JPS5970714A - Heating method in heat treatment furnace - Google Patents

Heating method in heat treatment furnace

Info

Publication number
JPS5970714A
JPS5970714A JP18025582A JP18025582A JPS5970714A JP S5970714 A JPS5970714 A JP S5970714A JP 18025582 A JP18025582 A JP 18025582A JP 18025582 A JP18025582 A JP 18025582A JP S5970714 A JPS5970714 A JP S5970714A
Authority
JP
Japan
Prior art keywords
furnace
burner
heat
temp
heaters
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
JP18025582A
Other languages
Japanese (ja)
Other versions
JPS6150123B2 (en
Inventor
Yusuke Furui
古居 佑介
Hiromi Tomishige
富重 博美
Kikuo Enoki
榎 喜久雄
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.)
Toyota Motor Corp
Original Assignee
Toyota Motor Corp
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 Toyota Motor Corp filed Critical Toyota Motor Corp
Priority to JP18025582A priority Critical patent/JPS5970714A/en
Publication of JPS5970714A publication Critical patent/JPS5970714A/en
Publication of JPS6150123B2 publication Critical patent/JPS6150123B2/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
    • C21D1/00General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
    • C21D1/34Methods of heating

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)
  • Heat Treatment Of Strip Materials And Filament Materials (AREA)
  • Furnace Details (AREA)

Abstract

PURPOSE:To control securely the temp. in a heat treatment furnace with a reduction in required energy cost by providing electric heaters and a burner in combination in the furnace, supplying the prescribed quantity of the required quantity of heat with the burner and controlling the heaters to maintain the specified temp. in the furnace. CONSTITUTION:A required set temp. T deg.C is inputted to a temp. controller 11, and and a furnace 3 is heated up to the temp. T deg.C by starting a fan 7, igniting a burner 8 and energizing electric heaters 9. Since the furnace 3 is cold in the beginning when the heating is started, the burner 8 is operated to burn at a high level while the electric power to be supplied to the heaters 9 is increased. The heating period operates on the largest electric power but if several tens % of the required quantity of heat is supplied by the burner 8, the max. power can be decreased largely and since the heating time is shortened, the total energy cost required for the heating is economized. A power control board 10 decreases the power supply to the heaters 9 in accordance with the result of comparison between the signal from the thermocouple 12 of a controller 11 and a set value when the temp. in the furnace is approximate to the T deg.C. The heaters 9 are controlled by the board 10 and the burner 8 is put into the combustion state at a low level when the furnace temp. attains the T deg.C.

Description

【発明の詳細な説明】 この発明は焼入炉や焼戻し炉などの熱処理炉における加
熱方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heating method in a heat treatment furnace such as a quenching furnace or a tempering furnace.

従来から各種金属製品の熱処理炉として、重油バーナや
ガスバーナ等のバーナを加熱装置としたタイプのものや
、電熱ヒータを加熱装置としたタイプのものが知られて
いるが、これらのタイプの熱処理炉には一長一短があり
、熱処理対象物や要求される熱処理条件によってそれぞ
れ使い分けられている。たとえば、アルミ鋳物やアルミ
合金鋳物を熱処理する場合は、加熱温度を所期の温度か
ら±5℃程度の範囲に保たなければならない場合もある
ので、温度制御の容易性、的確性の点がらすると、電熱
ヒータを加熱装置とした熱処理炉が好ましい。これに対
し、エネルギーコストの点がらすると、電力コストが極
めて高いのが実情であるから、バーナを加熱装置としだ
熱処理炉が好ましい。ざらに、例えば自動車用鋳造部品
にあっては、軽量化のために薄肉化が図られているため
、中子砂払い落し工程で充分な振動衝撃を掛けられない
場合があり、このような鋳造部品を対象物とした場合に
は、熱硬化性樹脂を含んだ中子砂を熱処理工程で焼くこ
とが望まれるが、バーナを加熱装置とした熱処理炉では
、炉内の酸素濃度が低下し、中子砂を充分焼くことがで
きない場合があり、したがって中子砂を充分に焼く点か
らすると、電熱ヒータを加熱装置とした熱処理炉が好ま
しい。
Conventionally, heat treatment furnaces for various metal products have been known, including those that use a burner such as a heavy oil burner or gas burner as the heating device, and those that use an electric heater as the heating device. Each has advantages and disadvantages, and each is used depending on the object to be heat treated and the required heat treatment conditions. For example, when heat treating aluminum castings or aluminum alloy castings, it may be necessary to maintain the heating temperature within a range of approximately ±5°C from the desired temperature. In this case, a heat treatment furnace using an electric heater as a heating device is preferable. On the other hand, from the point of view of energy cost, the fact is that the electric power cost is extremely high, so a heat treatment furnace using a burner as a heating device is preferable. Generally speaking, for example, in the case of cast parts for automobiles, the walls are made thinner to reduce weight, so it may not be possible to apply sufficient vibration and shock during the core sand removal process. When the object is a component, it is desirable to bake core sand containing thermosetting resin in the heat treatment process, but in a heat treatment furnace that uses a burner as a heating device, the oxygen concentration in the furnace decreases. There are cases where the core sand cannot be baked sufficiently, so from the viewpoint of sufficiently baking the core sand, a heat treatment furnace using an electric heater as a heating device is preferable.

しかるに従来では、電熱ヒータもしくはバーナのいずれ
か一方で加熱しているのが一般的であって、上述したよ
うな相反する要請のいずれをも満足し得ないのが実情で
あり、たとえばアルミ鋳物もしくはアルミ合金鋳物を熱
処理する場合には、専ら電熱ヒータによって加熱し、多
大のエネルギーコストをかけていた。
However, in the past, it was common to heat with either an electric heater or a burner, and the reality is that it is impossible to satisfy either of the conflicting requirements mentioned above. When aluminum alloy castings are heat treated, they are heated exclusively by electric heaters, which requires a large amount of energy cost.

この発明は上記の事情に鑑みてなされたもので、炉内温
度を容易かつ的確に制御することができるうえに、対象
物に付着している中子砂を確実に焼くことができ6しか
も所要エネルギーコストの低廉化を図ることのできる熱
処理炉における加熱方法を提供することを目的とするも
のである。そしてこの発明の特徴とするところは、発熱
量が一定となるようバーナを固定燃焼させて必要熱量の
うち所定の割合の熱量を炉内に供給する一方、必要熱量
のうち残部を電熱ヒータによって供給しかつ炉内温度が
一定となるよう電熱ヒータの熱量を制御する点にある。
This invention was made in view of the above circumstances, and it is possible to easily and accurately control the temperature inside the furnace, and also to reliably burn the core sand attached to the object. The object of the present invention is to provide a heating method in a heat treatment furnace that can reduce energy costs. The feature of this invention is that the burner is fixedly combusted so that the calorific value is constant, and a predetermined proportion of the required heat is supplied into the furnace, while the remainder of the required heat is supplied by the electric heater. Moreover, the heat amount of the electric heater is controlled so that the temperature inside the furnace is constant.

以下この発明を実施例に基づいて詳細に説明する。The present invention will be described in detail below based on examples.

まずこの発明の方法を実施するための装置について説明
すると、第1図はこの発明の方法を実施し得るよう構成
した熱風循環式連続熱処理炉の一例を示す略解断面図で
あって、熱処理製品バスケット1を搬送するコンベヤ2
が類3内に設けられており、そのコンベヤ2上の熱処理
製品バスケット1を覆うようバッフル4が類3内に設置
されている。そのバッフル4の左右両側壁には、熱風流
    ・八日5が形成され、またバッフル4の天井部
には、吸込口をパンフル4内に向けて開口させかつ炉3
の上部に設けたモータ6によって駆動される循環ファン
7が設けられており、したがって類3内の気体が循環フ
ァン7によってバッフル4の内部と外部とを循環流動す
るようになっている。
First, to explain the apparatus for implementing the method of the present invention, FIG. 1 is a schematic cross-sectional view showing an example of a hot air circulation type continuous heat treatment furnace configured to implement the method of the present invention. Conveyor 2 that conveys 1
is provided in category 3, and a baffle 4 is provided in category 3 to cover the heat-treated product basket 1 on the conveyor 2. Hot air currents 5 are formed on the left and right side walls of the baffle 4, and the ceiling of the baffle 4 has a suction port opened toward the inside of the panfur 4 and the furnace 3.
A circulation fan 7 driven by a motor 6 provided on the upper part of the baffle 4 is provided, so that the gas in the group 3 is circulated between the inside and outside of the baffle 4 by the circulation fan 7.

また炉3の側壁部に重油バーナあるいはガスノ\−す等
のバーナ8が炉3の内部、より正確にはバッフル4と炉
壁との間に向けて設置されており、さらに炉3の天井部
には、電熱ヒータ9が類3内に垂下して設けられている
。その電熱ヒータ9は発熱量を制御するための電力制御
盤10に接続されており、さらにその電力制御盤10に
温度調節計11が接続されている。温度調節計11は予
め定めた設定温度を入力しておく機能および所定の温度
検出器からの入力信号と設定温度とを比較演算して出力
する■能を具備したものであって、その温度検出器とし
て熱雷対12が前記バッフル4の内部に挿入されている
。したがってバッフル4内の温度に応じて熱雷対12が
出力する信号と予め定めた設定温度に対応する設定値と
を温度調節計11が比較演算してその結果を出力し、温
度調節計11の出力信号によって電力料t[li!10
が動作し、電熱ヒータ9の発熱量を制御するようになっ
ている。
Furthermore, a burner 8 such as a heavy oil burner or a gas nozzle is installed on the side wall of the furnace 3 toward the inside of the furnace 3, more precisely between the baffle 4 and the furnace wall, and is further installed on the ceiling of the furnace 3. , an electric heater 9 is provided hanging down inside the casing 3. The electric heater 9 is connected to a power control panel 10 for controlling the amount of heat generated, and a temperature controller 11 is further connected to the power control panel 10. The temperature controller 11 has a function of inputting a predetermined set temperature and a function of comparing and calculating an input signal from a predetermined temperature detector and the set temperature and outputting the result. A thermal lightning pair 12 is inserted inside the baffle 4 as a container. Therefore, the temperature controller 11 compares and calculates the signal output by the thermal lightning pair 12 according to the temperature inside the baffle 4 and the set value corresponding to a predetermined set temperature, and outputs the result. The power charge t[li! 10
is operated to control the amount of heat generated by the electric heater 9.

つぎに上記のように構成した熱処理炉における加熱方法
すなわちこの発明の詳細な説明する。
Next, the heating method in the heat treatment furnace configured as described above, that is, the present invention will be explained in detail.

まず、温度調節計11に所期の設定温rIT℃(例えば
500℃)を入力しておくとともに、循環ファン7を動
作させ、その状態でバーナ8に点火し、かつ電熱ヒータ
9を通電発熱させる。第2図<A)は炉内温度の推移を
示す線図であり、第2図(B)はバーナ8および電熱ヒ
ータ9の発熱量を示す線図であって、加熱開始当初は炉
3が室温程度に冷えているので、熱処理を行う以前に炉
3を設定温度T℃まで昇温する必要があり、そのため加
熱開始当初はバーナ8を高レベルで燃焼させて発熱量を
多(し、かつ電熱ヒータ9に対する供給電力を多く設定
しその発熱量を高くする。この昇温期間における電力が
最大電力となるが、昇温に必要な熱量のうちの数十%例
えば20〜70%をバーナ8によって供給することによ
り、電熱ヒータのみによって加熱する場合と比べて最大
電力を大幅に低下させることができ、したがって買電の
場合には契約電力を低くできるので、ランニングコスト
の低廉化に大きく資することができる。また逆に昇温詩
において既存の契約電力の限度程度まで電力を使った場
合には、バーナ8による熱量が付加されることになるた
め、昇温時間を短縮でき、したがって電力消費量が少な
くなるためにバーナ8で消費するエネルギーコストを考
え合せても、昇温に要する総エネルギーコストを低廉化
することができる。
First, input a desired set temperature rIT°C (for example, 500°C) into the temperature controller 11, operate the circulation fan 7, ignite the burner 8 in this state, and energize the electric heater 9 to generate heat. . Fig. 2 <A) is a diagram showing the transition of the temperature inside the furnace, and Fig. 2 (B) is a diagram showing the calorific value of the burner 8 and the electric heater 9. Since it is cooled to about room temperature, it is necessary to raise the temperature of the furnace 3 to the set temperature T℃ before heat treatment. Therefore, at the beginning of heating, the burner 8 is burned at a high level to generate a large amount of heat (and The amount of power supplied to the electric heater 9 is increased to increase its calorific value.The electric power during this heating period becomes the maximum electric power, but several tens of percent, for example 20 to 70%, of the amount of heat required for heating is supplied to the burner 8. By supplying electricity by heating, the maximum power can be significantly lowered compared to the case of heating only with electric heaters, and therefore the contract power can be lowered in the case of power purchase, which greatly contributes to lower running costs. On the other hand, if electricity is used up to the limit of the existing contract electricity in the heating process, the amount of heat generated by burner 8 will be added, so the heating time can be shortened, and therefore the electricity consumption will be reduced. Even if the energy cost consumed by the burner 8 is taken into account, the total energy cost required for temperature increase can be reduced.

以上のようにして炉3の内部を加熱した結果炉3の内部
温度が設定温度T℃近くまでに達すると、局部的な温度
のバラつきがあるために、温度調節計11における熱電
対12からの入力信号と設定値との比較結果に基づいて
電力制御盤10が電熱ヒータ9に対する供給電力を低下
させるので、電熱ヒータ9の発熱Rが一時的に低下する
。すなわち電熱ヒータ9の発熱量を制御することにより
炉3の内部温度が制御され、その結果炉3の内部全体が
設定温度T℃になると、電熱ヒータ9が電力料t11盤
10によって制御されてその発熱量が大幅に低下し、こ
れと同時にバーナ8を低レベルの燃焼状態に切り換え、
その状態で熱処理製品をバスケット1に入れて類3内に
送り込むことにより、熱処理製品の加熱すなわちランニ
ングを行う。したがってランニング時においてもバーナ
8と電熱ヒータ9とによって加熱することになるが、そ
の場合のバーナ8の燃焼は、低レベルでかつ発熱量が一
定となる固定燃焼としておく。ここで低レベルの燃焼と
は、バーナ8に対する二次空気および熱処理製品の炉3
に対する搬入・搬出時の扉開閉に伴って類3内に侵入す
る外気によって類3内の02濃度が15%以上となるよ
うな燃焼状態である。
As a result of heating the inside of the furnace 3 as described above, when the internal temperature of the furnace 3 reaches close to the set temperature T°C, the temperature changes from the thermocouple 12 in the temperature controller 11 due to local temperature variations. Since the power control panel 10 reduces the power supplied to the electric heater 9 based on the comparison result between the input signal and the set value, the heat generation R of the electric heater 9 is temporarily reduced. That is, the internal temperature of the furnace 3 is controlled by controlling the calorific value of the electric heater 9, and as a result, when the entire inside of the furnace 3 reaches the set temperature T°C, the electric heater 9 is controlled by the power consumption board 10 and its temperature is increased. The calorific value decreases significantly, and at the same time, burner 8 is switched to a low-level combustion state,
In this state, the heat-treated product is placed in the basket 1 and fed into the casing 3, thereby heating, that is, running the heat-treated product. Therefore, even during running, heating is performed by the burner 8 and the electric heater 9, but the combustion in the burner 8 in this case is fixed combustion at a low level and with a constant calorific value. Low level combustion here refers to the secondary air to burner 8 and the furnace 3 of the heat treated product.
This is a combustion state in which the 02 concentration within Class 3 becomes 15% or more due to outside air entering the Class 3 interior when the door is opened and closed during loading and unloading.

すなわち本発明者等の実験によれば、熱処理製品に付着
している中子砂を焼き落すためには、類3内の02?1
1度が最低15%程度あれば充分であるからである。第
3図に本発明者等が行った実験における類3内の021
度の推移を示す。
In other words, according to the experiments of the present inventors, in order to burn off the core sand adhering to the heat-treated product,
This is because it is sufficient that the degree of 1 degree is at least about 15%. Figure 3 shows 021 in class 3 in the experiment conducted by the inventors.
It shows the change in degree.

ところでランニング時には、熱処理製品の搬入・搬出の
ため扉を開閉することによる外気の侵入、空温程度の低
温度の熱処理製品の新規搬入、また加熱を完了した熱処
理製品の搬出、さらには炉壁からの放熱等によって炉3
の内部温度が低下するが、内部温度の低下が生じると、
温度調節計11が熱雷対12からの入力信号と設定値と
を比較して信号を出力し、その出力信号によって電力制
御盤10が電熱ヒータ9に供給する電力示を増大させる
ので、炉3の内部が従前よりも加熱され、゛その結果炉
3の内部温度が設定温度T℃にほぼ一定に保たれる。す
なわちランニング時においても炉3の内部温度の制御を
、電熱ヒータ9の発熱量を制御することによって行う。
By the way, during running, outside air enters when the door is opened and closed to carry in and take out heat-treated products, new heat-treated products at a temperature as low as air temperature are brought in, heated heat-treated products are carried out, and heat-treated products are removed from the furnace wall. Furnace 3 due to heat radiation, etc.
The internal temperature of decreases, but when the decrease in internal temperature occurs,
The temperature controller 11 compares the input signal from the thermal lightning pair 12 with a set value and outputs a signal, and the power control panel 10 increases the power indication supplied to the electric heater 9 based on the output signal, so that the furnace 3 The inside of the furnace 3 is heated more than before, and as a result, the internal temperature of the furnace 3 is kept almost constant at the set temperature T°C. That is, even during running, the internal temperature of the furnace 3 is controlled by controlling the amount of heat generated by the electric heater 9.

したがってバーナ8の発熱量の微妙な制御は一般に困難
であり、これに加え類3内の02濃度の調整のためには
バーナ8の二次空気の制御も必要であるが、この発明の
方法では上述したようにバーナ8を固定燃焼とし、温度
1iIJ t[Iを電熱ヒータ9の発熱量を制御するこ
とにより行うから、炉3の内部温度の制御を容易かつ的
確に行うことができる。またバーナ8を設置したことに
より、電力よりもエネルギー単価の安い熱源を併用する
ことになるから、総エネルギーコストを低く抑えること
ができる。
Therefore, it is generally difficult to delicately control the calorific value of the burner 8, and in addition to this, it is necessary to control the secondary air of the burner 8 in order to adjust the 02 concentration within Class 3, but the method of this invention As described above, since the burner 8 is set to fixed combustion and the temperature 1iIJ t[I is controlled by controlling the calorific value of the electric heater 9, the internal temperature of the furnace 3 can be controlled easily and accurately. Furthermore, by installing the burner 8, a heat source with a lower energy unit price than electricity is used in combination, so the total energy cost can be kept low.

なお、上記の実施例では連続熱処理炉を例に採ったが、
この発明はバッチ式(回分式)熱処理炉にも適用できる
ことは勿論である。
In addition, although a continuous heat treatment furnace was used as an example in the above example,
Of course, the present invention can also be applied to a batch type heat treatment furnace.

以上の説明から明らかなようにこの発明の加熱方法によ
れば、発熱量が一定となるようバーナを固定燃焼させて
必要熱量のうち所定の割合の熱量を炉内に供給する一方
、必要熱量のうち残部を電熱ヒータによって供給しかつ
炉内温度が一定となるよう電熱ヒータの熱量を制御する
方法であるから、温度制御を電気的に行うことになるた
めに炉の内部温度を容易かつ的確に制御することができ
、しかも電力の他に電力よりもエネルギー単価の安い重
油やLPG等のエネルギー源を用いるから、必要総エネ
ルギーコストを低廉化することができ、同時にバーナの
燃焼状態を所定レベル以下にすることにより、中子砂を
良好に焼き落すことができる。また加熱開始当初の昇温
時には大熱量を必要とするが、この発明の方法ではバー
ナを併用したことにより、所要電力筒を従来よりも大幅
に少なくすることができるため、買電の場合には契約電
力を低く抑えることができ、同時に必要昇温時間が短く
なるために電力消費量が少なくなり、これらの点からも
所要エネルギーコストの低廉化を図ることができる。さ
らにバーナを設けたことにより、炉の内部圧力が大気圧
より若干高い正圧となるので、扉開閉時に炉内に侵入す
る大気量が少なくなり、したがって炉内の温度分布をよ
り均一化することができる。
As is clear from the above description, according to the heating method of the present invention, the burner is fixedly combusted so that the calorific value is constant, and a predetermined proportion of the required heat is supplied into the furnace. The remainder is supplied by an electric heater, and the amount of heat from the electric heater is controlled so that the temperature inside the furnace remains constant.Since temperature control is performed electrically, the internal temperature of the furnace can be easily and accurately adjusted. Furthermore, since energy sources such as heavy oil and LPG, which have lower energy unit costs than electricity, are used in addition to electricity, the total required energy cost can be lowered, and at the same time, the combustion state of the burner can be kept below a predetermined level. By doing so, the core sand can be burnt off well. In addition, a large amount of heat is required to raise the temperature at the beginning of heating, but by using the method of this invention in combination with a burner, the required electric power tube can be significantly reduced compared to the conventional method, so in the case of electricity purchase. The contract power can be kept low, and at the same time, the required heating time is shortened, so power consumption is reduced, and from these points of view as well, the required energy cost can be reduced. Furthermore, by installing a burner, the internal pressure of the furnace becomes a positive pressure that is slightly higher than atmospheric pressure, which reduces the amount of air that enters the furnace when the door is opened and closed, thus making the temperature distribution inside the furnace more uniform. I can do it.

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

第1図はこの発明の方法を実施するための熱処理炉の一
例を示す略解断面図、第2図(A>は炉の内部温度の推
移を示す線図、第2図(B)は電熱ヒータとバーナとの
発熱量の推移を示す線図、第3図は炉内の02m度の推
移を示す線図である。 3・・・炉、 8・・・バーナ、 9・・・N熱ヒータ
、10・・・電力料m+盤、 11・・・温度調節計、
 12・・・熱電対。 出願人  トヨタ自動車株式会社 代理人  弁理士 豊 1)武 久 (ほか1名) 第1図 手   続   補   正   書  (自発)昭和
57年11月29F! 特許庁長官  若 杉 和 夫 殿 1、事件の表示 昭和57年特許願第180255号 2、発明の名称 熱処理炉における加熱方法 3、補正をする者 事件との関係 特許出願人 住 所   愛知県豊田市トヨタ町1番地名 称  (
320) l−ヨタ自動車株式会社4、代理人 住  所  東京都港区三田3丁目4番18号5、補正
の対象 明りl書の「発明の詳細な説明」の欄 6、補正の内容 明細書第2頁第4行目の「これらのタイプの」とあるの
を「これらのタイプの」と訂正する。
Figure 1 is a schematic cross-sectional view showing an example of a heat treatment furnace for carrying out the method of the present invention, Figure 2 (A> is a diagram showing changes in the internal temperature of the furnace, and Figure 2 (B) is an electric heater. Fig. 3 is a diagram showing the transition of the calorific value between the burner and the burner, and Fig. 3 is a diagram showing the transition of 02m degrees inside the furnace. 3...furnace, 8...burner, 9...N heat heater , 10...Electricity charge m+ panel, 11...Temperature controller,
12...Thermocouple. Applicant Toyota Motor Corporation Representative Patent Attorney Yutaka 1) Hisashi Take (and 1 other person) Amendment to Figure 1 Procedures (Voluntary) November 29, 1980! Commissioner of the Japan Patent Office Kazuo Wakasugi1, Indication of the case, Patent Application No. 180255 of 19802, Title of the invention: Heating method in a heat treatment furnace3, Relationship with the amended person case Address of the patent applicant: Toyota City, Aichi Prefecture Toyota Town 1 name (
320) l-Yota Jidosha Co., Ltd. 4, Agent address: 3-4-18-5, Mita, Minato-ku, Tokyo, ``Detailed description of the invention'' column 6 of the statement of subject matter of the amendment, Statement of contents of the amendment In the fourth line of page 2, "of these types" is corrected to "of these types."

Claims (2)

【特許請求の範囲】[Claims] (1)熱処理炉内に電熱ヒータを設置するとともに、そ
の熱処理炉内に向けてバーナを設置しておき、バーナを
その発熱量が一定となるよう固定燃焼させて必要熱量の
うち所定の熱量を炉内に供給する一方、必要熱量の残部
を前記電熱ヒータによって供給しかつ炉内温度を一定に
保つべく電熱ヒータの発熱量を制御することにより、前
記電熱ヒータとバーナとによって炉内を加熱することを
特徴とする熱処理炉における加熱方法。
(1) An electric heater is installed in the heat treatment furnace, and a burner is installed facing the inside of the heat treatment furnace, and the burner is fixedly burned so that its calorific value remains constant to generate a predetermined amount of heat out of the required amount of heat. While supplying heat into the furnace, the electric heater and the burner heat the inside of the furnace by supplying the remainder of the required amount of heat by the electric heater and controlling the amount of heat generated by the electric heater to keep the furnace temperature constant. A heating method in a heat treatment furnace characterized by:
(2)前記熱処理炉内の酸素濃度が15%以上となるよ
う前記バーナを固定燃焼させることを特徴とする特許請
求の範囲第1項記載の熱処理炉における加熱方法。
(2) A heating method in a heat treatment furnace according to claim 1, characterized in that the burner is operated in a fixed manner so that the oxygen concentration in the heat treatment furnace becomes 15% or more.
JP18025582A 1982-10-14 1982-10-14 Heating method in heat treatment furnace Granted JPS5970714A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18025582A JPS5970714A (en) 1982-10-14 1982-10-14 Heating method in heat treatment furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18025582A JPS5970714A (en) 1982-10-14 1982-10-14 Heating method in heat treatment furnace

Publications (2)

Publication Number Publication Date
JPS5970714A true JPS5970714A (en) 1984-04-21
JPS6150123B2 JPS6150123B2 (en) 1986-11-01

Family

ID=16080060

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18025582A Granted JPS5970714A (en) 1982-10-14 1982-10-14 Heating method in heat treatment furnace

Country Status (1)

Country Link
JP (1) JPS5970714A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6154612A (en) * 1984-08-24 1986-03-18 Toshiba Corp Manufacture of core
JPS62243718A (en) * 1986-04-16 1987-10-24 Nisshin Steel Co Ltd Heat treatment of cold rolled stainless steel strip
JP2014114510A (en) * 2012-11-30 2014-06-26 Bilstein Gmbh & Co Kg Hood-type annealing furnace and method for operating the same
CN110699533A (en) * 2019-10-12 2020-01-17 哈尔滨飞机工业集团有限责任公司 Heat treatment furnace convenient for temperature measurement and capable of reducing temperature measurement errors
KR102411139B1 (en) * 2021-10-15 2022-06-22 주식회사 동성테크 High-efficiency hybrid heat treatment device

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109987925A (en) * 2019-04-15 2019-07-09 丽水学院 A method of kiln and application kiln that firing Longquan celadon electrical bond fires Longquan celadon

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6154612A (en) * 1984-08-24 1986-03-18 Toshiba Corp Manufacture of core
JPH0552653B2 (en) * 1984-08-24 1993-08-06 Tokyo Shibaura Electric Co
JPS62243718A (en) * 1986-04-16 1987-10-24 Nisshin Steel Co Ltd Heat treatment of cold rolled stainless steel strip
JP2014114510A (en) * 2012-11-30 2014-06-26 Bilstein Gmbh & Co Kg Hood-type annealing furnace and method for operating the same
CN110699533A (en) * 2019-10-12 2020-01-17 哈尔滨飞机工业集团有限责任公司 Heat treatment furnace convenient for temperature measurement and capable of reducing temperature measurement errors
KR102411139B1 (en) * 2021-10-15 2022-06-22 주식회사 동성테크 High-efficiency hybrid heat treatment device

Also Published As

Publication number Publication date
JPS6150123B2 (en) 1986-11-01

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