JPS5814856B2 - Heating furnace control method - Google Patents
Heating furnace control methodInfo
- Publication number
- JPS5814856B2 JPS5814856B2 JP3641579A JP3641579A JPS5814856B2 JP S5814856 B2 JPS5814856 B2 JP S5814856B2 JP 3641579 A JP3641579 A JP 3641579A JP 3641579 A JP3641579 A JP 3641579A JP S5814856 B2 JPS5814856 B2 JP S5814856B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- zone
- heating furnace
- temperature
- determined
- 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
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
- C21D11/00—Process control or regulation for heat treatments
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)
Description
【発明の詳細な説明】
本発明は、工業用多帯式加熱炉の制御方法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for controlling an industrial multi-zone heating furnace.
一般ζこ工業用多帯式加熱炉を有する熱間圧延ラインO
こおいては鋼片の加熱炉抽出速度は一定ではない。General ζHot rolling line with industrial multi-zone heating furnace O
Here, the furnace extraction rate of the steel billet is not constant.
すなわち統計学上における鋼片抽出速度は一定であるが
、ミクロ的に観察した場合Gこは加熱炉操業中の個々の
鋼片についての抽出速度は全て異なっており、また加熱
炉操業中でのライントラブルあるいはロール替等の段取
替さらQこはその他停機等があってこれ等もまた鋼片の
抽出速度を乱している要因の一つである。In other words, statistically speaking, the extraction rate of steel slabs is constant, but when observed microscopically, the extraction rates of individual steel slabs during heating furnace operation are all different, and the extraction rate during heating furnace operation is different. There are line troubles, setup changes such as roll changes, and other machine stoppages, which are also factors that disturb the extraction speed of steel pieces.
さらに手動操炉の場合ζこは操炉状況の変化Cこ対する
炉渦の適切な変更が行なイつれない為ζこ例えばライン
停機の場合ζこは鋼片(こ必要以上の熱量を投入するこ
とによって核鋼片を必要以上昇湛させることになる。Furthermore, in the case of manual furnace operation, it is difficult to make appropriate changes to the furnace vortex in response to changes in furnace operating conditions. As a result, the core steel pieces are made to rise more than necessary.
また逆に抽出速度が標準抽出速度よりも速い場合には鋼
片に焼け不厄を来たし、例えば製管ラインにおける丸鋼
片の場合Qこは均熱度が悪化して穿孔時にねじれあるい
は偏肉現象を起こし成品品質上悪影響をおよほすという
問題点があった。On the other hand, if the extraction speed is faster than the standard extraction speed, the steel billet will be burned, and for example, in the case of a round steel billet in a pipe manufacturing line, the uniformity of heat will deteriorate, resulting in twisting or uneven thickness during drilling. There was a problem in that this caused a negative impact on the quality of the product.
本発明は上述の如く鋼片の抽出速度の乱れζこ起因する
諸悪現象を回避するととも(こ燃料の原単位の低減を計
るための加熱炉の炉温制御方法を提供せんとするもので
あり、以下本発明方法を詳細に説明する。The present invention aims to provide a method for controlling the temperature of a heating furnace in order to avoid the various adverse phenomena caused by disturbances in the extraction rate of steel billets as described above (and to reduce the fuel consumption rate). Hereinafter, the method of the present invention will be explained in detail.
まず、加熱炉仕様を考慮して目標材料の昇温ヒトパター
ンを予め第2図に示すフローチャートすなわち目標材料
に抽出速度Vが与えられた時(こ、その材料篇度を所定
の目標昇温パターンに沿わしめる炉渦TVを決定するた
めのフローチャ−1−6こより決定する。First, in consideration of the heating furnace specifications, the temperature increase pattern of the target material is determined in advance by the flowchart shown in FIG. Flowchart 1-6 for determining the furnace vortex TV to follow.
なおこの昇温ヒートパターンは一般Oこは鋼片の鋼種、
寸法毎に経験的に決定されるものである。Note that this temperature increase heat pattern applies to the steel type of the general steel billet.
It is determined empirically for each dimension.
すなわち本発明制御方法の基本原則は、上記の予じめ決
定した目標材料の昇渦ヒートパターンを基準6こして抽
出速度ζこ変動が生じた場合においても該昇温ヒートパ
ターンに沿うよう炉扁を設定することである。In other words, the basic principle of the control method of the present invention is to use the predetermined vortex heating heat pattern of the target material as a reference 6 and to adjust the furnace plate to follow the heating heat pattern even if the extraction rate ζ varies. is to set.
つまり、炉湿をこの目標材料の昇渦ヒートパターンに沿
イっし,めることQこよって材科を常Oこ適正温度とな
さしめ、また抽出速度が遅くなった場合ζこは炉漉を■
げることで燃料ゑ単位の低減を図るものである。In other words, the furnace humidity should be adjusted according to the vortex heat pattern of the target material. ■
The aim is to reduce the unit fuel consumption by increasing the amount of fuel.
ここ(こおいて、目標材料の昇滉巳−トパターンとは加
熱炉の各帯出側で鋼片が目標渦度θi(iは各帯No)
を得る材料混度の昇湛カーブであり、第1図にその1例
として3帯式加熱炉における丸鋼片の場合の昇湛ヒート
パターンを示す。(Here, the target material's heating pattern is the target vorticity θi (i is the number of each band) of the steel slab on each band exit side of the heating furnace.
Figure 1 shows, as an example, the heating pattern of a round steel piece in a three-zone heating furnace.
なお第1図では簡単のために各帯間の昇温状態は直線で
示す。In addition, in FIG. 1, the temperature increase state between each zone is shown by a straight line for the sake of simplicity.
次に、材料温度を上述した目標材料の昇温ヒートパター
ンζこ沿わしめるべく、炉温Tviを各帯域毎Gこ決定
する。Next, the furnace temperature Tvi is determined for each zone so that the material temperature follows the temperature increase heat pattern ζ of the target material described above.
すなわち第2図フローチャートに示す如く、材料に任意
の抽出速度■を与えると第1帯域の在帯時間△L1は、
△ti二Li/V ・・・・・・・・・■たた
し、L1二各帯域長さ
(こよって算出され、また第1帯域(こ搬入時の材料温
度が第( i−1 ’)帯域で目標材料温度に到達して
いると仮定すれば該材料湛度はθl−1であり、さらに
第1帯域での炉湛Tviが前記材料ζこ与えられれば、
第■式に示す温度計算法により第■式の△L時間後の材
料温度θ′lは算出される。That is, as shown in the flowchart in Fig. 2, when an arbitrary extraction speed ■ is given to the material, the residence time ΔL1 in the first zone is Δti2Li/V ・・・・・・・・・■Tax, L12 The length of each zone (thus calculated, and assuming that the material temperature at the time of loading has reached the target material temperature in the (i-1')th zone, the material fullness is θl−1, and if the temperature Tvi in the first zone is given as the material ζ,
The material temperature θ'l after ΔL time in equation (2) is calculated by the temperature calculation method shown in equation (2).
たたし、φCG二加熱炉型式等によって定まる総括熱伝
達係数
ρ二材料密度
C二材料比熱
h:材料寸法
△[:時間間隔
ここで、第■式Qこより算出された材料渦度θ’iは第
1帯での目標材料温度θ■と等しい場合は、これが求め
るところのある抽出速度■に対する炉混Tviである。(2) Overall heat transfer coefficient ρ determined by the heating furnace model, etc. (2) Material density C (2) Material specific heat h: Material dimension △ [: Time interval Here, material vorticity θ'i calculated from equation (2) Q When is equal to the target material temperature θ■ in the first zone, this is the furnace mixture Tvi for the desired extraction rate ■.
また算出材料混度θ′1が目標材料渦度θ1と等しくな
い場合は、炉温Tviを修正後、前記と同様の材料温度
計算を行ない△L時間後の算出材科温度θ′1が目標{
オ別渦度θ1と等しくなる迄反復する。If the calculated material mixture θ'1 is not equal to the target material vorticity θ1, the same material temperature calculation as above is performed after correcting the furnace temperature Tvi, and the calculated material temperature θ'1 after △L time is the target. {
Repeat until the vorticity becomes equal to O's vorticity θ1.
すなイつち上述した作業を行なうことによって、ある抽
出速度■ζこ対する炉渦TVが一意的に決定する。In other words, by performing the above-mentioned operations, the furnace vortex TV corresponding to a certain extraction rate ■ζ is uniquely determined.
以上述べた方法Qこより抽出速度■を0から無限大に変
化させて各帯域毎に炉温Tviを算出することQこより
、ある鋼種、寸法(こ対する第i帯域の抽出速度■と炉
1/M T vとの関係図(以’FTv −’V線図と
称す)が求められ、このTv−V線図を全帯域さらζこ
は全鋼種、寸法について作成する。From the above method Q, the extraction rate ■ is varied from 0 to infinity and the furnace temperature Tvi is calculated for each zone. A relationship diagram with M T v (hereinafter referred to as 'FTv-'V diagram) is obtained, and this Tv-V diagram is created for all bands and also for all steel types and dimensions.
第1図と同様の実施例においてのTv一■線図を第3図
に示す。FIG. 3 shows a Tv line diagram in an embodiment similar to that in FIG. 1.
前記した寸法ζこより全鋼種、寸法ζこついてのT v
− V線図を求めた後第4図に示すフローチャートに
基づいて炉渦Tviを設定出力するっ例えば回転炉床炉
の場合においては、時々刻々の回転角Cとその時刻Lを
検出することで材料の抽出速度Vζこ等しい炉床移動速
度を
ただし、K:定数
Qこより算出する。From the above-mentioned dimension ζ, all steel types, T v with dimension ζ
- After obtaining the V diagram, set and output the furnace vortex Tvi based on the flowchart shown in Figure 4. For example, in the case of a rotary hearth furnace, by detecting the momentary rotation angle C and its time L. The hearth moving speed is equal to the material extraction speed Vζ, where K: constant Q.
次に第1帯域内に存在する材料の鋼種、寸法が同−鋼種
、寸法かどうかを判断する。Next, it is determined whether the steel type and size of the materials existing in the first zone are the same steel type and size.
そして第1帯域内に同一の鋼踵、寸法のみが存在する場
合ζこは、該帯域内の鋼種、寸法に対応するTv−V線
図を探索決定する。If only the same steel heel and dimensions exist within the first zone, the Tv-V diagram corresponding to the steel type and dimensions within the zone is searched and determined.
しかる後該当するTv−V線図からこの時の抽出速度V
6こ対応する第1帯の炉湛Tviを判読して、該炉渦T
VIを設定出力Tsiとして出力する。After that, the extraction speed V at this time is determined from the corresponding Tv-V diagram.
6, the corresponding furnace vortex Tvi of the first zone is read, and the corresponding furnace vortex T
VI is output as the setting output Tsi.
また、第1帯域内ζこ異なる鋼種、寸法の材料が混在す
る場合Qこは、該帯域内Qこ存在する材料の全鋼種、寸
法の中から後述する優先度の高い鋼種、寸法に適合する
Tv−V線図を探索決定し、このTv−V線図から第1
帯の炉渦TvIを判読してこれを設定出力Tsiとして
出力する。In addition, if there are materials with different steel types and dimensions in the first zone, the material will match the steel types and dimensions with higher priority, which will be described later, from among all the steel types and dimensions of the materials present in the zone. Search and determine the Tv-V diagram, and from this Tv-V diagram,
The furnace vortex TvI of the belt is read and outputted as the set output Tsi.
上述操作を全帯域について行なうことによって加熱炉内
の炉渦T■が最適Cこ制御されることになる。By performing the above-mentioned operation for the entire zone, the furnace vortex T in the heating furnace can be controlled optimally.
なお、鋼種、寸法の優先順位とは各製造工程において一
般に経験的}こ決定されるものであり、その決定条件と
しては、例えば最も加熱条件(・こ対して敏感に影響を
受けるステンレスのようなものの加熱不足やオーバヒー
トを避けるべく決定するものである。The priority order of steel types and dimensions is generally determined empirically in each manufacturing process, and the determining conditions include, for example, steel materials such as stainless steel, which are most sensitive to heating conditions. This decision is made to avoid underheating or overheating things.
つまり、本発明制御方法は加熱炉の加熱能力が圧延速度
■を上まわる操業状態の場合に適用されるものである。That is, the control method of the present invention is applied when the heating capacity of the heating furnace exceeds the rolling speed (2).
なぜならば各加熱炉Qこは個有の加熱能力があり、該加
熱能力に従って各加熱炉の最犬炉温設定値Tsmaxが
制限され、該設定値Tsmax以上の値ζこ設定するこ
とができないからである。This is because each heating furnace has its own heating capacity, and the maximum furnace temperature setting value Tsmax of each heating furnace is limited according to the heating capacity, and it is not possible to set a value higher than the setting value Tsmax. It is.
すなわち、ある加熱炉の最大抽出速度Vmaxを越えた
場合でもTv一■線図より炉温T vは求められるが、
加熱炉の加熱能力より該加熱炉の最犬炉温設定値Tsm
axが制限されるために、Tsi二Tviとして設定出
力することができないからである。In other words, even if the maximum extraction speed Vmax of a certain heating furnace is exceeded, the furnace temperature Tv can be determined from the Tv line diagram.
Based on the heating capacity of the heating furnace, the maximum furnace temperature setting value Tsm of the heating furnace is determined.
This is because ax is limited, so it is not possible to set and output Tsi and Tvi.
以上述べたように本発明制御方法によれば加熱炉内の各
帯抽出速度の時々刻々の変化に対応して該抽出速度に対
する炉温設定を最適に制御せしめるようなさしめたため
に、抽出速度の変動に対しても常ζこ材料湛度を最適に
維持出来、製品の不良化を防止しうるのみならず燃料原
単位の低減が計れる効果を有する発明である。As described above, according to the control method of the present invention, the furnace temperature setting for the extraction rate is optimally controlled in response to the momentary changes in the extraction rate of each zone in the heating furnace. This invention has the effect of not only being able to maintain optimal material saturation even in the face of fluctuations, preventing product defects, but also reducing fuel consumption.
ちなみQこ、加熱能力1 00TON/HOURのソー
ムレス製管用3帯弐回転炉でφ180X4000l,φ
170X350M,φ160X3000lの炭素鋼材を
混在して加熱せしめた場合の抽出温度と抽出{オの偏熱
のヒスI・ダラムを第5図に示す。Chinami Q: φ180×4000l, φ with a 3-zone 2 rotary furnace for somless pipe making with a heating capacity of 100 TON/HOUR.
Figure 5 shows the extraction temperature and the hiss I/Durham of the uneven heat of the extraction when carbon steel materials of 170 x 350 M and φ 160 x 3000 l are mixed and heated.
第5図イは手動による加熱炉操業時のものであり、同図
口は本発明方法ζこおける加熱炉操業時のものを示して
いる。Figure 5A shows the situation when the heating furnace is operated manually, and the opening of the figure shows the situation when the heating furnace is operated according to the method ζ of the present invention.
同図より明らかな如く本発明方法を使用することζこよ
り、抽出湛度のバラツキが半減し、ひいては製品の品質
向上ζこも寄与しているのがイつかる。As is clear from the figure, by using the method of the present invention, the variation in the degree of extraction is reduced by half, which in turn contributes to improving the quality of the product.
また本実施例Qこおける燃料原単位は手動操炉時が4
6. 9 X 1 0’ Kcal/ tonであるの
Cこ対し、本発明制御実施時は44.6X1 0’ K
cal/ tonであった。In addition, the fuel consumption rate in this example Q is 4 when the reactor is operated manually.
6. 9 X 1 0' Kcal/ton, whereas when the control of the present invention is implemented, it is 44.6 X 1 0' Kcal/ton.
It was cal/ton.
第1図は3帯式加熱炉における1実施例の昇温ヒートパ
ターンを示し、第2図は本発明6こおける炉温設定のフ
ローチャートであり、第3図は第1図と同様の実施例(
こおける抽出速度と炉温との関係図、第4図は回転炉床
炉Qこおける本発明方法実施のためのフローチャート、
第5図は3帯弐回転炉床炉Qこ3種の材料を混在加熱し
た場合の抽出湛度と偏熱のヒストグラムを示したもので
あり同図イは手動操業の場合、口は本発明制御の場合で
ある。FIG. 1 shows a heating pattern for one embodiment of a three-zone heating furnace, FIG. 2 is a flowchart for setting the furnace temperature in the sixth embodiment of the present invention, and FIG. 3 is a similar embodiment to FIG. 1. (
FIG. 4 is a flowchart for implementing the method of the present invention in a rotary hearth furnace Q;
Figure 5 shows a histogram of extraction depth and uneven heat when three types of materials are mixed and heated in a three-zone two-rotary hearth furnace. This is a case of control.
Claims (1)
ーンを予め決定し、一般的な温度計算方式Cこより被加
熱材料湛度を常時算出してその材料湿度と上記目標昇温
パターンとが等しくなるように各帯域毎に炉渦を決定出
力する方法において、材料抽出速度V4こ応じて、材料
温度を上記目標昇温パターンに沿わしめる炉湛T vの
関係Tv−’V線図を種々の鋼種、寸法(こついて予め
求めて置き、実績あるいは予測抽出速度■に対し、加熱
炉帯域中の鋼種、寸法に応じて決まった優先度の高い材
料のTv−V線図を用いて炉温を決定算出し、炉温の制
御を行なうことを特徴とする加熱炉制御方法。1 In an industrial multi-zone heating furnace, the temperature increase pattern of the target material is determined in advance, and the content of the material to be heated is constantly calculated using the general temperature calculation method C, and the humidity of the material and the target temperature increase pattern are calculated. In the method of determining and outputting the furnace vortices for each zone so that they are equal, the relationship Tv-'V diagram of the furnace vortex Tv that makes the material temperature follow the above-mentioned target temperature increase pattern is varied depending on the material extraction rate V4. The steel type and dimensions (determined in advance and the actual or predicted extraction rate) are determined using the Tv-V diagram of the high-priority material determined according to the steel type and dimensions in the heating furnace zone. A heating furnace control method characterized by determining and calculating and controlling the furnace temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3641579A JPS5814856B2 (en) | 1979-03-27 | 1979-03-27 | Heating furnace control method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3641579A JPS5814856B2 (en) | 1979-03-27 | 1979-03-27 | Heating furnace control method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS55128546A JPS55128546A (en) | 1980-10-04 |
| JPS5814856B2 true JPS5814856B2 (en) | 1983-03-22 |
Family
ID=12469191
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3641579A Expired JPS5814856B2 (en) | 1979-03-27 | 1979-03-27 | Heating furnace control method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5814856B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62186980A (en) * | 1986-02-12 | 1987-08-15 | 株式会社タツノ・メカトロニクス | Matsuto cleaner |
| JPS62269792A (en) * | 1986-05-16 | 1987-11-24 | 株式会社タツノ・メカトロニクス | Matsuto cleaner |
-
1979
- 1979-03-27 JP JP3641579A patent/JPS5814856B2/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62186980A (en) * | 1986-02-12 | 1987-08-15 | 株式会社タツノ・メカトロニクス | Matsuto cleaner |
| JPS62269792A (en) * | 1986-05-16 | 1987-11-24 | 株式会社タツノ・メカトロニクス | Matsuto cleaner |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS55128546A (en) | 1980-10-04 |
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