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JPS6216257B2 - - Google Patents
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JPS6216257B2 - - Google Patents

Info

Publication number
JPS6216257B2
JPS6216257B2 JP16194581A JP16194581A JPS6216257B2 JP S6216257 B2 JPS6216257 B2 JP S6216257B2 JP 16194581 A JP16194581 A JP 16194581A JP 16194581 A JP16194581 A JP 16194581A JP S6216257 B2 JPS6216257 B2 JP S6216257B2
Authority
JP
Japan
Prior art keywords
catenary
strip
amount
sectional area
leading
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
Application number
JP16194581A
Other languages
Japanese (ja)
Other versions
JPS5864318A (en
Inventor
Shigetada Oosaki
Norikatsu Yoshimoto
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 JP16194581A priority Critical patent/JPS5864318A/en
Publication of JPS5864318A publication Critical patent/JPS5864318A/en
Publication of JPS6216257B2 publication Critical patent/JPS6216257B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21DMODIFYING 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
    • C21D9/00Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
    • C21D9/52Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for wires; for strips ; for rods of unlimited length
    • C21D9/54Furnaces for treating strips or wire
    • C21D9/56Continuous 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】 本発明はストリツプをカテナリー状で連続的に
加熱する場合において該ストリツプのカテナリー
量を制御する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for controlling the catenary amount of a strip when the strip is continuously heated in a catenary manner.

ストリツプを連続的に加熱する方法として、第
1図に示すように先行ストリツプSt1の末端と後
行ストリツプSt2の先端との接合部S0を溶接等で
順次接合し、連続的に加熱炉1内に供給し加熱す
る方法がある。
As shown in Fig. 1, a method for continuously heating the strip is to sequentially join the joint S0 between the end of the leading strip St1 and the tip of the trailing strip St2 by welding, etc., and then heat the strip continuously in a heating furnace. There is a method of supplying it into a chamber and heating it.

このような加熱炉内のカテナリー量は少なすぎ
るとストリツプにかかる張力が過大となりストリ
ツプの異常伸び又は破断を生じることがあり、多
すぎるとストリツプが炉床に接触し表面に疵を付
けてしまうことがある。また炉床への接触を防ぐ
ため炉内を大きくとると、炉の昇温のために無駄
な燃料を必要とする。また加熱用バーナーの直近
とこれより離れたところでは温度に差が生じ、炉
内の温度分布を均一にすることが困難となる。こ
のため、カテナリー量の変化によりストリツプの
昇温履歴にばらつきを生じ品質安定化の上で問題
がある。このため加熱炉内の大きさはストリツプ
に過大の張力がかからない程度のカテナリー量を
許容する範囲で可能な限り小さくする必要があ
り、またカテナリー量はこのような小さな炉内に
おいてもストリツプが炉床に接触せずかつ加熱用
バーナーから常に一定距離を通板するように制御
しなければならない。
If the amount of catenary in the heating furnace is too small, the tension applied to the strip will be excessive, which may cause abnormal elongation or breakage of the strip, and if it is too large, the strip may come into contact with the hearth and cause scratches on the surface. There is. Furthermore, if the inside of the furnace is made large to prevent contact with the hearth, fuel will be wasted to raise the temperature of the furnace. Furthermore, there is a difference in temperature between the area immediately adjacent to the heating burner and the area further away from the heating burner, making it difficult to make the temperature distribution within the furnace uniform. Therefore, variations in the amount of catenary cause variations in the temperature rise history of the strip, which poses a problem in terms of quality stabilization. For this reason, the size of the heating furnace must be as small as possible to allow for the amount of catenary that does not apply excessive tension to the strip. It must be controlled so that the sheet does not come into contact with the heating burner and always passes at a certain distance from the heating burner.

ところでカテナリー量を一定に制御する従来方
法は、ロードセル等を付設したロールをストリツ
プに押付けて、間接的にストリツプの張力を測定
し、この値により第1図のブライドルロール3あ
るいは4のトルクをコントロールする方法、ある
いは第1図の加熱炉1に取付けたカテナリー量検
出器2によりストリツプSのカテナリー量を直接
検出し、この検出信号とカテナリー量設定値とを
比較演算して入側ブライドル3のスピードをコン
トロールして(この場合出側ブライドル4のスピ
ードは一定値に固定)、カテナリー量一定制御を
行う方法等がある。
By the way, the conventional method of controlling the catenary amount at a constant level is to press a roll equipped with a load cell or the like against the strip, indirectly measure the tension of the strip, and use this value to control the torque of the bridle roll 3 or 4 in Fig. 1. Alternatively, the catenary amount of the strip S is directly detected by the catenary amount detector 2 attached to the heating furnace 1 shown in FIG. (in this case, the speed of the exit bridle 4 is fixed at a constant value) to control the catenary amount at a constant value.

しかしながら第2図のロ,ハのようにストリツ
プの接合部S0を境にして先行ストリツプSt1と後
行ストリツプSt2とで断面積、すなわち板厚、板
幅が異なる場合は、カテナリー検出点Pでのカテ
ナリー量により前記のようにしてカテナリー量の
制御を行うと次のような支障をきたす。
However, if the cross-sectional area, that is, the plate thickness and plate width, differ between the leading strip St 1 and the trailing strip St 2 with the strip junction S 0 as the border, as shown in Fig. 2 B and C, the catenary detection point If the catenary amount is controlled as described above using the catenary amount at P, the following problems will occur.

すなわち第2図のイは先行ストリツプSt1と後
行ストリツプSt2とが同一断面積の場合のカテナ
リー形成状況を示し、ロは先行ストリツプSt1
断面積大の場合、ハは先行ストリツプSt2が断面
積小の場合のそれぞれカテナリー形成状況を示
す。まずロの場合は、カテナリー量検出点Pのカ
テナリー量が一定になるように制御を行うと先行
ストリツプSt1のカテナリー量が過大になり炉底
部へのストリツプの接触あるいは温度変化を来た
し、品質不良の原因になる。ハの場合は逆に先行
ストリツプSt1の張力が過大になりストリツプ破
断等の原因となる。
In other words, A in Fig. 2 shows the catenary formation situation when the leading strip St 1 and the trailing strip St 2 have the same cross-sectional area, B shows the catenary formation situation when the leading strip St 1 has a large cross-sectional area, and C shows the catenary formation situation when the leading strip St 1 has a large cross-sectional area. shows the catenary formation situation when the cross-sectional area is small. First, in case (b), if the catenary amount at the catenary amount detection point P is controlled to be constant, the amount of catenary in the preceding strip St 1 will become excessive, causing the strip to come into contact with the bottom of the furnace or causing a temperature change, resulting in poor quality. It causes In case C, on the other hand, the tension in the preceding strip St1 becomes excessive, causing the strip to break.

本発明はこのような問題を解決したカテナリー
量の制御方法を提供するものである。
The present invention provides a method for controlling the amount of catenary that solves these problems.

カテナリー量は次式で与えられる。 The catenary quantity is given by the following formula.

y≒ρl/8u 但しρはストリツプの密度、lはストリツプ支
持点間距離、uはストリツプに加わる単位張力、
yはカテナリー量を示す。ここでρ,lが一定で
あれば、 y≒k1/u (kは定数) 従つてカテナリー量yは単位張力uに反比例す
る。ここで単位張力は断面積により変わるため、
先行ストリツプと後行ストリツプのカテナリー量
の差は Δy=t×S/S となる。ここでΔyは先行ストリツプSt1と後行
ストリツプSt2のカテナリー量の差であり、S1
先行材の断面積、S2は後行材の断面積、tはカテ
ナリー検出点での基準カテナリー量を示す。なお
基準カテナリー量とは、許容される最大カテナリ
ー量と最小カテナリー量の合計量の1/2をいう。
y≒ρl 2 /8u where ρ is the density of the strip, l is the distance between the strip support points, u is the unit tension applied to the strip,
y indicates the catenary amount. Here, if ρ and l are constant, y≈k1/u (k is a constant).Therefore, the catenary amount y is inversely proportional to the unit tension u. Here, since the unit tension changes depending on the cross-sectional area,
The difference in catenary amount between the leading strip and the trailing strip is Δy=t×S 1 /S 2 . Here, Δy is the difference in catenary amount between the leading strip St 1 and the trailing strip St 2 , S 1 is the cross-sectional area of the leading strip, S 2 is the cross-sectional area of the trailing strip, and t is the reference catenary at the catenary detection point. Indicate quantity. Note that the standard catenary amount is 1/2 of the total amount of the maximum catenary amount and minimum catenary amount allowed.

以上から先行ストリツプSt1のカテナリー量あ
るいは張力値を適正範囲に維持するためには、カ
テナリー検出点Pでの基準カテナリー量を補正す
ることが必要とされる。補正量として先行ストリ
ツプSt1と後行ストリツプSt2とのカテナリー量の
差Δyの1/2つまりΔy/2だけ基準カテナリー
量を補正することにより、各カテナリー量を基準
カテナリー量に等分に近ずける。即ち、第2図の
ロの場合は後行ストリツプSt2のカテナリー量を
基準カテナリー量よりΔy/2だけ小さくし、ハ
の場合にはΔy/2だけ大きくする。
From the above, in order to maintain the catenary amount or tension value of the preceding strip St 1 within an appropriate range, it is necessary to correct the reference catenary amount at the catenary detection point P. By correcting the reference catenary amount by 1/2 of the difference Δy in the catenary amount between the leading strip St 1 and the trailing strip St 2 , that is, Δy/2, each catenary amount can be made to be approximately equal to the reference catenary amount. I can't stand it. That is, in case (b) of FIG. 2, the catenary amount of the trailing strip St 2 is made smaller than the reference catenary amount by Δy/2, and in case (c), it is made larger by Δy/2.

以上の様にストリツプ接合部S0の位置が炉の入
側に入る点で基準カテナリー量を補正し、炉を出
た点で元の基準カテナリー量に戻すものである。
ストリツプの接合部の位置及び断面積はマニユア
ル設定でもよいが、接合部位置をトラツキングし
て計算機等を使用して自動入力すれば容易に実現
可能である。
As described above, the standard catenary amount is corrected at the point where the strip joint S0 enters the entrance side of the furnace, and is returned to the original standard catenary amount at the point where the strip joint S0 exits the furnace.
The position and cross-sectional area of the joint of the strip may be set manually, but it can be easily realized by tracking the position of the joint and automatically inputting it using a computer or the like.

第3図は補正の接合部S0の位置とカテナリー基
準量補正値との関係を示す。
FIG. 3 shows the relationship between the position of the correction junction S 0 and the catenary reference amount correction value.

第4図は本発明を実施するための回路例であ
る。11の記憶回路には先行材St1の断面積S1
データが、12の記憶回路には後行材St2の断面
積S2のデータが予め入力されている。比較回路1
3では該データS1,S2により先行材と後行材の断
面積比較を行い、後述するカテナリー修正量Δ
y/2(=t/2・S1/S2)を基準カテナリー量
にプラスするか、マイナスするかを判定する。1
4は割算器でありS2/S1の演算を行い、16の割
算器は基準カテナリー設定器15の信号からt/
2の演算を行うものである。掛算器17は割算器
14,16の出力信号からカテナリー修正量Δ
y/2=t/2・S1/S2の演算を行うものであ
る。
FIG. 4 is an example of a circuit for implementing the present invention. The data of the cross-sectional area S 1 of the preceding material St 1 is input in advance to the memory circuit 11, and the data of the cross-sectional area S 2 of the succeeding material St 2 is input in advance to the memory circuit 12. Comparison circuit 1
In 3, the cross-sectional areas of the preceding material and the succeeding material are compared using the data S 1 and S 2 , and the catenary correction amount Δ, which will be described later, is calculated.
It is determined whether y/2 (=t/2·S 1 /S 2 ) is added or subtracted from the reference catenary amount. 1
A divider 4 calculates S 2 /S 1 , and a divider 16 calculates t/S from the signal of the reference catenary setter 15.
This is to perform the calculation of 2. Multiplier 17 calculates the catenary correction amount Δ from the output signals of dividers 14 and 16.
The calculation is y/2=t/2·S 1 /S 2 .

一方、溶接部のトラツキング信号から溶接部が
加熱炉入口に到達すると、該信号によりフリツプ
フロツプ18をセツトし、ゲート回路19を開
く、17の掛算器出力信号が加算器20で基準カ
テナリー信号とプラスされる。24は符号反転回
路で比較回路13で演算された信号により、つま
りS1>S2の場合は側がONされ基準カテナリー
指令値からカテナリー修正量をマイナスすること
になる。逆に、S1>S2の場合は側がONしプラ
スされることになる。該修正された基準カテナリ
ー量指令値はカテナリー制御用回転数制御器21
に入力され、カテナリー量検出器22からの信号
との偏差信号により入側ブライドル25を駆動す
るモータ23の回転数を変化させ、カテナリー量
の修正を行うものである。
On the other hand, when the weld reaches the inlet of the heating furnace from the tracking signal of the weld, the signal sets the flip-flop 18 and opens the gate circuit 19, and the multiplier output signal 17 is added to the reference catenary signal by the adder 20. Ru. Reference numeral 24 denotes a sign inversion circuit which is turned ON by the signal calculated by the comparison circuit 13, that is, when S 1 >S 2 , the catenary correction amount is subtracted from the reference catenary command value. Conversely, if S 1 > S 2 , the side is turned on and becomes positive. The revised reference catenary amount command value is sent to the rotation speed controller 21 for catenary control.
The rotational speed of the motor 23 that drives the entry side bridle 25 is changed based on the deviation signal from the signal from the catenary amount detector 22, thereby correcting the catenary amount.

溶接部信号が炉の出側に到達すると、フリツプ
フロツプ18をリセツトしゲート回路19を閉じ
ることにより、加算器20の出力は基準カテナリ
ー指令値がそのまま出力される。加算器20から
の出力はカテナリー制御用回転数制御器21に入
力され、22のカテナリー量検出信号との偏差信
号により入側ブライドル25を駆動するモータ2
3の回転数を変化させ、基準カテナリー量となる
よう制御する。
When the welding part signal reaches the outlet side of the furnace, the flip-flop 18 is reset and the gate circuit 19 is closed, so that the output of the adder 20 is the reference catenary command value as it is. The output from the adder 20 is input to the catenary control rotation speed controller 21, and the motor 2 drives the entry side bridle 25 based on the deviation signal from the catenary amount detection signal 22.
The rotation speed of 3 is changed to control the reference catenary amount.

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

第1図はストリツプを接続して加熱炉に通す態
様を示す概略図、第2図イ,ロ,ハは先後行スト
リツプのカテナリー形成状況を示す模式図、第3
図は補正の接合部位置とカテナリー基準量補正値
との関係を示す図表、第4図は本発明を実施する
ための回路例である。 St1…先行ストリツプ、St2…後行ストリツプ、
S0…接合部、1…加熱炉、2…カテナリー量検出
器、3,4…ブライドルロール、11,12…記
憶回路、13…比較器、14,16…割算器、1
5…基準カテナリー設定器、17…掛算器、18
…フリツプフロツプ、19…ゲート回路、20…
加算器、21…カテナリー制御用回転数制御器、
22…カテナリー量検出器、23…モータ、24
…符号反転回路。
Fig. 1 is a schematic diagram showing how the strips are connected and passed through a heating furnace; Fig. 2 A, B, and C are schematic diagrams showing how the leading and trailing strips are formed as catenaries;
The figure is a chart showing the relationship between the correction joint position and the catenary reference amount correction value, and FIG. 4 is an example of a circuit for implementing the present invention. St 1 ... Leading strip, St 2 ... Trailing strip,
S0 ...Joint part, 1...Heating furnace, 2...Catenary amount detector, 3, 4...Bridle roll, 11, 12...Memory circuit, 13...Comparator, 14, 16...Divider, 1
5... Reference catenary setter, 17... Multiplier, 18
...Flip-flop, 19...Gate circuit, 20...
Adder, 21... Rotation speed controller for catenary control,
22... Catenary amount detector, 23... Motor, 24
...Sign inversion circuit.

Claims (1)

【特許請求の範囲】[Claims] 1 ストリツプが加熱炉内を複数のカテナリーを
形成しながら通過し、かつ該ストリツプの先行ス
トリツプと後行ストリツプとで断面積が異なる場
合において、先行ストリツプと後行ストリツプの
断面積比に基いて各カテナリーの量を制御するこ
とを特徴とするストリツプカテナリー制御方法。
1. When a strip passes through a heating furnace forming a plurality of catenaries, and the leading strip and the trailing strip have different cross-sectional areas, each catenary is A strip catenary control method characterized by controlling the amount of catenary.
JP16194581A 1981-10-13 1981-10-13 Controlling method of strip catenary Granted JPS5864318A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16194581A JPS5864318A (en) 1981-10-13 1981-10-13 Controlling method of strip catenary

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16194581A JPS5864318A (en) 1981-10-13 1981-10-13 Controlling method of strip catenary

Publications (2)

Publication Number Publication Date
JPS5864318A JPS5864318A (en) 1983-04-16
JPS6216257B2 true JPS6216257B2 (en) 1987-04-11

Family

ID=15745024

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16194581A Granted JPS5864318A (en) 1981-10-13 1981-10-13 Controlling method of strip catenary

Country Status (1)

Country Link
JP (1) JPS5864318A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0460044U (en) * 1990-09-21 1992-05-22

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0460044U (en) * 1990-09-21 1992-05-22

Also Published As

Publication number Publication date
JPS5864318A (en) 1983-04-16

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