Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS6235471B2 - - Google Patents
[go: Go Back, main page]

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
Application number
JP20138982A
Other languages
Japanese (ja)
Other versions
JPS5993841A (en
Inventor
Toshifumi Shishida
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.)
Matsuda KK
Original Assignee
Matsuda KK
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 Matsuda KK filed Critical Matsuda KK
Priority to JP20138982A priority Critical patent/JPS5993841A/en
Publication of JPS5993841A publication Critical patent/JPS5993841A/en
Publication of JPS6235471B2 publication Critical patent/JPS6235471B2/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
    • C21D9/0006Details, 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.

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

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)

【特許請求の範囲】[Claims] 1 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:
JP20138982A 1982-11-17 1982-11-17 Method for controlling heating in continuous heat treatment furnace Granted JPS5993841A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (2)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
EP0168788B1 (en) Continuous type atmosphere heat treating furnace
US4740157A (en) Method of calcining solid materials and single column kiln therefor
CA1065135A (en) Scrap preheating system
US1949716A (en) Method of and apparatus for heattreating
US3988012A (en) Rotary hearth
EP1581778B1 (en) Oven
JPS6235471B2 (en)
JPH05172465A (en) Temperature control device for continuous burning furnace
US4321085A (en) Method of sintering pellets
US4578030A (en) Method of and a plant for preheating and, possibly, heat-treating and subsequently dividing rod-shaped material into slugs
AU3982395A (en) Reactor for heating and treating materials in a controlled atmosphere
US2497442A (en) Means for heat-treating material
JPS55107735A (en) Batch annealing furnace operating method
US3930831A (en) Furnace for heat treating glass sheet material
JPS62235401A (en) Method for controlling in-furnace conveying speed of material to be treated in heat treatment furnace
SU1534271A1 (en) Conveyer-type firing machine
RU2206841C2 (en) Method for heat treatment of solid lumpy fuel
JP4091754B2 (en) Annular multi-stage furnace
CA1087836A (en) Scrap preheating system
SU964396A1 (en) Tunnel furnace
SU1323835A1 (en) Method of operating conveyer-type burning machine
SU827931A1 (en) Furnace for heating metals
JPS5633423A (en) Combustion apparatus for atmosphere of continuous nonoxidation heat treating furnace
SU1321760A1 (en) Method of producing iron ore pellets on roasting conveyer machine
KR910001578B1 (en) Continuous heat treatment device of metal strip coil