JPS5855214B2 - Combustion control method for heat treatment furnace - Google Patents
Combustion control method for heat treatment furnaceInfo
- Publication number
- JPS5855214B2 JPS5855214B2 JP1004380A JP1004380A JPS5855214B2 JP S5855214 B2 JPS5855214 B2 JP S5855214B2 JP 1004380 A JP1004380 A JP 1004380A JP 1004380 A JP1004380 A JP 1004380A JP S5855214 B2 JPS5855214 B2 JP S5855214B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- time
- zone
- temperature
- steel pipe
- 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
- 238000010438 heat treatment Methods 0.000 title claims description 17
- 238000002485 combustion reaction Methods 0.000 title claims description 12
- 238000000034 method Methods 0.000 title claims description 7
- 229910000831 Steel Inorganic materials 0.000 claims description 24
- 239000010959 steel Substances 0.000 claims description 24
- 238000010791 quenching Methods 0.000 claims description 20
- 230000000171 quenching effect Effects 0.000 claims description 20
- 238000005496 tempering Methods 0.000 claims description 12
- 230000003247 decreasing effect Effects 0.000 claims 1
- 238000001816 cooling Methods 0.000 description 9
- 239000000463 material Substances 0.000 description 6
- 238000002791 soaking Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 2
- 238000007664 blowing Methods 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000005096 rolling process 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
- 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 Temperature (AREA)
- Control Of Heat Treatment Processes (AREA)
- Heat Treatment Of Articles (AREA)
Description
【発明の詳細な説明】
鋼管の熱処理ラインの制御に係り、特にロフト替りにお
けるロフト装入タイミング、炉温設定変更開始のタイミ
ング制御に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to control of a heat treatment line for steel pipes, and particularly to control of loft charging timing in loft change and timing control of starting change of furnace temperature setting.
鋼管は圧延機にて製造したままの状態では特性値のばら
つきがあり、熱処理により均一な金属組織、物理特性を
もたせる必要がある。Steel pipes have variations in their characteristic values as they are manufactured in a rolling mill, so it is necessary to give them a uniform metallographic structure and physical properties through heat treatment.
又油井管に使用される鋼管等の高級用途向は鋼管は規格
または需要家の指定により定められた熱処理を行う必要
がある。In addition, for high-grade steel pipes such as those used in oil country tubular goods, the steel pipes need to be heat treated as specified by standards or specified by the customer.
本発明は連続鋼材焼入炉、水冷装置、連続鋼材焼入炉、
空冷装置より構成され各設備をローラーテーブル等によ
り結びつけた鋼管熱処理ラインにおいて、ロフト変更時
における炉の燃焼及び鋼管の炉への装入タイミングを制
御する事により作業効率向上及び省エネルギーを実現す
る事を目的とする。The present invention provides a continuous steel quenching furnace, a water cooling device, a continuous steel quenching furnace,
In a steel pipe heat treatment line consisting of an air-cooling device and connecting each piece of equipment with a roller table, etc., we aim to improve work efficiency and save energy by controlling the combustion in the furnace and the timing of charging steel pipes into the furnace when the loft is changed. purpose.
上記の鋼管熱処理ラインの鋼管搬送間隔時間(以下サイ
クル・タイムという)は焼戻炉の均熱時間(熱処理の仕
様より指定される)により決定される。The steel pipe conveyance interval time (hereinafter referred to as cycle time) in the above-mentioned steel pipe heat treatment line is determined by the soaking time of the tempering furnace (designated from the heat treatment specifications).
又焼入炉及び焼戻し4各々個有の炉温変更に必要な時間
をもっている。In addition, each of the quenching furnace and tempering 4 has its own time required for changing the furnace temperature.
ロフト変更時はサイクル・タイム及び各炉の設定温度が
変更となる。When changing the loft, the cycle time and set temperature of each furnace will change.
本発明は各炉すなわち焼入れ炉、焼戻し炉の各帯(加熱
帯、均熱帯)毎に前ロフトの最終打通過後適切なタイミ
ングにて炉温変更を開始し、炉温設定完了のタイミング
で各炉の各帯に次ロフトの先頭材が進入する様に制御す
るものである。The present invention starts changing the furnace temperature for each zone (heating zone, soaking zone) of each furnace, that is, the quenching furnace and the tempering furnace, at an appropriate timing after passing the final blowing of the front loft, and changes the furnace temperature at the timing when the furnace temperature setting is completed. This is to control so that the leading material of the next loft enters each zone of the furnace.
本発明は前ロフトのサイクルタイム及び各炉各帯の炉温
設定変更時間より各炉各帯の変更完了時間をもとめ、次
ロフトのサイクル・タイムより隘路となる燃焼炉帯をも
とめ、隘路となる燃焼炉帯から次ロット先頭材の焼入れ
炉装入時刻をもとめ、隘路とならない燃焼炉帯の炉温変
更が炉温下降なら前ロフト最終打通過後即時に炉温変更
し、炉温変更が炉温上昇なら次ロフト先頭材が各燃焼炉
帯に到着する時刻より炉温変更開始時刻を決定する燃焼
制御方式である。The present invention determines the completion time for changing each furnace zone from the cycle time of the previous loft and the furnace temperature setting change time of each furnace zone, and determines the combustion furnace zone that will be the bottleneck from the cycle time of the next loft. Determine the time to charge the first material of the next lot into the quenching furnace from the combustion furnace zone, and if changing the furnace temperature in the combustion furnace zone that does not become a bottleneck causes a decrease in the furnace temperature, change the furnace temperature immediately after passing the final blow in the previous loft, and In the case of temperature rise, this combustion control method determines the furnace temperature change start time based on the time when the next loft leading material arrives at each combustion furnace zone.
ここで隘路となる帯とは、次ロフトの設定温度変更時間
が他の帯よりも長くかる帯をいう。Here, the zone that is a bottleneck refers to a zone where the time required to change the set temperature of the next loft is longer than other zones.
このためにライン全体の操業がその帯の設定温度変更を
待つことになる。For this reason, the operation of the entire line must wait for the temperature set point of that zone to be changed.
炉温の変化幅や炉の設備状況により、加熱帯が隘路帯と
なる場合もあるし、均熱帯が隘路となる場合もある。Depending on the range of changes in furnace temperature and the condition of the furnace equipment, the heating zone may become a bottleneck, or the soaking zone may become a bottleneck.
ここで、炉温か下降のときは即時に変更して燃料の節約
をはかる。Here, when the furnace temperature drops, change immediately to save fuel.
一方昇温の場合は昇温操作を開始してから実際に炉温か
上昇するまでには時間遅れ(炉の時定数による)がある
ので、先行して昇温をおこなうものである。On the other hand, in the case of temperature raising, there is a time delay (depending on the time constant of the furnace) from the start of the temperature raising operation until the furnace temperature actually rises, so the temperature is raised in advance.
第1図は熱処理ラインの概略図である。FIG. 1 is a schematic diagram of a heat treatment line.
鋼管は焼入れ炉1にて約800〜1100℃程度に加熱
され、水冷装置2にて急冷される。The steel pipe is heated to about 800 to 1100°C in a quenching furnace 1 and rapidly cooled in a water cooling device 2.
急冷された鋼管は次に焼戻し炉3にて450〜750℃
程度に加熱後数十分間均熱保持されたのち空冷装置4に
て空冷される。The rapidly cooled steel pipe is then heated to 450 to 750°C in a tempering furnace 3.
After being heated to a certain degree, the temperature is kept soaked for several tens of minutes, and then it is air cooled in an air cooling device 4.
焼入れ炉及び焼戻し炉は通常加熱帯A及び均熱帯Bに分
かれており、個々に炉温設定可能となっている。The quenching furnace and the tempering furnace are usually divided into a heating zone A and a soaking zone B, and the furnace temperature can be set individually.
第2図により詳細に説明する。A1.A2は焼入炉焼戻
炉の加熱帯、B、 、 B2は焼入炉焼戻炉の均熱帯で
ある。This will be explained in detail with reference to FIG. A1. A2 is the heating zone of the quenching furnace and tempering furnace, and B, B2 is the soaking zone of the quenching and tempering furnace.
またCは水冷領域である前ロフトのサイクル・タイムを
T1とすると、焼入炉及び焼戻し炉の各燃焼帯を通過す
る時刻はサイクルタイムより決定される。Further, if C is the cycle time of the front loft, which is a water-cooled region, as T1, the time at which the fuel passes through each combustion zone of the quenching furnace and the tempering furnace is determined from the cycle time.
各帯通過時刻をt。0〜103とする。Each band passing time is t. 0 to 103.
次に次ロフトのための炉温設定変更に必要な時間を変更
量より算出し、時刻t。Next, the time required to change the furnace temperature setting for the next loft is calculated from the amount of change, and the time is set at time t.
0〜toaに変更所要時間を加算しt 10−113を
求める。Add the required change time to 0 to toa to obtain t10-113.
tOH:@ロフト通過時刻 lθi:各帯の炉温変更量 gi:各帯の昇温/降温速度 jti :時刻t。tOH: @ Loft passing time lθi: Furnace temperature change amount for each zone gi: Temperature increase/cooling rate of each zone jti: Time t.
iより炉温変更して炉温設定の完了時刻
次に各々の時刻t11に各帯へ進入するための焼入炉装
入時刻T1を求める。The furnace temperature is changed from i and the furnace temperature setting completion time is determined.Then, the quenching furnace charging time T1 for entering each zone at each time t11 is determined.
g。g.
T1−tll−一 T2・・・・・・・・・・・・・・
・・・・・・・(2)41:各帯までの焼入炉装入から
の距離
e:鋼材間隔(設備的に一定)
τ2:次ロットのサイクル・タイム
(2)式よりT。T1-tll-1 T2・・・・・・・・・・・・・・・
・・・・・・・・・(2) 41: Distance from charging to the quenching furnace to each band e: Steel spacing (constant due to equipment) τ2: Cycle time of next lot T from equation (2).
−T3を求める最大の値をTMAXとする。Let TMAX be the maximum value for determining -T3.
TMAX−MAX(To、T1 、T2 、T3 )・
・・・・・・・・・・・・・・(3)
TMAXを次ロット1本目の焼入炉装入時刻とする。TMAX-MAX(To, T1, T2, T3)・
・・・・・・・・・・・・・・・(3) Let TMAX be the charging time of the first quenching furnace of the next lot.
次にTMAXにて焼入炉装入された鋼管が各燃焼帯に進
入する時刻t2iをもとめる。Next, the time t2i at which the steel pipe charged into the quenching furnace enters each combustion zone at TMAX is determined.
e。e.
t 21 = TMAX ”−τ ・・・・・・・・・
・・・・・・・・・(4)2
上記(4)式で求めた時刻より炉温変更開始時刻t31
を求める。t21=TMAX”−τ・・・・・・・・・
・・・・・・・・・(4)2 Furnace temperature change start time t31 from the time calculated by the above equation (4)
seek.
降温の場合はt。iにてただちに変更開始する。t in case of temperature drop. Press i to start changing immediately.
以上の計算方式の流れ図を第3図に示す処理ステップA
−Fから成る。The flowchart of the above calculation method is shown in FIG. 3. Processing step A
- Consists of F.
以上の方式により、焼入炉及び焼戻炉より構成される鋼
管の熱処理ラインのロフト替り時の最適な次ロフト装入
時刻及び炉温変更開始時刻を簡易に決定できた。Using the above method, it was possible to easily determine the optimal next loft charging time and furnace temperature change start time when changing lofts in a steel pipe heat treatment line consisting of a quenching furnace and a tempering furnace.
本発明によれば焼入炉、水冷装置、焼戻炉、空冷装置よ
り構成される鋼管の熱処理ラインにて、ロフト替り時の
空炉時間を最小にし、かつ炉の昇温か必要な場合は昇温
開始を可能なかぎり遅らせる事が可能である。According to the present invention, in a heat treatment line for steel pipes consisting of a quenching furnace, a water cooling device, a tempering furnace, and an air cooling device, the empty furnace time when changing lofts can be minimized, and the heating temperature of the furnace can be increased if necessary. It is possible to delay the onset of heat as much as possible.
本方式を計算機を用いて実施すれば、省エネルギー、省
力化、生産効率の向上をはかることができる。If this method is implemented using a computer, it is possible to save energy, save labor, and improve production efficiency.
第1図は鋼管の熱処理ラインの概要を示す構成図を第2
図はロフト替り時の前ロフト最終材及び次ロフト先頭材
の各燃焼帯進入通過タイミングの説明図を第3図は本発
明による次ロット先頭材の焼入炉装入タイミング及び各
燃焼帯の炉温設定変更タイミング決定方法の流れ図を示
す。
1・・・・・・焼入れ炉、2・・・・・・水冷装置、3
・・・・・・焼戻し炉、4・・・・・・空冷装置、5・
・・・・・鋼管。Figure 1 is a block diagram showing an overview of a steel pipe heat treatment line.
The figure is an explanatory diagram of the timing of entering and passing through each combustion zone for the final material of the previous loft and the leading material of the next loft when changing lofts. Figure 3 is the timing of charging the leading material of the next lot into the quenching furnace according to the present invention and the furnace of each combustion zone. A flowchart of a method for determining temperature setting change timing is shown. 1...Quenching furnace, 2...Water cooling device, 3
..... Tempering furnace, 4.. Air cooling device, 5.
...Steel pipe.
Claims (1)
管の熱処理ラインで複数ロットの鋼管の熱処理をおこな
う制御方法において、前ロフトリサイクルタイムおよび
該焼入炉、焼戻炉の加熱帯、均熱帯の炉温設定変更所要
時間から該炉帯それぞれの炉温変更完了時刻(1,1)
を演算し、熱処理される鋼管が該炉温変更完了時刻に各
帯へ進入するための焼入炉装入時刻(T1)のうち最遅
時刻(TMAX)を演算し、該最遅時刻に焼入炉に装入
された鋼管が各炉各帯に進入する時刻(t21)を予測
演算し、各炉各帯の炉温変更開始時刻(t3t)を昇温
変更の場合は該鋼管が各炉各帯に進入する時刻に先行し
て昇温時刻を設定し、降温変更の場合は該鋼管が各炉各
帯に進入する時刻から降温を開始して各炉各帯の炉温を
変更することを特徴とする熱処理炉の燃焼制御方法。1. In a control method for heat treating multiple lots of steel pipes in a steel pipe heat treatment line consisting of at least a quenching furnace and a tempering furnace, The furnace temperature change completion time for each furnace zone from the time required to change the furnace temperature setting (1, 1)
, calculate the latest time (TMAX) of the quenching furnace charging time (T1) for the steel pipe to be heat treated to enter each zone at the time when the furnace temperature change is completed, and The time (t21) at which the steel pipe charged into the furnace enters each zone of each furnace is predicted and calculated, and the time (t3t) at which the furnace temperature change starts for each zone of each furnace is determined. Set the temperature increase time in advance of the time when the steel pipe enters each zone, and when changing the temperature, start decreasing the temperature from the time when the steel pipe enters each zone of each furnace to change the furnace temperature of each zone of each furnace. A combustion control method for a heat treatment furnace, characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1004380A JPS5855214B2 (en) | 1980-02-01 | 1980-02-01 | Combustion control method for heat treatment furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1004380A JPS5855214B2 (en) | 1980-02-01 | 1980-02-01 | Combustion control method for heat treatment furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56108834A JPS56108834A (en) | 1981-08-28 |
| JPS5855214B2 true JPS5855214B2 (en) | 1983-12-08 |
Family
ID=11739361
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1004380A Expired JPS5855214B2 (en) | 1980-02-01 | 1980-02-01 | Combustion control method for heat treatment furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5855214B2 (en) |
-
1980
- 1980-02-01 JP JP1004380A patent/JPS5855214B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56108834A (en) | 1981-08-28 |
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