JPS639566B2 - - Google Patents
Info
- Publication number
- JPS639566B2 JPS639566B2 JP24568983A JP24568983A JPS639566B2 JP S639566 B2 JPS639566 B2 JP S639566B2 JP 24568983 A JP24568983 A JP 24568983A JP 24568983 A JP24568983 A JP 24568983A JP S639566 B2 JPS639566 B2 JP S639566B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- furnace
- zone
- metal strip
- monitoring zone
- 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
- 238000012544 monitoring process Methods 0.000 claims description 30
- 239000002184 metal Substances 0.000 claims description 24
- 238000002791 soaking Methods 0.000 claims description 24
- 238000010438 heat treatment Methods 0.000 claims description 22
- 238000000137 annealing Methods 0.000 claims description 9
- 238000005192 partition Methods 0.000 claims description 6
- 238000001514 detection method Methods 0.000 claims description 3
- 239000000463 material Substances 0.000 description 8
- 238000010586 diagram Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 2
- 238000009529 body temperature measurement Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
- C21D9/00—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
- C21D9/52—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for wires; for strips ; for rods of unlimited length
- C21D9/54—Furnaces for treating strips or wire
- C21D9/56—Continuous furnaces for strip or wire
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Control Of Heat Treatment Processes (AREA)
- Heat Treatment Of Strip Materials And Filament Materials (AREA)
Description
【発明の詳細な説明】
本発明は金属ストリツプの熱処理を行う連続焼
鈍炉に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a continuous annealing furnace for heat treating metal strip.
一般に連続焼鈍炉においては、要求される製品
の種類に対応して、材質、寸法の異なる金属スト
リツプの各端部を溶接により接続して、連続的に
焼鈍する操業が行なわれている。この場合、金属
ストリツプの材質、寸法に合致した精密な熱処理
を行なわなければならない。 Generally, in a continuous annealing furnace, the ends of metal strips of different materials and sizes are connected by welding and annealed continuously, depending on the type of product required. In this case, precise heat treatment must be performed that matches the material and dimensions of the metal strip.
そこで従来においては、ライン速度、均熱温度
条件、板厚等の条件やヒートバランス式から、各
ゾーンの炉温設定値を計算機により演算し、その
設定炉温により操業されていた。 Therefore, in the past, furnace temperature settings for each zone were calculated using a computer based on conditions such as line speed, soaking temperature conditions, plate thickness, and heat balance equations, and the furnace was operated based on the set furnace temperatures.
しかし、この従来方法では、実際の操業として
は種々の想定されるケースを考え、各々のデータ
を与えてオフラインで計算し、この結果を近似式
化してプロセス計算機に入力し処理するのが一般
的であり、全てのケースで精密な熱処理制御を行
うことは困難で、精度上劣るという欠点が有つ
た。 However, in this conventional method, in actual operations, it is common to consider various possible cases, provide each data, perform offline calculations, and convert the results into approximate formulas and input them into a process computer for processing. However, it is difficult to perform precise heat treatment control in all cases, and there is a drawback that accuracy is poor.
本発明は上述の欠点を解消するために提案され
たもので、複雑な計算を必要とせず、簡単な調節
計のみで安い設備費で精密に金属ストリツプの均
熱温度を制御し、製品品質を向上させる連続焼鈍
炉を提供することを目的とする。 The present invention was proposed in order to solve the above-mentioned drawbacks, and it is possible to precisely control the soaking temperature of a metal strip with a simple controller and low equipment cost without requiring complicated calculations, thereby improving product quality. The purpose is to provide an improved continuous annealing furnace.
本発明の要旨は均熱帯入口部に金属ストリツプ
の目標均熱炉温を維持するため、放散熱量分のみ
の熱量が補償される監視帯を設け、このため監視
帯に入つてくる金属ストリツプの温度によつて監
視帯の炉温が変化するため、その変化分により加
熱帯各ゾーンの炉温をフイードバツク制御する連
続焼鈍炉である。 The gist of the present invention is to provide a monitoring zone at the entrance of the soaking zone that compensates for only the amount of heat dissipated in order to maintain the target soaking furnace temperature of the metal strip. This is a continuous annealing furnace in which the furnace temperature in each zone of the heating zone is feedback-controlled based on the change in furnace temperature in the monitoring zone.
まず、本発明の成立の前提知見について電熱ヒ
ータ方式の横型連続焼鈍炉で説明する。 First, the premise of the establishment of the present invention will be explained using an electric heater type horizontal continuous annealing furnace.
連続焼鈍炉で金属ストリツプを目標温度で均熱
する場合、理想的には無限に長い炉を設け全ゾー
ンをその目標温度に等しい炉温にしてやればよ
い。しかし、このような炉を設けることは実際上
は困難であるため、ライン速度を極力下げて均熱
する方法がとられる。しかし、最近の省エネルギ
ー、ラインの高速化の指向のため、炉温のハイヘ
ツド化が促進されてきており、例えば、第1図で
示されるような炉温分布で目標とする金属ストリ
ツプの昇温パターンAを得ようとするものであ
る。本発明では、加熱帯6と均熱帯7の間にその
放散熱量分のみの熱量が補償される監視帯5を設
け、この監視帯5の炉温を金属ストリツプの目標
均熱温度Aaに常に保つ。ここで金属ストリツプ
が理想の昇温パターンAで加熱された場合、監視
帯5には金属ストリツプは目標均熱温度Aaとほ
ぼ同温のAiの温度で入りAoの温度で出て行く。
もし、金属ストリツプが何らかの原因で昇温パタ
ーンBをとると、監視帯5の入口の材温はBi、
出口の材温はBoとなり、そのときの監視帯5の
炉温はBaは
Bi=Ba−ΔB1≦Ba−ΔB2=Bo≦Ba ……(1)
という関係を満足する。 When soaking a metal strip at a target temperature in a continuous annealing furnace, ideally an infinitely long furnace would be provided and all zones would be brought to a furnace temperature equal to the target temperature. However, since it is practically difficult to provide such a furnace, a method is used to uniformly heat the product by lowering the line speed as much as possible. However, due to the recent trend toward energy conservation and higher line speeds, higher head furnace temperatures are being promoted. The goal is to get an A. In the present invention, a monitoring zone 5 is provided between the heating zone 6 and the soaking zone 7 in which the amount of heat radiated is compensated for, and the furnace temperature in this monitoring zone 5 is always maintained at the target soaking temperature Aa of the metal strip. . When the metal strip is heated according to the ideal temperature increase pattern A, the metal strip enters the monitoring zone 5 at a temperature Ai, which is approximately the same as the target soaking temperature Aa, and exits at a temperature Ao.
If the metal strip adopts temperature rise pattern B for some reason, the material temperature at the entrance of monitoring zone 5 will be Bi,
The material temperature at the outlet is Bo, and the furnace temperature Ba in the monitoring zone 5 at that time satisfies the following relationship: Bi=Ba−ΔB1≦Ba−ΔB2=Bo≦Ba (1).
逆に金属ストリツプが昇温パターンCをとつた
とすると、監視帯5の入口の材温はCi、出口の材
温はCoなり、そのときの監視帯5の炉温Caは
Ci=Ca+ΔC1≧Ca+ΔC2=Co≧Ca ……(2)
なる関係を満足する。 Conversely, if the metal strip follows temperature increase pattern C, the material temperature at the entrance of the monitoring zone 5 is Ci, the material temperature at the exit is Co, and the furnace temperature Ca of the monitoring zone 5 at that time is Ci=Ca+ΔC1≧Ca+ΔC2 =Co≧Ca ……(2) Satisfies the relationship.
ここで、
ΔB1、ΔB2、ΔC1、ΔC2は炉温と材温の温度偏
差量である。 Here, ΔB1, ΔB2, ΔC1, and ΔC2 are the temperature deviation amounts between the furnace temperature and the material temperature.
従つて、監視帯5の炉温がBaとなつたとき、
第6、第5、第4ゾーン…と順次加熱帯7の炉温
を上げることにより、監視帯5の炉温をBaから
Aaになるようにすれば、昇温パターンはBから
Aへと変化し、最適な昇温パターン、すなわち最
適な均熱条件が整う。 Therefore, when the furnace temperature in monitoring zone 5 reaches Ba,
By increasing the furnace temperature of the heating zone 7 sequentially in the 6th, 5th, 4th zones, etc., the furnace temperature of the monitoring zone 5 is raised from Ba to
If Aa is set, the temperature increase pattern changes from B to A, and the optimum temperature increase pattern, that is, the optimum soaking condition is established.
また逆に監視帯の炉温がCaとなつたときも同
様に、第6、第5、第4ゾーン…と順次加熱帯7
の炉温を下げることにより、監視帯5の炉温を
CaからAaになるようにすれば、昇温パターンは
CからAへと変化し、最適な昇温パターン、すな
わち最適な均熱条件が整う。 Conversely, when the furnace temperature in the monitoring zone reaches Ca, the heating zone
By lowering the furnace temperature in monitoring zone 5,
If Ca is changed to Aa, the temperature increase pattern changes from C to A, and the optimum temperature increase pattern, that is, the optimum soaking conditions are established.
以下、本発明を図面を参照してその実施例に基
づいて説明する。 DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below based on embodiments with reference to the drawings.
第2図に示されるように仕切り壁4,4…を配
設し仕切ることによつて、加熱帯6と均熱帯7の
間に監視帯5を設ける。このような仕切り壁4,
4…を配設することにより、監視帯5の炉温が加
熱帯6、均熱帯7の炉温に影響されず動立し、制
御の精度が向上する。さらにこの監視帯5内に放
散熱量分のみの熱量を補償する第1の加熱手段で
あるヒータ10が配設される。このヒータ10は
制御装置13に接続される。この制御装置13は
さらに監視帯5内に配設された炉温検出手段であ
る熱電対8および加熱帯6に配設されたヒータ1
2に接続される。 As shown in FIG. 2, a monitoring zone 5 is provided between the heating zone 6 and the soaking zone 7 by arranging and partitioning the zones with partition walls 4, 4, . Such a partition wall 4,
4..., the furnace temperature in the monitoring zone 5 is not affected by the furnace temperatures in the heating zone 6 and the soaking zone 7, and the accuracy of control is improved. Furthermore, within this monitoring zone 5, a heater 10, which is a first heating means, is arranged to compensate for the amount of heat that is radiated. This heater 10 is connected to a control device 13. This control device 13 further includes a thermocouple 8 which is a furnace temperature detection means disposed in the monitoring zone 5 and a heater 1 disposed in the heating zone 6.
Connected to 2.
次に本実施例の動作について説明する。 Next, the operation of this embodiment will be explained.
炉1内をハースロール3によつて金属ストリツ
プ2が通過する。まず、監視帯5を空炉状態で昇
熱させた場合の第3図に示されるような予め求め
られた保熱炉温と投入熱量の関係を制御装置13
に記憶させ、また目標均熱炉温も設定される。こ
のように準備された連続焼鈍炉で操業をする場
合、まず均熱帯7、監視帯5をその金属ストリツ
プ2の目標均熱温度にし、加熱帯6は処理量に見
合つた設定温度にする。このとき、制御装置13
により制御される第一の加熱手段であるヒータ1
0によつて、第3図に示される関係に基づき決定
される熱量が監視帯5に投入され放散分の熱量が
補償される。この状態で金属ストリツプ2を通板
させ、金属ストリツプ2が最適昇温パターンAで
昇温されると、監視帯5の温度は変化せず、目標
均熱温度のままであるが、熱電対8によつて測定
された温度が、目標均熱温度と比較され、金属ス
トリツプの温度に影響され偏差が生じた場合は、
その偏差量に見合つた熱量を加熱帯6の炉温制御
系である第2の加熱手段であるヒータ12に加え
る。均熱時間の異なる材質や、ライン速度が変化
する場合は、監止帯5の位置をその都度選択でき
るように仕切り壁4,4…を着脱自在に所要位置
に配設する構成にしておけば、より柔軟な操業が
可能となる。また簡易的には仕切り壁がなくても
実現は可能である。 A metal strip 2 is passed through a furnace 1 by means of hearth rolls 3. First, the control device 13 calculates the relationship between the predetermined heat retention furnace temperature and the input heat amount as shown in FIG. 3 when the monitoring zone 5 is heated in an empty furnace state.
The target soaking furnace temperature is also set. When operating the continuous annealing furnace prepared in this manner, first the soaking zone 7 and monitoring zone 5 are set to the target soaking temperature of the metal strip 2, and the heating zone 6 is set to a set temperature commensurate with the throughput. At this time, the control device 13
Heater 1 which is the first heating means controlled by
0, the amount of heat determined based on the relationship shown in FIG. 3 is injected into the monitoring zone 5, and the amount of heat dissipated is compensated. When the metal strip 2 is passed through the metal strip 2 in this state and the temperature of the metal strip 2 is raised according to the optimum temperature increase pattern A, the temperature of the monitoring zone 5 does not change and remains at the target soaking temperature, but the thermocouple 8 The temperature measured by
An amount of heat commensurate with the amount of deviation is applied to the heater 12 which is the second heating means which is the furnace temperature control system of the heating zone 6. When using materials with different soaking times or changing line speeds, it is recommended to configure the partition walls 4, 4, etc. to be removably installed at desired positions so that the position of the guard zone 5 can be selected each time. , enabling more flexible operations. In addition, it can be realized simply without a partition wall.
本発明は以上説明したように簡単な温度制御系
で、直接金属ストリツプを測温する必要もなくま
た複雑な計算を必要とせず安い設備費で、金属ス
トリツプの均熱温度を精密に制御できるため製品
品質が向上するという効果を奏する。 As explained above, the present invention uses a simple temperature control system, does not require direct temperature measurement of the metal strip, does not require complicated calculations, and can precisely control the soaking temperature of the metal strip with low equipment costs. This has the effect of improving product quality.
第1図は金属ストリツプの昇温パターンと監視
帯の炉温の関係説明図、第2図は本発明の一実施
例の構成図、第3図は第2図の実施例の監視帯に
おける空炉状態で予め求められた保熱炉温と投入
熱量の関係説明図である。
1……炉、2……金属ストリツプ、3……ハー
スロール、4……仕切り壁、5……監視帯、6…
…加熱帯、7……均熱帯、8……熱電対、10,
12……ヒータ、13……制御装置。
Fig. 1 is an explanatory diagram of the relationship between the temperature rise pattern of the metal strip and the furnace temperature of the monitoring zone, Fig. 2 is a configuration diagram of an embodiment of the present invention, and Fig. 3 is an illustration of the relationship between the heating pattern of the metal strip and the furnace temperature of the monitoring zone. It is an explanatory diagram of the relationship between the heat retention furnace temperature and the input heat amount, which are determined in advance in the furnace state. 1... Furnace, 2... Metal strip, 3... Hearth roll, 4... Partition wall, 5... Monitoring strip, 6...
...Heating zone, 7...Soaking zone, 8...Thermocouple, 10,
12... Heater, 13... Control device.
Claims (1)
気温度を調節することにより行なう連続焼鈍炉に
おいて、 加熱帯と均熱帯間に仕切り壁が配設されること
により形成される監視帯と、該監視帯内において
予め求められた所定の放散分の熱量のみを補償
し、該金属ストリツプの目標均熱温度を維持させ
る第1の加熱手段と、該監視帯を通過する金属ス
トリツプの温度により変化する該監視帯内の炉温
を検出する炉温検出手段と、該加熱帯の炉温を制
御する第2の加熱手段と、該目標均熱温度が設定
され、該炉温検出手段からの信号により該監視帯
の炉温と該目標均熱温度との偏差により、該監視
帯の炉温が該目標均熱温度になるように、該第2
の加熱手段をフイードバツク制御する制御手段と
を備えたことを特徴とする連続焼鈍炉。[Claims] 1. In a continuous annealing furnace in which the temperature of the metal strip in the furnace is controlled by adjusting the atmospheric temperature in the furnace, a partition wall is provided between a heating zone and a soaking zone. a monitoring zone; a first heating means for compensating only for a predetermined amount of heat dissipated in the monitoring zone to maintain a target soaking temperature of the metal strip; and a metal strip passing through the monitoring zone. Furnace temperature detection means for detecting the furnace temperature within the monitoring zone that changes depending on the temperature of the heating zone; second heating means for controlling the furnace temperature of the heating zone; and the target soaking temperature is set, and the furnace temperature detection means According to a signal from the means, the second temperature is controlled so that the furnace temperature in the monitoring zone becomes the target soaking temperature according to the deviation between the furnace temperature in the monitoring zone and the target soaking temperature.
A continuous annealing furnace characterized by comprising: control means for feedback controlling the heating means of the furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24568983A JPS60141833A (en) | 1983-12-28 | 1983-12-28 | Continuous annealing furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24568983A JPS60141833A (en) | 1983-12-28 | 1983-12-28 | Continuous annealing furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60141833A JPS60141833A (en) | 1985-07-26 |
| JPS639566B2 true JPS639566B2 (en) | 1988-02-29 |
Family
ID=17137345
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24568983A Granted JPS60141833A (en) | 1983-12-28 | 1983-12-28 | Continuous annealing furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60141833A (en) |
-
1983
- 1983-12-28 JP JP24568983A patent/JPS60141833A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60141833A (en) | 1985-07-26 |
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