
リップ温度の変化量の比)
′i″贋゛翼蒜±7..6if!i、a*x+この関係
式Aから計算機12に入力した焼鈍条件を入れて一定炉
温Tzoを求め、この一定炉温Tzoと必要とする炉温
差ΔTzから関係式Bを用いてストリップ温度Tsは変
えないような該一定炉温Tzoと各ゾーン炉温Tziと
の差ΔTziを求め、この差から各ゾーンの炉温Tzi
を得る。C1=4. (t59w8.v5.Ts) In these relational expressions A and B, t5: plate thickness 0→Ws: plate width
0→v5 Niline speed
(mpm) T5: Heating zone lost IJ tube temperature (target value) (C) Tzi' i-th zone furnace temperature setting value (0) T2o: Furnace temperature when each zone is constant (C) fo: Each zone is constant Relational formula for determining furnace temperature A(0)ΔT: Target furnace temperature temperature difference
(C) ΔTzi ” l Tzi
−Tzo l (C) (=Oi):
Influence coefficient of i-th zone furnace temperature on heating zone exit (-) Strip temperature (ratio of change in strip temperature to change in furnace temperature in each zone from a constant value) ′i″ ゛wings ±7. .6if!i, a*x + From this relational expression A, enter the annealing conditions input into the calculator 12 to obtain a constant furnace temperature Tzo, and use relational expression B from this constant furnace temperature Tzo and the required furnace temperature difference ΔTz to perform stripping. The difference ΔTzi between the constant furnace temperature Tzo and each zone furnace temperature Tzi without changing the temperature Ts is determined, and from this difference, the furnace temperature Tzi of each zone is determined.
get.
すなわち目標炉温温度差ΔTz及びΔTzi (Tzi
−TzO)から次のような連立方程式が得られ、これを
解くことにより各ゾーン炉温設定値が求まる。That is, the target furnace temperature temperature difference ΔTz and ΔTzi (Tzi
-TzO), the following simultaneous equations are obtained, and by solving these, the furnace temperature set value for each zone is determined.
−C,ΔTZ1−C2ΔTz2−c3ΔTz3+C4Δ
Tz4+C5ΔTz5+C6ΔTz6= O(1)ΔT
z1−ΔTz2=ΔTz3(2)
ΔTz4=ΔTz5−ΔTZ6(3)
ΔTz1+ΔTz4−ΔTz (
4)これを解けばΔTziが求まる。-C, ΔTZ1-C2ΔTz2-c3ΔTz3+C4Δ
Tz4+C5ΔTz5+C6ΔTz6= O(1)ΔT
z1-ΔTz2=ΔTz3(2) ΔTz4=ΔTz5-ΔTZ6(3) ΔTz1+ΔTz4-ΔTz (
4) By solving this, ΔTzi can be found.
すなわち式(2)。(3)を式(1)に代入すれば
−(C1+C2+ C3)ΔTZ1+(C4+C5+C
6)ΔTz4= 0
(5)(4)を(5)に代入すれば
(C4+C5+C6) (ΔTz−ΔTz4)+(C
4+C5+C6)ΔTZ4−0
−(C1+q十C3)ΔTZ+ (CI+C2+C3+
C4+C5+C6)ΔTz4−0
ΔTz1−ΔTz−ΔTz4(7)
ΔTz2−ΔTz1(8)
ΔTz3=ΔTz1(9)
ΔTz5=ΔTz4(10)
ΔTz6=ΔTz4(11)
故に各ゾーン炉温設定値は以下の式で求まる。That is, equation (2). Substituting (3) into equation (1) gives -(C1+C2+C3)ΔTZ1+(C4+C5+C
6)ΔTz4=0
(5) Substituting (4) into (5), we get (C4+C5+C6) (ΔTz-ΔTz4)+(C
4+C5+C6)ΔTZ4-0 −(C1+q0C3)ΔTZ+ (CI+C2+C3+
C4+C5+C6) ΔTz4-0 ΔTz1-ΔTz-ΔTz4(7) ΔTz2-ΔTz1(8) ΔTz3=ΔTz1(9) ΔTz5=ΔTz4(10) ΔTz6=ΔTz4(11) Therefore, the furnace temperature settings for each zone are as follows. It is found by the formula of .
Tzi = Tzo−ΔTzi(i=1−3)Tzi
= Tzo+ΔTzi (i = 4〜6)以上説明し
たように本発明によればストリップ蛇行防止などのため
連続焼鈍設備加熱帯の各ゾーンの炉温を炉出ロストリッ
プ温度を変えないで異なる値にしたい場合に所定の炉温
、温度差を与えれば自動的に各ゾーン炉温設定値を計算
し、その設定値に対して炉温制御するので運転員の煩雑
な作業をなくし、従来の如く運転員の経験にたよらずに
実験式または伝熱計算による理論式により自動的に設定
変更するので加熱帯出ロストリップ温度の変動が少なく
なり製品品質の向上、均一化が可能となるなど顕著な効
果を奏する。Tzi = Tzo-ΔTzi (i=1-3)Tzi
= Tzo + ΔTzi (i = 4 to 6) As explained above, according to the present invention, in order to prevent strip meandering, etc., it is desired to set the furnace temperature of each zone of the continuous annealing equipment heating zone to a different value without changing the furnace exit loss strip temperature. When a predetermined furnace temperature and temperature difference are given, the furnace temperature setting value for each zone is automatically calculated, and the furnace temperature is controlled based on the set value, eliminating the complicated work of the operator. Since the settings are automatically changed using experimental formulas or theoretical formulas based on heat transfer calculations without relying on experience, fluctuations in the temperature of the heating strip loss strip are reduced, resulting in remarkable effects such as improved product quality and uniformity. .
第1図は連続焼鈍設備の1概要図であり、第2図は連続
焼鈍設備において熱処理する熱サイクルの1例を示す説
明図であり、第3図は従来の連続焼鈍設備加熱帯のスト
リップ温度制御方法を示す説明図であり、第4図は本発
明方法の1実施例を示したストリップ温度制御方法の説
明図、第5図は各ゾーンの目標炉温温度差を示す説明図
である。
1・・・・・・加熱帯、2・・・・・・第1均熱帯、3
・・・・・・第1冷却帯、4・・・・・・第2均熱帯、
5・・・・・・第2冷却帯、6・・・・・・ストリップ
、7・・曲ラジアントチューブ、8・・・・・・炉温検
出器、9・・・・・・炉温設定器、1o・・聞炉温調節
計、11・・・・・・燃料流量調節計、12・曲・計算
機、13・・・・・・加熱帯出ロスl−IJツブ温度検
出器、14・・・・・・ゾーン炉温検出器、15・・間
ライン速度検出器。Fig. 1 is a schematic diagram of continuous annealing equipment, Fig. 2 is an explanatory diagram showing an example of a thermal cycle for heat treatment in continuous annealing equipment, and Fig. 3 is a strip temperature of the heating zone of conventional continuous annealing equipment. 4 is an explanatory diagram showing a control method, FIG. 4 is an explanatory diagram of a strip temperature control method showing one embodiment of the method of the present invention, and FIG. 5 is an explanatory diagram showing a target furnace temperature temperature difference in each zone. 1... Heating zone, 2... First soaking zone, 3
...First cooling zone, 4...Second soaking zone,
5...Second cooling zone, 6...Strip, 7...Curved radiant tube, 8...Furnace temperature detector, 9...Furnace temperature setting equipment, 1o... Furnace temperature controller, 11... Fuel flow rate controller, 12... Song/calculator, 13... Heating zone loss l-IJ tube temperature detector, 14... ...Zone furnace temperature detector, 15... line speed detector.
Claims (1)
計の設定値を変えて出口ストリップ温度を制御する連続
焼鈍設備加熱帯の炉温設定方法において、前記ストリッ
プ温度に応じたゾーンごとに変わらない一定炉温と焼鈍
条件との関係式A、および各ゾーンの炉温の前記一定値
からの変化量に対する前記ストリップ温度の変化量の比
と焼鈍条件との関係式Bを予じめ求めておき、関係式A
から一定炉温を求めるとともに該一定炉温と必要とする
炉温差とから前記関係式Bにより前記ストリップ温度を
変えないような該一定炉温と各ゾーン炉温との差を求め
、しかる後その差から得た各ゾーンの炉温を上記炉温調
節計に設定することを特徴とする連続焼鈍設備加熱帯の
炉温設定方法。1. In a furnace temperature setting method for a continuous annealing equipment heating zone in which the outlet strip temperature is controlled by changing the set value of a furnace temperature controller installed in each zone according to the annealing conditions, the furnace temperature is changed for each zone according to the strip temperature. A relational expression A between the constant furnace temperature and the annealing conditions, and a relational expression B between the annealing conditions and the ratio of the amount of change in the strip temperature to the amount of change from the constant value of the furnace temperature in each zone are determined in advance. Ok, relational expression A
From the constant furnace temperature and the required furnace temperature difference, find the difference between the constant furnace temperature and each zone furnace temperature that does not change the strip temperature using the relational formula B, and then A method for setting a furnace temperature in a heating zone of continuous annealing equipment, characterized in that the furnace temperature of each zone obtained from the difference is set in the furnace temperature controller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15538679A JPS5952934B2 (en) | 1979-11-30 | 1979-11-30 | Furnace temperature setting method for continuous annealing equipment heating zone |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15538679A JPS5952934B2 (en) | 1979-11-30 | 1979-11-30 | Furnace temperature setting method for continuous annealing equipment heating zone |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5677335A JPS5677335A (en) | 1981-06-25 |
| JPS5952934B2 true JPS5952934B2 (en) | 1984-12-22 |
Family
ID=15604807
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15538679A Expired JPS5952934B2 (en) | 1979-11-30 | 1979-11-30 | Furnace temperature setting method for continuous annealing equipment heating zone |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5952934B2 (en) |
-
1979
- 1979-11-30 JP JP15538679A patent/JPS5952934B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5677335A (en) | 1981-06-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1055317C (en) | On-line Control Method of Continuous Annealing Furnace | |
| JPS6227135B2 (en) | ||
| CN104894362A (en) | Method for setting temperature of heating furnace in cold and hot steel billet mixed loading | |
| JPS5952934B2 (en) | Furnace temperature setting method for continuous annealing equipment heating zone | |
| CN110398158A (en) | A kind of furnace temperature of heating furnace intelligence setting method | |
| JPS6289821A (en) | Line speed controlling method for continuous annealing equipment | |
| JPH0564687B2 (en) | ||
| CN116219154B (en) | A method and device for controlling the temperature of strip steel continuous annealing | |
| CN101131572B (en) | System for fast cooling temperature control | |
| JPS5754229A (en) | Control system for plate temperature in continuous furnace | |
| SU572639A1 (en) | Method of automatic control of heat-exchange apparatus | |
| JPS5823447B2 (en) | Heat pattern optimization control method | |
| JPH0610057A (en) | Plate furnace heating furnace plate temperature control method and device | |
| JPH04246130A (en) | Method for controlling flow rate of combustion gas in continuous annealing furnace | |
| KR100250760B1 (en) | Controlling method for steel heat treatment in continuous furnace | |
| JPS61279625A (en) | Method for controlling slab heating furnace | |
| JPH0658610B2 (en) | Temperature control method for distribution device | |
| SU974083A1 (en) | Method and device for controlling furnace thermal mode | |
| JPH0135895B2 (en) | ||
| JPH0328488B2 (en) | ||
| JPS5831372B2 (en) | Continuous annealing method | |
| JPS6070127A (en) | Method for controlling temperature of strip with continuous annealing furnace | |
| SU964015A1 (en) | Method for controlling billet heating in multiple-zone heating furnace | |
| JPS62101037A (en) | Control system of temperature of wafer in oxidizing and diffusing device | |
| JPH03120320A (en) | Sheet temperature control method for continuous annealing furnace |