JPS62166282A - Continuous heat treatment furnace - Google Patents

Continuous heat treatment furnace

Info

Publication number
JPS62166282A
JPS62166282A JP873386A JP873386A JPS62166282A JP S62166282 A JPS62166282 A JP S62166282A JP 873386 A JP873386 A JP 873386A JP 873386 A JP873386 A JP 873386A JP S62166282 A JPS62166282 A JP S62166282A
Authority
JP
Japan
Prior art keywords
zone
temperature
slow cooling
heating
cooling 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.)
Granted
Application number
JP873386A
Other languages
Japanese (ja)
Other versions
JPH0633946B2 (en
Inventor
崇 石本
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.)
Daido Steel Co Ltd
Original Assignee
Daido Steel Co Ltd
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 Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP873386A priority Critical patent/JPH0633946B2/en
Publication of JPS62166282A publication Critical patent/JPS62166282A/en
Publication of JPH0633946B2 publication Critical patent/JPH0633946B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は連続熱処理炉に関するもので、さらに詳しくは
その徐冷帯における温度コン1〜ロール機能を改良せん
とするものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a continuous heat treatment furnace, and more specifically, to improving the temperature controller 1 to roll functions in the slow cooling zone.

[従来の技術とその問題点] 処理物を加熱・均熱マ(Fから徐冷帯へと一連に搬送し
て所要の温度カーブに従い該処理物を加熱。
[Prior art and its problems] The processed material is conveyed in series from a heating and soaking machine (F) to an annealing zone, and the processed material is heated according to a required temperature curve.

冷却する従来の連続熱処理炉を第5図に示す。同図にお
いて、1は処理物aを矢印の方向に搬送するコンベヤ、
2は加熱・均熱帯、3は徐冷帯である。4,4・・・・
はラジアントチューブバーナ等の熱源を示す。加熱・均
熱帯2および徐冷帯3は隔壁5,5・・・・によって多
数の温度ゾーンに区画されており、その各ゾーンに熱源
4,4・・・・を備えている。そして各ゾーンの炉内ガ
スの温度を熱電対6,6・・・・により検出し各温度ゾ
ーンが所要の設定温度に維持されるように温度調節計7
,7・・・・により熱源4,4・・・・の発熱量がコン
トロールされる。第5図にはこの熱処理炉の各帯の設定
温度と処理物の温度カーブを併記したが、徐冷4”+F
はこのように多数の温度ゾーンに分割することによって
処理物が徐々に温度低下するようにしている。
A conventional continuous heat treatment furnace for cooling is shown in FIG. In the figure, 1 is a conveyor that conveys the processed material a in the direction of the arrow;
2 is a heating/soaking zone, and 3 is a gradual cooling zone. 4,4...
indicates a heat source such as a radiant tube burner. The heating/soaking zone 2 and the slow cooling zone 3 are divided into a number of temperature zones by partition walls 5, 5, . . . , and each zone is equipped with a heat source 4, 4, . Then, the temperature of the furnace gas in each zone is detected by thermocouples 6, 6, etc., and a temperature controller 7 is used to maintain each temperature zone at the required set temperature.
, 7... controls the amount of heat generated by the heat sources 4, 4.... Figure 5 shows the set temperature of each zone of this heat treatment furnace and the temperature curve of the processed material.
By dividing the temperature into a large number of temperature zones in this way, the temperature of the processed material is gradually lowered.

即ちこの分割数が少ないと各ゾーンの温度差が大きくな
り処理物がゾーンを移る毎に急冷されて品質に異常を来
たすことがある。特に処理物がブララン管のようなガラ
ス製品の場合急冷によって割れを生じたりするおそれが
あった。このため温度ゾーンの細分割は欠かせず炉の築
造コストを高いものとしていた。また、徐冷帯3には炉
の操業開始時のように各温度ゾーンの温度が低いときに
処理物の急冷をさけるために熱源を設けているが、連続
操業によって処理物の放出熱が炉壁に蓄熱されると熱源
はカットされ、さらに、炉壁がらの放出熱より処理物の
放出熱のほうが大きくなると逆に冷却のためにラジアン
トチューブ中に冷気を通して抜熱するようにしている。
That is, if the number of divisions is small, the temperature difference between each zone will be large, and the processed material will be rapidly cooled each time it moves from one zone to another, resulting in abnormal quality. In particular, when the processed material is a glass product such as a Bralan tube, there is a risk of cracking due to rapid cooling. For this reason, it was essential to subdivide the temperature zones, making the construction cost of the furnace high. In addition, a heat source is installed in slow cooling zone 3 to avoid rapid cooling of the material to be treated when the temperature in each temperature zone is low, such as when the furnace starts operating, but due to continuous operation, the heat released from the material is When heat is stored in the walls, the heat source is cut off, and when the heat released from the processed material is greater than the heat released from the furnace walls, cold air is passed through the radiant tubes to remove the heat.

従って複雑な温度コントロール機能を持たねばならず炉
のコストを一層高いものとしていた。
Therefore, the furnace must have a complicated temperature control function, making the cost of the furnace even higher.

[問題点を解決するための手段] 本発明の連続熱処理炉は上記問題点を解消せんとするも
ので、加熱・均熱帯に続く徐冷帯の炉壁の断熱性が該加
熱・均熱帯から遠ざかるにつれて次第にノ」1さくなる
ようにしたことを特徴とするものである。また本発明は
上記連続熱処理炉において、徐冷帯の出口部付近から吸
引したガスを加熱・均熱帯に循環させる循環ファンを設
けて加熱・均熱帯の熱風を徐冷帯に流動させると共に、
徐冷帯の出口部付近における炉内ガスの温度を検出し、
前記循環ファンによるガスの循環量をコントロールする
ようにしたことを第2の特徴とするものである。
[Means for Solving the Problems] The continuous heat treatment furnace of the present invention is intended to solve the above problems, and the heat insulation of the furnace wall of the slow cooling zone following the heating/soaking zone improves from the heating/soaking zone. It is characterized in that it gradually becomes smaller as it gets farther away. Further, the present invention provides the continuous heat treatment furnace as described above, in which a circulation fan is provided to circulate the gas sucked from the vicinity of the outlet of the slow cooling zone into the heating/soaking zone, and the hot air in the heating/soaking zone is made to flow into the slow cooling zone.
Detects the temperature of the gas in the furnace near the outlet of the slow cooling zone,
A second feature is that the amount of gas circulated by the circulation fan is controlled.

[作用コ 徐冷帯の炉壁の断熱性を徐々に小さくしてゆくことで炉
単位長さ当りの放散熱を徐冷帯全長にわたり同一になる
ようにする。
[Operation: By gradually reducing the heat insulation of the furnace wall of the slow cooling zone, the heat dissipated per unit length of the furnace is made to be the same over the entire length of the slow cooling zone.

加熱・均熱帯の熱風を徐冷帯に流すので徐冷帯の温度勾
配は直線状になり処理品を文字どおり徐冷することがで
きると共に、その温度コントロールが容易となる。
Since the hot air from the heating/soaking zone is passed through the slow cooling zone, the temperature gradient in the slow cooling zone becomes linear, making it possible to literally slowly cool the processed product and making it easy to control the temperature.

[実施例コ 第1図に本発明に係る連続熱処理炉の縦断面図を示し、
第2図にはその徐冷帯の水平断面図を示す。同図におい
て、aは処理物、1はコンベヤ。
[Example 1] Fig. 1 shows a longitudinal cross-sectional view of a continuous heat treatment furnace according to the present invention,
FIG. 2 shows a horizontal sectional view of the slow cooling zone. In the figure, a represents the processed material, and 1 represents the conveyor.

2は加熱・均熱帯、3は徐冷帯、4,4・・・・は加熱
・均熱帯2に設けられたラジアントチューブバーナであ
る。徐冷帯3はその側壁が第2図に示されるように加熱
・均熱?IF2から遠ざかるにつれて次第に薄くなるよ
うに形成してその断熱性が徐々に小さくなるようにする
。そしてこれによって炉単位長さ当りの放散熱Q (K
cal/h−m)が徐冷帯全長にわたり同一になるよう
にする。また徐冷帯3の出口部付近に吸気口8を設は循
環ファン7により該吸気口8から徐冷帯3内のガスを吸
引すると共にその吸引したガスを加熱・均熱帯2に循環
させる。10は徐冷帯3の出口部付近に設けられた熱電
対、11は循環ファン7と吸気口8とを結ぶダスト中に
その吸込ガス流量をコントロールするように設けられた
電磁流量調節弁、12は熱電対10による温度検出信号
を受けて電磁流量調節弁11にフィードバック指令を出
すコントローラである。しかしてこの徐冷帯3し;は熱
源は設けられず、加熱・均熱帯2の熱風を徐冷帯3流動
させることにより所要の温度を保つ。即ち、循環ファン
7によるガスの循環で加熱・均熱帯2の熱風は徐冷帯3
に流動し該徐冷帯の温度を設定炉温に昇温する。徐冷帯
3では次第に炉壁が薄くなっているのでその熱風の温度
は加熱・均熱帯から遠ざかるにつれて徐々に低下する。
2 is a heating/soaking zone, 3 is a slow cooling zone, and 4, 4, . . . are radiant tube burners provided in the heating/soaking zone 2. Is the side wall of the slow cooling zone 3 heated and soaked as shown in Figure 2? It is formed so that it becomes gradually thinner as it moves away from IF2, so that its heat insulating properties gradually decrease. As a result, the heat dissipated per unit length of the furnace Q (K
cal/hm) is made to be the same over the entire length of the slow cooling zone. Further, an inlet 8 is provided near the outlet of the annealing zone 3, and a circulation fan 7 sucks the gas in the annealing zone 3 through the inlet 8 and circulates the sucked gas to the heating/soaking zone 2. 10 is a thermocouple provided near the outlet of the slow cooling zone 3; 11 is an electromagnetic flow rate control valve provided in the dust connecting the circulation fan 7 and the intake port 8 to control the flow rate of the suction gas; 12 is a controller that receives a temperature detection signal from the thermocouple 10 and issues a feedback command to the electromagnetic flow control valve 11. However, no heat source is provided in the slow cooling zone 3; the required temperature is maintained by flowing hot air from the heating/soaking zone 2 into the slow cooling zone 3. That is, the hot air in the heating/soaking zone 2 is transferred to the slow cooling zone 3 by the circulation of gas by the circulation fan 7.
The temperature of the slow cooling zone is raised to the set furnace temperature. In the slow cooling zone 3, the furnace wall gradually becomes thinner, so the temperature of the hot air gradually decreases as it moves away from the heating/soaking zone.

第1図にはその模様を炉内ガスの温度を破断線で表わし
、処理物aの温度を実線で表わした。このように加熱・
均熱帯から熱風を導入することによって徐冷帯3の温度
は直線状に変化する。そして循環ファン7による循環量
は流量調節弁11によりコントロールされるので熱電対
lOによって徐冷帯3出口付近の温度が所要の設定温度
になるようにコントローラ12に該流量調節弁11の開
度を制御させる。即ち、徐冷帯3出口付近の温度が所要
設定温度よりも低くなったときは流量調節弁11の開度
を上げてガスの環検量を増加させ加熱・均熱帯2から徐
冷帯3へ流動する熱風量が多くなるようにしてその出口
部付近の温度が高くなるように制御し、反対に徐冷;X
jF3出口部付近の温度が所要設定温度よりも高くなっ
たときは流量調節弁11の開度を下げて加熱・均熱帯2
から徐冷帯3へ流動する熱風量を抑えその出口部付近の
温度を下げることにより、常に出口部付近が所要設定温
度に維持されるようにフィードバック制御する。この結
果徐冷帯3は加熱・均熱帯2からりニヤに温度低下し、
処理物aをなだらかに温度低下させることができる。
In FIG. 1, the temperature of the gas in the furnace is represented by a broken line, and the temperature of the processed material a is represented by a solid line. In this way, heating
By introducing hot air from the soaking zone, the temperature of the slow cooling zone 3 changes linearly. Since the amount of circulation by the circulation fan 7 is controlled by the flow rate control valve 11, the opening degree of the flow rate control valve 11 is controlled by the controller 12 using the thermocouple lO so that the temperature near the outlet of the slow cooling zone 3 reaches the desired set temperature. Let it be controlled. That is, when the temperature near the outlet of the slow cooling zone 3 becomes lower than the required set temperature, the opening degree of the flow rate control valve 11 is increased to increase the ring metering amount of gas and flow from the heating/soaking zone 2 to the slow cooling zone 3. Control the flow of hot air to increase so that the temperature near the outlet of the hot air becomes high, and conversely slow cooling;
j When the temperature near the F3 outlet becomes higher than the required set temperature, the opening degree of the flow control valve 11 is lowered and the heating/soaking zone 2
By suppressing the amount of hot air flowing from the cooling zone 3 to the slow cooling zone 3 and lowering the temperature in the vicinity of the outlet, feedback control is performed so that the temperature in the vicinity of the outlet is always maintained at the required set temperature. As a result, the temperature of the slow cooling zone 3 decreases rapidly from that of the heating/soaking zone 2,
The temperature of the processed material a can be lowered gently.

第3図には第2図と同じく炉壁を次第に薄くした徐冷帯
(この場合炉内幅は変化なく炉外面を先細とした。)を
示す。また第4図には炉qをその内面から段階的に肉薄
とした徐冷帯を示すが、本発明はこのようにして断熱性
を加熱・均熱帯から遠ざかるに従い徐々に小さくすれば
よくその手段についてはこの実施例以外にも種々考えら
れる。
FIG. 3 shows an annealing zone in which the furnace wall is gradually thinned as in FIG. 2 (in this case, the inside width of the furnace remains unchanged and the outside surface of the furnace is tapered). In addition, FIG. 4 shows a slow cooling zone in which the wall of the furnace q is gradually thinned from the inner surface of the furnace q. In addition to this embodiment, various other methods can be considered.

[発明の効果] 以上実施例について説明したように本発明の連続熱処理
炉は、徐冷帯に多数の温度ゾーンを設けなくてもその設
定炉温を直線状に変化させら9、処理物の品質異常や割
れ等の支障を起こさない。また徐冷帯には熱源が不用と
なり温度制御系も簡単になるので炉の築造コストも安く
なるなど顕著な効果がある。
[Effects of the Invention] As described in the embodiments above, the continuous heat treatment furnace of the present invention can linearly change the set furnace temperature without providing a large number of temperature zones in the slow cooling zone9, and Does not cause problems such as quality abnormalities or cracks. In addition, the slow cooling zone does not require a heat source and the temperature control system is simple, so the construction cost of the furnace is reduced, which has significant effects.

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

第1図は本発明の一実施例を示した連続熱処理炉の縦断
面図とその温度線図、第2図はその徐冷帯の水平断面図
、第3図および第4図は徐冷帯3の他の実施例を示した
水平断面図である。第5図は従来の連続熱処理炉の縦断
面図とその温度線図である。 a・・・・処理物、2・・・・加熱・均熱帯、3・・・
・徐冷帯、7・・・・循環ファン、8・・・・吸気口、
IO・・・・熱電対、11・・・・流量調節弁。 喋2図
Fig. 1 is a longitudinal cross-sectional view of a continuous heat treatment furnace showing an embodiment of the present invention and its temperature diagram, Fig. 2 is a horizontal cross-sectional view of its lehr-cooling zone, and Figs. 3 and 4 are its lehr-cooling zone. FIG. 3 is a horizontal cross-sectional view showing another embodiment of No. 3; FIG. 5 is a longitudinal cross-sectional view of a conventional continuous heat treatment furnace and its temperature diagram. a... Processed material, 2... Heating/soaking zone, 3...
・Slow cooling zone, 7...Circulation fan, 8...Intake port,
IO...Thermocouple, 11...Flow control valve. Diagram 2

Claims (1)

【特許請求の範囲】 1、加熱・均熱帯に続く徐冷帯の炉壁の断熱性を該加熱
・均熱帯から遠ざかるにつれて次第に小さくなるように
したことを特徴とする連続熱処理炉。 2、徐冷帯の出口部付近から吸引したガスを加熱・均熱
帯に循環させる循環ファンを設けて加熱・均熱帯の熱風
を徐冷帯に流動させると共に、徐冷帯の出口部付近にお
ける炉内ガスの温度を検出し、前記循環ファンによるガ
スの循環量をコントロールするようにしたことを特徴と
する特許請求の範囲第1項に記載の連続熱処理炉。
[Scope of Claims] 1. A continuous heat treatment furnace characterized in that the heat insulation property of the furnace wall of the slow cooling zone following the heating/soaking zone gradually decreases as the distance from the heating/soaking zone increases. 2. A circulation fan is installed to circulate the gas sucked in from near the exit of the slow cooling zone to the heating/soaking zone, and the hot air from the heating/soaking zone flows into the slow cooling zone. 2. The continuous heat treatment furnace according to claim 1, wherein the temperature of the internal gas is detected and the amount of gas circulated by the circulation fan is controlled.
JP873386A 1986-01-17 1986-01-17 Continuous heat treatment furnace Expired - Lifetime JPH0633946B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP873386A JPH0633946B2 (en) 1986-01-17 1986-01-17 Continuous heat treatment furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP873386A JPH0633946B2 (en) 1986-01-17 1986-01-17 Continuous heat treatment furnace

Publications (2)

Publication Number Publication Date
JPS62166282A true JPS62166282A (en) 1987-07-22
JPH0633946B2 JPH0633946B2 (en) 1994-05-02

Family

ID=11701150

Family Applications (1)

Application Number Title Priority Date Filing Date
JP873386A Expired - Lifetime JPH0633946B2 (en) 1986-01-17 1986-01-17 Continuous heat treatment furnace

Country Status (1)

Country Link
JP (1) JPH0633946B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006500545A (en) * 2002-09-26 2006-01-05 ビーティーユー インターナショナル インコーポレイテッド Improvement of temperature distribution in convection heating furnace.
JP2010216737A (en) * 2009-03-17 2010-09-30 Tdk Corp Continuous baking furnace and manufacturing system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006500545A (en) * 2002-09-26 2006-01-05 ビーティーユー インターナショナル インコーポレイテッド Improvement of temperature distribution in convection heating furnace.
JP2010216737A (en) * 2009-03-17 2010-09-30 Tdk Corp Continuous baking furnace and manufacturing system

Also Published As

Publication number Publication date
JPH0633946B2 (en) 1994-05-02

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