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JPS6356288B2 - - Google Patents
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JPS6356288B2 - - Google Patents

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Publication number
JPS6356288B2
JPS6356288B2 JP3602281A JP3602281A JPS6356288B2 JP S6356288 B2 JPS6356288 B2 JP S6356288B2 JP 3602281 A JP3602281 A JP 3602281A JP 3602281 A JP3602281 A JP 3602281A JP S6356288 B2 JPS6356288 B2 JP S6356288B2
Authority
JP
Japan
Prior art keywords
furnace body
heating
zone
carbon monoxide
heated
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
JP3602281A
Other languages
Japanese (ja)
Other versions
JPS57149417A (en
Inventor
Kuniaki Honda
Kunihiro Funamoto
Kanta Akagi
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.)
Osaka Gas Co Ltd
Original Assignee
Osaka Gas 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 Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP3602281A priority Critical patent/JPS57149417A/en
Publication of JPS57149417A publication Critical patent/JPS57149417A/en
Publication of JPS6356288B2 publication Critical patent/JPS6356288B2/ja
Granted legal-status Critical Current

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  • Heat Treatments In General, Especially Conveying And Cooling (AREA)
  • Tunnel Furnaces (AREA)

Description

【発明の詳細な説明】 本発明は直火式加熱炉に関する。[Detailed description of the invention] The present invention relates to a direct-fired heating furnace.

従来から鋼材や銅合金などの被加熱物を加熱す
る直火式加熱炉において、被加熱物を装入するた
めの扉やその他の間隙から空気が侵入すると、被
加熱物が酸化されて被加熱物表面に酸化膜が形成
される。そのため加熱後に鋼材や銅合金などを圧
延やプレス等の加工を行なう場合に、前記酸化膜
が製品に付着したり圧入されるなど不良品の発生
原因となつていた。
Conventionally, in direct-fired heating furnaces that heat materials such as steel and copper alloys, if air enters through the door or other gaps used to charge the materials, the materials will be oxidized and the materials will be heated. An oxide film is formed on the surface of the object. Therefore, when steel materials, copper alloys, etc. are subjected to processing such as rolling or pressing after heating, the oxide film adheres to the product or is press-fitted into the product, causing defective products.

そのような欠点を解消するために、炉内を無酸
化状態にして加熱するには、加熱炉を間接加熱式
や電気加熱式として、雰囲気ガスを封入した炉内
で輻射熱によつて被加熱物を加熱する必要があ
る。ところが、被加熱物が銅または銅合金である
場合には、被加熱物表面の黒度が小であるため、
前記輻射熱によつては加熱時間が長くなり、した
がつて加熱炉が大形化する。また、このような間
接加熱あるいは電気加熱では設備費が高くなると
ともに運転費が高くなる。
In order to eliminate such drawbacks and heat the inside of the furnace in a non-oxidizing state, the heating furnace should be of an indirect heating type or an electric heating type. need to be heated. However, when the object to be heated is copper or a copper alloy, the blackness of the surface of the object to be heated is small;
The radiant heat increases the heating time and therefore increases the size of the heating furnace. In addition, such indirect heating or electric heating increases equipment costs and operating costs.

本発明は、上述の技術的課題を解決し、無酸化
状態で加熱しうる直火式加熱炉を提供することを
目的とする。
An object of the present invention is to solve the above-mentioned technical problems and provide a direct-fired heating furnace that can heat in a non-oxidizing state.

本発明は、被加熱物10の搬送方向に沿つて被
加熱物10の装入口2から排出口3に向けて予熱
帯6、加熱帯7および均熱帯8がこの順序で形成
され、前記装入口2付近には、燃焼排ガスを排出
する排気管11が設けられ、加熱帯7および均熱
帯8には加熱用バーナ9が設けられ、加熱帯7お
よび均熱帯8には噴出孔13が設けられる炉本体
1と、 噴出孔13に可燃性ガスを供給する管路15
と、 管路15に介在される流量制御弁16と、 炉本体1内で前記排出口3に近接した位置に設
けられ、一酸化炭素濃度を検出する一酸化炭素濃
度検出器18と、 前記一酸化炭素濃度検出器18からの出力に応
答し、炉本体1内の一酸化炭素濃度が予め定める
値になるように流量制御弁16の開度を調節する
手段19とを含むことを特徴とする直火式加熱炉
である。
In the present invention, a preheating zone 6, a heating zone 7, and a soaking zone 8 are formed in this order from the charging port 2 of the heated object 10 toward the discharge port 3 along the conveyance direction of the heated object 10, and the charging port 2, an exhaust pipe 11 for discharging combustion exhaust gas is provided, a heating burner 9 is provided in the heating zone 7 and the soaking zone 8, and an ejection hole 13 is provided in the heating zone 7 and the soaking zone 8. Main body 1 and pipe line 15 for supplying flammable gas to jet hole 13
a flow rate control valve 16 interposed in the pipe line 15; a carbon monoxide concentration detector 18 provided in the furnace body 1 at a position close to the discharge port 3 to detect the carbon monoxide concentration; It is characterized by including means 19 for adjusting the opening degree of the flow rate control valve 16 in response to the output from the carbon oxide concentration detector 18 so that the carbon monoxide concentration in the furnace body 1 becomes a predetermined value. It is a direct-fired heating furnace.

以下、図面によつて本発明の実施例を説明す
る。図面は本発明の一実施例の断面図である。こ
の直火式加熱炉の炉本体1は、横方向に長く形成
されており、その一端部(図面の右端部)には装
入口2が形成され、他端部(図面の左端部)には
排出口3が形成される。これらの装入口2よび排
出口3には、上下に変位自在の扉4,5がそれぞ
れ設けられる。炉本体1内は、装入口2から排出
口3に向けて順に、予熱帯6、加熱帯7および均
熱帯8が設定される。加熱帯7および均熱帯8に
は、複数の加熱用バーナ9が設けられる。
Embodiments of the present invention will be described below with reference to the drawings. The drawing is a sectional view of one embodiment of the present invention. The furnace body 1 of this direct-fired heating furnace is formed long in the horizontal direction, and a charging port 2 is formed at one end (the right end in the drawing), and at the other end (the left end in the drawing). A discharge port 3 is formed. These charging port 2 and discharge port 3 are provided with doors 4 and 5, respectively, which are vertically displaceable. Inside the furnace body 1, a preheating zone 6, a heating zone 7, and a soaking zone 8 are set in order from the charging port 2 toward the discharge port 3. A plurality of heating burners 9 are provided in the heating zone 7 and the soaking zone 8.

鋼材や銅合金などの被加熱物10は、装入口2
から炉本体1内に装入され、図示しない搬送手段
によつて炉本体1内を排出口3に向けて連続的に
搬送される。予熱帯6、加熱帯7および均熱帯8
を順次経過することによつて加熱された被加熱物
10は排出口3から排出される。一方、加熱バー
ナ9からの燃焼排ガスは、被加熱物10の搬送方
向と逆方向に流通し、炉本体1の装入口2附近の
上部に設けられた排気管11から排出される。
The object to be heated 10 such as steel material or copper alloy is inserted into the charging port 2
It is then charged into the furnace body 1 and continuously conveyed within the furnace body 1 toward the discharge port 3 by a conveying means (not shown). Pre-heating zone 6, heating zone 7 and soaking zone 8
The heated object 10 is discharged from the discharge port 3. On the other hand, the combustion exhaust gas from the heating burner 9 flows in a direction opposite to the conveyance direction of the object to be heated 10 and is discharged from an exhaust pipe 11 provided at the upper part of the furnace body 1 near the charging port 2 .

このような直火式加熱炉において、炉本体1内
に空気が外部から侵入すると、被加熱物10は前
記空気中の酸素と反応して被加熱物10の表面に
酸化膜が形成される。しかもそのような酸化反応
は被加熱物10が高温となつている場合に促進さ
れる。
In such a direct-fired heating furnace, when air enters the furnace body 1 from the outside, the object to be heated 10 reacts with oxygen in the air, and an oxide film is formed on the surface of the object to be heated 10 . Moreover, such an oxidation reaction is accelerated when the heated object 10 is at a high temperature.

上述のような直火式加熱炉において、酸化防止
のために加熱用バーナ9における燃料と空気の比
率を調整し、炉本体1内を無酸化状態に保つこと
は可能である。しかし炉本体1内の温度制御を行
うために、各加熱バーナ9の燃焼量が変化するの
に対応して空燃比を一定に保つことは困難であ
り、また外部か侵入する空気に対応して燃料供給
量を調節することは困難である。さらに各加熱用
バーナ9に供給する空気を理論空気量以下にして
おくと、未燃ガスや煤が発生することになり、省
エネルギーや環境汚染の点からみて好ましくな
い。外部から侵入する空気を防止するために排気
管11の途中にダンパ12を設けて、炉本体1内
を若干の正圧に保つておけば、外部から侵入する
空気量を抑えることができるが、被加熱物10を
炉本体1内に装入したり排出したりする際に、扉
4,5を開放すると装入口2および排出口3の上
部から燃焼ガスが排出し、それに応じて下部から
空気が侵入する。したがつて炉内圧力を制御する
ことによつては外部空気の侵入を防ぎ得ない。
In the direct-fired heating furnace as described above, it is possible to maintain the inside of the furnace body 1 in an oxidation-free state by adjusting the ratio of fuel and air in the heating burner 9 to prevent oxidation. However, in order to control the temperature inside the furnace body 1, it is difficult to maintain a constant air-fuel ratio in response to changes in the combustion amount of each heating burner 9, and it is difficult to maintain a constant air-fuel ratio in response to changes in the combustion amount of each heating burner 9. It is difficult to regulate the amount of fuel supplied. Furthermore, if the air supplied to each heating burner 9 is kept below the theoretical air amount, unburned gas and soot will be generated, which is undesirable from the point of view of energy saving and environmental pollution. If a damper 12 is provided in the middle of the exhaust pipe 11 to prevent air from entering from the outside and a slight positive pressure is maintained inside the furnace body 1, the amount of air entering from the outside can be suppressed. When the objects 10 to be heated are charged into or discharged from the furnace body 1, when the doors 4 and 5 are opened, combustion gas is discharged from the upper part of the charging port 2 and the discharge port 3, and air is discharged from the lower part accordingly. invades. Therefore, the intrusion of outside air cannot be prevented by controlling the pressure inside the furnace.

そこで、本発明では炉本体1内に外部から空気
が侵入する部分であつてしかも被加熱物10が比
較的高温となる部分、すなわちこの実施例では、
加熱帯7、均熱帯8における下部に複数の噴出孔
13が設けられる。しかも、これらの噴出孔13
は加熱帯7および均熱帯8における下部に設けら
れる。噴出孔13には逆止弁14aを備えるガス
供給管14がそれぞれ接続され、それらのガス供
給管14は管路15に共通に接続される。管路1
5は流量制御弁16および電磁弁17を備え、可
燃性ガス供給源(図示せず)に接続される。この
ようにして各噴出孔13からは天然ガス、都市ガ
ス、液化石油ガスなどの可燃性ガスが炉本体1内
に送入される。
Therefore, in the present invention, a portion where air enters the furnace body 1 from the outside and where the heated object 10 is relatively high temperature, that is, in this embodiment,
A plurality of ejection holes 13 are provided at the lower part of the heating zone 7 and the soaking zone 8. Moreover, these blowholes 13
is provided at the lower part of the heating zone 7 and the soaking zone 8. Gas supply pipes 14 each having a check valve 14a are connected to the ejection holes 13, and these gas supply pipes 14 are commonly connected to a pipe line 15. Conduit 1
5 includes a flow control valve 16 and a solenoid valve 17, and is connected to a combustible gas supply source (not shown). In this way, combustible gas such as natural gas, city gas, liquefied petroleum gas, etc. is fed into the furnace body 1 from each blowout hole 13 .

上述のごとく炉本体1内に可燃性ガスが送入さ
れると、炉本体1内に外部から侵入した空気が存
在したときに前記可燃性ガスが空気中の酸素との
反応によつて燃焼するので、炉本体1内は無酸化
雰囲気となる。しかも各噴出孔13は加熱帯7お
よび均熱帯8に設けられているので、加熱用バー
ナ9の空燃比が多少ずれて過剰空気が存在したと
しても、その過剰空気が前記可燃性ガスとの反応
によつて消費される。なお前記可燃性ガスの燃焼
による発熱は被加熱物10の加熱に利用される。
As described above, when flammable gas is introduced into the furnace body 1, when there is air that has entered the furnace body 1 from the outside, the flammable gas is combusted by reaction with oxygen in the air. Therefore, the inside of the furnace body 1 becomes a non-oxidizing atmosphere. Moreover, since each jet hole 13 is provided in the heating zone 7 and the soaking zone 8, even if the air-fuel ratio of the heating burner 9 deviates slightly and there is excess air, the excess air will react with the combustible gas. consumed by. Note that the heat generated by the combustion of the flammable gas is used to heat the object to be heated 10.

噴出孔13から送入された可燃性ガスの量は、
炉本体1内に酸素が存在しないような量に設定さ
れる。すなわち炉本体1内に侵入した酸素にみあ
う以上に可燃性ガスを送入しなければ、炉本体1
内が無酸化の雰囲気とはならないが、可燃性ガス
を余分に送入すると未燃ガスが発生して排気管1
1から煤が発生することがある。
The amount of combustible gas sent from the nozzle 13 is
The amount is set so that no oxygen exists in the furnace body 1. In other words, unless flammable gas is introduced in excess of the amount of oxygen that has entered the furnace body 1, the furnace body 1
Although the atmosphere inside the exhaust pipe 1 will not be non-oxidizing, if excess flammable gas is introduced, unburned gas will be generated and the exhaust pipe 1
Soot may be generated from 1.

そこで、炉本体1内の雰囲気を最適の無酸化状
態に保つために、炉本体1内の雰囲気ガス中にお
ける一酸化炭素の濃度は検出する検出器18が設
けられる。この検出器18は炉本体1における排
出口3に近接した均熱帯8に設けられ、その一酸
化炭素濃度検出値は制御手段19に入力される。
制御手段19は予め設定された一酸化炭素濃度た
とえば0.5〜1%程度と、検出器18で検出され
た一酸化炭素濃度とを比較し、炉本体1内の一酸
化炭素濃度が設定値に等しくなるように流量制御
弁16の開度を調節する。
Therefore, in order to maintain the atmosphere within the furnace body 1 in an optimal non-oxidizing state, a detector 18 is provided to detect the concentration of carbon monoxide in the atmospheric gas within the furnace body 1. This detector 18 is provided in a soaking zone 8 in the vicinity of the discharge port 3 in the furnace body 1, and its detected carbon monoxide concentration value is inputted to the control means 19.
The control means 19 compares a preset carbon monoxide concentration, for example, about 0.5 to 1%, with the carbon monoxide concentration detected by the detector 18, and determines that the carbon monoxide concentration in the furnace body 1 is equal to the set value. Adjust the opening degree of the flow rate control valve 16 so that

なお、電磁弁17は噴出孔13が設けられた部
分すなわち加熱帯7および均熱帯8における温度
が可燃性ガスの着火温度たとえば約800℃以上と
なつたときに開弁するように設定されている。
The solenoid valve 17 is set to open when the temperature in the portion where the jet hole 13 is provided, that is, in the heating zone 7 and the soaking zone 8, reaches the ignition temperature of the combustible gas, for example, approximately 800° C. or higher. .

排出口3における扉5が開放されたときには、
炉本体1内の圧力が低下し外部から空気が侵入し
て一酸化炭素濃度が低下するが、その一酸化炭素
濃度の低下に応じて流量制御弁16の開度が大と
なり、噴出孔13から噴出される可燃性ガスの流
量が増加して炉本体1内の一酸化炭素濃度が設定
値に保たれる。また扉5が聞じたときには外部か
らの侵入空気量が少なくなるので一酸化炭素濃度
が増大し、それに応じて可燃性ガス流量が減少さ
れる。しかも扉5の開放時において、外部から侵
入する空気は排出口3の下部から侵入するが、噴
出孔13は炉本体1の下部に設けられているので
侵入した空気は可燃性ガスと直ちに反応して消費
される。
When the door 5 at the outlet 3 is opened,
The pressure inside the furnace body 1 decreases, air enters from the outside, and the carbon monoxide concentration decreases, but the opening degree of the flow rate control valve 16 increases in response to the decrease in the carbon monoxide concentration, and air flows from the jet hole 13. The flow rate of the ejected combustible gas increases, and the carbon monoxide concentration within the furnace body 1 is maintained at the set value. Furthermore, when the door 5 is opened, the amount of air entering from the outside decreases, so the carbon monoxide concentration increases, and the flammable gas flow rate decreases accordingly. Moreover, when the door 5 is opened, air entering from the outside enters from the lower part of the exhaust port 3, but since the jet hole 13 is provided at the lower part of the furnace body 1, the incoming air immediately reacts with the flammable gas. consumed.

なお装入口2において、扉4が開放したときに
も炉本体1内に空気が侵入するが、装入口2に近
接して排気管11が設けられており、しかも予熱
帯6においては被加熱物10の温度は比較的低温
であるので、被加熱物10の酸化量は無視しうる
ほど小さい。
At the charging port 2, air also enters the furnace body 1 when the door 4 is opened. Since the temperature 10 is relatively low, the amount of oxidation of the heated object 10 is negligibly small.

以上のように本発明によれば、炉本体1内で加
熱帯7および均熱帯8に噴出孔13が設けられ、
この噴出孔13には、管路15に介在されている
流量制御弁16を介して、一酸化炭素が供給さ
れ、被加熱物10の排出口3付近には一酸化炭素
濃度検出器18が設けられ、この検出器18によ
つて検出器される一酸化炭素濃度が、予め定める
値になるように流量制御弁16の開度が調節され
るので、炉本体内をほぼ無酸化の状態に保つこと
ができ、したがつて被加熱物10の酸化を防止す
ることができる。しかも噴出孔13から噴出され
た可燃性ガスの燃焼熱は、被加熱物10の加熱に
利用されるので省エネルギに資するところが大き
い。
As described above, according to the present invention, the ejection holes 13 are provided in the heating zone 7 and the soaking zone 8 in the furnace body 1,
Carbon monoxide is supplied to this jet hole 13 via a flow rate control valve 16 interposed in a pipe 15, and a carbon monoxide concentration detector 18 is provided near the outlet 3 of the object to be heated 10. The opening degree of the flow rate control valve 16 is adjusted so that the carbon monoxide concentration detected by the detector 18 reaches a predetermined value, so that the inside of the furnace body is maintained in an almost oxidation-free state. Therefore, oxidation of the heated object 10 can be prevented. Furthermore, the combustion heat of the combustible gas ejected from the ejection holes 13 is used to heat the object to be heated 10, which greatly contributes to energy saving.

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

図面は本発明の一実施例の断面図である。 1…炉本体、13…噴出孔、16…流量制御
弁、18…検出器、19…制御手段。
The drawing is a sectional view of one embodiment of the present invention. DESCRIPTION OF SYMBOLS 1...Furnace body, 13...Ejection hole, 16...Flow control valve, 18...Detector, 19...Control means.

Claims (1)

【特許請求の範囲】 1 被加熱物10の搬送方向に沿つて被加熱物1
0の装入口2から排出口3に向けて予熱帯6、加
熱帯7および均熱帯8がこの順序で形成され、前
記装入口2付近には、燃焼排ガスを排出する排気
管11が設けられ、加熱帯7および均熱帯8には
加熱用バーナ9が設けられ、加熱帯7および均熱
帯8には噴出孔13が設けられる炉本体1と、 噴出孔13に可燃性ガスを供給する管路15
と、 管路15に介在される流量制御弁16と、 炉本体1内で前記排出口3に近接した位置に設
けられ、一酸化炭素濃度を検出する一酸化炭素濃
度検出器18と、 前記一酸化炭素濃度検出器18からの出力に応
答し、炉本体1内の一酸化炭素濃度が予め定める
値になるように流量制御弁16の開度を調節する
手段19とを含むことを特徴とする直火式加熱
炉。
[Claims] 1 The object to be heated 1 along the conveyance direction of the object to be heated 10
A preheating zone 6, a heating zone 7, and a soaking zone 8 are formed in this order from the charging port 2 to the discharge port 3, and an exhaust pipe 11 for discharging combustion exhaust gas is provided near the charging port 2. The heating zone 7 and the soaking zone 8 are provided with heating burners 9, and the heating zone 7 and the soaking zone 8 are provided with a furnace body 1 having a jet hole 13, and a pipe line 15 that supplies combustible gas to the jet hole 13.
a flow rate control valve 16 interposed in the pipe line 15; a carbon monoxide concentration detector 18 provided in the furnace body 1 at a position close to the discharge port 3 to detect the carbon monoxide concentration; It is characterized by including means 19 for adjusting the opening degree of the flow rate control valve 16 in response to the output from the carbon oxide concentration detector 18 so that the carbon monoxide concentration in the furnace body 1 becomes a predetermined value. Direct-fire heating furnace.
JP3602281A 1981-03-12 1981-03-12 Direct-firing type heating furnace Granted JPS57149417A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3602281A JPS57149417A (en) 1981-03-12 1981-03-12 Direct-firing type heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3602281A JPS57149417A (en) 1981-03-12 1981-03-12 Direct-firing type heating furnace

Publications (2)

Publication Number Publication Date
JPS57149417A JPS57149417A (en) 1982-09-16
JPS6356288B2 true JPS6356288B2 (en) 1988-11-08

Family

ID=12458094

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3602281A Granted JPS57149417A (en) 1981-03-12 1981-03-12 Direct-firing type heating furnace

Country Status (1)

Country Link
JP (1) JPS57149417A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2683908B2 (en) * 1988-03-31 1997-12-03 同和鉱業株式会社 Atmosphere oxidation prevention method

Also Published As

Publication number Publication date
JPS57149417A (en) 1982-09-16

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