JPS6235471B2 - - Google Patents
Info
- Publication number
- JPS6235471B2 JPS6235471B2 JP20138982A JP20138982A JPS6235471B2 JP S6235471 B2 JPS6235471 B2 JP S6235471B2 JP 20138982 A JP20138982 A JP 20138982A JP 20138982 A JP20138982 A JP 20138982A JP S6235471 B2 JPS6235471 B2 JP S6235471B2
- Authority
- JP
- Japan
- Prior art keywords
- heated
- objects
- heating
- zone
- heat treatment
- 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 claims description 56
- 238000002791 soaking Methods 0.000 claims description 13
- 239000002912 waste gas Substances 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 7
- 238000002485 combustion reaction Methods 0.000 claims description 6
- 230000007423 decrease Effects 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 230000003247 decreasing effect Effects 0.000 claims description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 238000010010 raising Methods 0.000 description 1
- 238000003756 stirring 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
- C21D9/0006—Details, accessories not peculiar to any of the following furnaces
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、被加熱処理物の個数の変化に対応し
得る経済効率の高い連続熱処理炉の加熱制御方法
に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a highly economically efficient heating control method for a continuous heat treatment furnace that can respond to changes in the number of objects to be heated.
熱処理炉で連続的に熱処理を行う場合、従来で
は、一定速度で被加熱処理物の入つたバスケツト
を搬送しつつ所定の熱処理条件を充足するように
制御しており、処理個数が変化した場合には、炉
内のすべてのバーナを点火した状態で、送り速度
を変えることなくバスケツトの中に入れる被加熱
処理物の個数を変化させることにより対応してい
た。従つて、この方法では処理個数の変化に拘ら
ず、常に炉内の全バーナを点火しているため、燃
料消費が多くなり、不経済である。特開昭第52―
54604号には、異なる形状、寸法、材質の被加熱
処理物が同時に炉内を進行する連続熱処理炉の制
御方法を与えており、この開示されたものでは、
被加熱処理物の加熱条件及び形状等に応じた搬送
速度を与えるとともに、必要に応じて出口に近い
バーナを点火及び停止するようにしている。しか
し、この熱処理では、予熱、昇温、均熱、冷却を
すべて炉内で制御するようにしているため、制御
が複雑になるとともに、均熱行程に連続して大気
中での自然冷却を行えない場合が生じる。 Conventionally, when heat treatment is performed continuously in a heat treatment furnace, the basket containing the objects to be heated is conveyed at a constant speed while being controlled to satisfy predetermined heat treatment conditions. This was handled by changing the number of objects to be heated in the basket without changing the feed speed with all burners in the furnace ignited. Therefore, in this method, all burners in the furnace are always ignited regardless of changes in the number of pieces to be processed, which increases fuel consumption and is uneconomical. Japanese Patent Publication No. 52-
No. 54604 provides a method for controlling a continuous heat treatment furnace in which objects to be heated of different shapes, sizes, and materials proceed through the furnace at the same time.
The conveyance speed is set according to the heating conditions and shape of the object to be heated, and the burner near the outlet is ignited and stopped as necessary. However, in this heat treatment, preheating, temperature raising, soaking, and cooling are all controlled within the furnace, which makes the control complex and requires natural cooling in the atmosphere following the soaking process. There may be cases where this is not the case.
従つて、本発明の目的は、被加熱処理物の個数
の変化に応じて、加熱バーナ点火数を変化させ
て、経済効率を向上させる一方被加熱処理物の搬
送速度を個数の変化に応じて変化させ均熱時間を
一定に保持して所定の熱処理条件を充足する連続
熱処理炉の加熱制御方法を提供することである。 Therefore, an object of the present invention is to improve economic efficiency by changing the number of heating burners fired in accordance with changes in the number of objects to be heated, and at the same time to change the conveyance speed of objects to be heated in accordance with changes in the number of objects to be heated. It is an object of the present invention to provide a heating control method for a continuous heat treatment furnace that satisfies predetermined heat treatment conditions by changing the soaking time and keeping it constant.
本発明の構成は加熱バーナを備えた加熱ゾーン
が直列に複数設けられた熱処理炉の入口から出口
側に被加熱処理物を搬送する一方、前記加熱ゾー
ンの燃焼廃ガスをまとめて入口側の加熱ゾーンを
介して大気に導出し、被加熱処理物の個数の減少
に応じて入口側の加熱ゾーンの加熱バーナから順
次停止し、バーナが点火中の後続加熱ゾーンの燃
焼廃ガスによりバーナが停止した加熱ゾーン内の
被加熱処理物を予熱するとともに被加熱処理物の
搬送速度を被加熱処理物の数の減少に応じて減少
させて均熱時間を被加熱処理物の個数の変化に応
じてほぼ一定に保持することを特徴とする。 The structure of the present invention is such that the material to be heated is transported from the inlet to the outlet side of a heat treatment furnace in which a plurality of heating zones equipped with heating burners are provided in series, while the combustion waste gas from the heating zones is collectively heated at the inlet side. As the number of objects to be heated decreases, the heating burners in the heating zone on the inlet side are stopped sequentially, and the burners are stopped due to combustion waste gas in the subsequent heating zone while the burner is being ignited. The objects to be heated in the heating zone are preheated, and the conveyance speed of the objects to be heated is decreased in accordance with the decrease in the number of objects to be heated, so that the soaking time is kept almost constant as the number of objects to be heated is changed. It is characterized by holding.
本発明によれば、被加熱処理物の個数が変化し
た場合には、それに応じて入口側の加熱ゾーンの
バーナから順次点火数を変化させるようにしてい
る。これにより、燃料が必要以上に消費されるの
が防止される。また、バーナ点火数が変化にかか
わらず均熱時間を一定に保持し得るように被加熱
処理物の搬送速度を変化させている。さらに、バ
ーナを停止した加熱ゾーンでは、後続の加熱ゾー
ンの燃焼廃ガスの熱を利用して被加熱処理物を予
熱することができる。これによつて、経済効率が
高くしかも、所定の熱処理条件を充足し得る連続
熱処理炉の熱処理制御方法が得られる。 According to the present invention, when the number of objects to be heated changes, the number of ignitions of the burners in the heating zone on the inlet side is sequentially changed accordingly. This prevents fuel from being consumed more than necessary. Further, the conveyance speed of the object to be heated is changed so that the soaking time can be kept constant regardless of the change in the number of burner ignitions. Furthermore, in the heating zone where the burner is stopped, the heat of the combustion waste gas in the subsequent heating zone can be used to preheat the object to be heated. This provides a heat treatment control method for a continuous heat treatment furnace that is highly economically efficient and can satisfy predetermined heat treatment conditions.
以下、図面を参照しつつ、本発明の実施例につ
き説明する。 Embodiments of the present invention will be described below with reference to the drawings.
図を参照すれば、連続熱処理炉10は複数の直
列に配列された加熱ゾーン12,14,16,1
8を有しており、各加熱ゾーンは、ゾーン壁2
0,22,24で仕切られている。熱処理炉10
の入口26及び出口28は入口蓋30、出口蓋3
2でそれぞれ外気と遮断される。該入口蓋30、
出口蓋32は図示していないシリンダにより開閉
される。各加熱ゾーンには、加熱バーナ34が配
置されるとともに、ゾーン内を撹拌して、温度を
均一化する図示しないモータで駆動される撹拌機
42が設けられている。各加熱バーナ34は、プ
ロパンやブタンなどと空気とを混合させて燃焼さ
せるようにしている。アルミニウム合金製シリン
ダヘツドなどの被加熱処理物50は、バスケツト
52内に入れられ、熱処理炉の入口26から出口
28の方に順次搬送される。この場合、バスケツ
ト52は炉内に配列されたローラ54の上に互い
に接触した状態で載置されており、入口側でバス
ケツト52をプツシヤシリンダ62により進行方
向に押すとその力は順次、伝わつて、バスケツト
52は出口方向に搬送されるようになつている。
また、入口側に最も近い加熱ゾーン12には、燃
焼廃ガスを収集して大気に排出するための排気ダ
クト56が設けられている。この排気ダクト56
の途中には排風機58が設置され、ダクト56内
の廃ガスを大気に排出する。さらにダクト内には
廃ガスの熱を利用する熱交換器60が設けられ、
この熱交換器60は主としてバーナ用の空気を予
熱するのに用いられる。 Referring to the figure, a continuous heat treatment furnace 10 includes a plurality of heating zones 12, 14, 16, 1 arranged in series.
8, each heating zone has a zone wall 2
It is divided into 0, 22, and 24. Heat treatment furnace 10
The inlet 26 and outlet 28 of the
2, each is cut off from the outside air. the inlet lid 30;
The outlet cover 32 is opened and closed by a cylinder (not shown). Each heating zone is provided with a heating burner 34 and a stirrer 42 driven by a motor (not shown) that stirs the inside of the zone to equalize the temperature. Each heating burner 34 mixes propane, butane, or the like with air and burns the mixture. Objects 50 to be heated, such as aluminum alloy cylinder heads, are placed in a basket 52 and sequentially conveyed from the inlet 26 to the outlet 28 of the heat treatment furnace. In this case, the baskets 52 are placed in contact with each other on rollers 54 arranged in the furnace, and when the baskets 52 are pushed in the advancing direction by a pusher cylinder 62 on the entrance side, the force is sequentially transmitted, The basket 52 is adapted to be conveyed in the direction of the exit.
The heating zone 12 closest to the inlet side is also provided with an exhaust duct 56 for collecting combustion waste gas and discharging it to the atmosphere. This exhaust duct 56
An exhaust fan 58 is installed in the middle of the duct 56 to discharge the waste gas inside the duct 56 to the atmosphere. Furthermore, a heat exchanger 60 is provided in the duct to utilize the heat of the waste gas.
This heat exchanger 60 is mainly used to preheat the air for the burner.
以上のような熱処理炉10を用いて、被加熱処
理物を所定の条件で加熱処理を行う場合におい
て、バスケツト52内にある被加熱処理物50の
処理個数が最大である場合には炉内のバーナ34
は全部点火されている。このとき、各加熱ゾーン
は、例えば、加熱ゾーン12は予熱ゾーンとし
て、ゾーン14は昇温ゾーンとして、ゾーン1
6,18は均熱ゾーンとして機能するように調整
されている。このときのプツシヤシリンダ62に
よるバスケツト52の搬送タクトをTとし、均熱
ゾーン内に収容されるバスケツトの数をn(実施
例ではn=6)とすると、このときの均熱時間T
1はT1=nTである。この均熱時間はアルミニウ
ムシリンダヘツドでは、溶体化処理のため240分
取られ、このときの温度は485℃である。この
後、被加熱処理物50の処理個数が半減した場合
には、例えば加熱ゾーン12のバーナ34を停止
する。これにより、ゾーン12,14は予熱ゾー
ンとして、ゾーン16は昇温ゾーンとして、ゾー
ン18は均熱ゾーンとして機能する。この場合、
バーナ34の廃ガスを入口側に設けたダクト58
により排出するようになつているのでバーナが停
止された加熱ゾーン12を経由する。従つて、加
熱ゾーン12のバーナ34は停止していても予熱
ゾーンとして機能させることができる。このとき
プツシヤシリンダ62によるバスケツト52の搬
送タクトを遅くして2Tとすることにより均熱ゾ
ーン18における均熱時間T2をT2=n/2・2T=
nT=T1と一定に保持することができる。すなわ
ち、経済効率を高く維持しつつ、被加熱処理物の
処理個数の変化に対応させることができる。 When heat-treating objects to be heated under predetermined conditions using the heat treatment furnace 10 as described above, if the number of objects to be heated 50 in the basket 52 is the maximum, the number of objects in the furnace Burner 34
are all lit. At this time, each heating zone is, for example, heating zone 12 as a preheating zone, zone 14 as a temperature increasing zone, zone 1
6 and 18 are adjusted to function as a soaking zone. If the transport tact of the basket 52 by the pusher cylinder 62 at this time is T, and the number of baskets accommodated in the soaking zone is n (n=6 in the embodiment), then the soaking time T at this time is
1 is T1=nT. This soaking time is 240 minutes for the aluminum cylinder head due to solution treatment, and the temperature at this time is 485°C. Thereafter, when the number of objects to be heated 50 to be processed is reduced by half, for example, the burner 34 in the heating zone 12 is stopped. As a result, zones 12 and 14 function as preheating zones, zone 16 functions as a temperature increasing zone, and zone 18 functions as a soaking zone. in this case,
Duct 58 installed on the inlet side for exhaust gas from burner 34
Since the gas is discharged through the heating zone 12 where the burner is stopped. Therefore, even if the burner 34 of the heating zone 12 is stopped, it can function as a preheating zone. At this time, by slowing down the transport tact of the basket 52 by the pusher cylinder 62 to 2T, the soaking time T2 in the soaking zone 18 can be kept constant as T2=n/2.2T=nT=T1. That is, it is possible to respond to changes in the number of objects to be heated while maintaining high economic efficiency.
図は、本発明の1実施例に係る連続熱処理炉の
断面図である。
符号の説明 10……連続熱処理炉、12,1
4,16,18……加熱ゾーン、20,22,2
4……ゾーン壁、34……加熱バーナ、42……
撹拌機、50……被加熱処理物、52……バスケ
ツト。
The figure is a sectional view of a continuous heat treatment furnace according to one embodiment of the present invention. Explanation of symbols 10...Continuous heat treatment furnace, 12,1
4, 16, 18... heating zone, 20, 22, 2
4... Zone wall, 34... Heating burner, 42...
Stirrer, 50... Material to be heated, 52... Basket.
Claims (1)
設けられた熱処理炉の入口から出口側に被加熱処
理物を搬送する一方、前記加熱ゾーンの燃焼廃ガ
スをまとめて入口側の加熱ゾーンを介して大気に
導出し、被加熱処理物の個数の減少に応じて入口
側の加熱ゾーンの加熱バーナから順次停止し、バ
ーナが点火中の後続の加熱ゾーンの燃焼廃ガスに
よりバーナが停止した加熱ゾーン内の被加熱処理
物を予熱するとともに、被加熱処理物の搬送速度
を被加熱処理物の個数の減少に応じて減少させて
均熱時間を被加熱処理物の個数の変化に応じてほ
ぼ一定に保持することを特徴とする連続熱処理炉
の加熱制御方法。1. A material to be heated is transported from the inlet to the outlet side of a heat treatment furnace in which a plurality of heating zones equipped with heating burners are provided in series, while the combustion waste gas from the heating zone is collectively transported through the heating zone on the inlet side. The heating burners in the heating zone on the inlet side are stopped sequentially as the number of objects to be heated decreases, and the burners in the heating zone are stopped due to combustion waste gas in the subsequent heating zone while the burners are being ignited. In addition to preheating the objects to be heated, the conveyance speed of the objects to be heated is decreased according to the decrease in the number of objects to be heated, and the soaking time is kept almost constant according to the change in the number of objects to be heated. 1. A heating control method for a continuous heat treatment furnace, characterized in that:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20138982A JPS5993841A (en) | 1982-11-17 | 1982-11-17 | Method for controlling heating in continuous heat treatment furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20138982A JPS5993841A (en) | 1982-11-17 | 1982-11-17 | Method for controlling heating in continuous heat treatment furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5993841A JPS5993841A (en) | 1984-05-30 |
| JPS6235471B2 true JPS6235471B2 (en) | 1987-08-01 |
Family
ID=16440267
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20138982A Granted JPS5993841A (en) | 1982-11-17 | 1982-11-17 | Method for controlling heating in continuous heat treatment furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5993841A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH042386U (en) * | 1990-04-17 | 1992-01-09 | ||
| KR20230092627A (en) * | 2021-12-17 | 2023-06-26 | 세메스 주식회사 | Substrate treating apparatus and method thereof |
-
1982
- 1982-11-17 JP JP20138982A patent/JPS5993841A/en active Granted
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH042386U (en) * | 1990-04-17 | 1992-01-09 | ||
| KR20230092627A (en) * | 2021-12-17 | 2023-06-26 | 세메스 주식회사 | Substrate treating apparatus and method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5993841A (en) | 1984-05-30 |
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