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JPS5952933B2 - Continuous furnace for sequential heat treatment of strip coils - Google Patents
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JPS5952933B2 - Continuous furnace for sequential heat treatment of strip coils - Google Patents

Continuous furnace for sequential heat treatment of strip coils

Info

Publication number
JPS5952933B2
JPS5952933B2 JP14763579A JP14763579A JPS5952933B2 JP S5952933 B2 JPS5952933 B2 JP S5952933B2 JP 14763579 A JP14763579 A JP 14763579A JP 14763579 A JP14763579 A JP 14763579A JP S5952933 B2 JPS5952933 B2 JP S5952933B2
Authority
JP
Japan
Prior art keywords
furnace
gas
matsufuru
heat treatment
temperature region
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
JP14763579A
Other languages
Japanese (ja)
Other versions
JPS5672130A (en
Inventor
公夫 前山
武一 関谷
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.)
JFE Steel Corp
Original Assignee
Kawasaki Steel 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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP14763579A priority Critical patent/JPS5952933B2/en
Publication of JPS5672130A publication Critical patent/JPS5672130A/en
Publication of JPS5952933B2 publication Critical patent/JPS5952933B2/en
Expired 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
    • C21D9/52Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for wires; for strips ; for rods of unlimited length
    • C21D9/54Furnaces for treating strips or wire

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

Description

【発明の詳細な説明】 この発明は、ストリップコイルの逐次熱処理用連続炉に
関し、とくに炉内ガスを適切に処理してその有害作用を
除去した、新規なこの種連続炉を提案しようとするもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a continuous furnace for sequential heat treatment of strip coils, and particularly aims to propose a new continuous furnace of this kind in which the gas in the furnace is appropriately treated to eliminate its harmful effects. It is.

一般に金属とくに鋼の圧延ストリップなかでもけい素鋼
帯のストリップコイルのコイル姿態での熱処理、就中無
酸化雰囲気での焼なましには、N2を含む雰囲気ガスを
用いることが多く、通常はコイルにマツフルをかぶせ、
このマツフルの内部に該雰囲気ガスを供給して、マツフ
ルの外側で電熱ヒータまたはラジアントチューブなどに
よる間接加熱、またときにはガスもしくは液体燃料を用
いる直火式バーナの直接加熱を施す場合もある。
In general, an atmospheric gas containing N2 is often used for heat treatment of rolled strip coils of metals, especially silicon steel strips, in the form of coils, especially annealing in a non-oxidizing atmosphere. Cover with matzuru,
The atmospheric gas is supplied to the inside of the matsufuru, and indirect heating is performed outside the matsufuru using an electric heater or a radiant tube, or sometimes direct heating is performed by a direct-fired burner using gas or liquid fuel.

ここにマツフルの裾には、いわゆるサンドシール、セラ
ミックウールシールなどの施用が一般であって完全な封
止は期し難く、さればといってマツフルの操作、作業性
の面から複雑なシールを用い得ないので、熱処理中にマ
ツフルに供給した雰囲気ガスは裾シールを通り抜けて炉
内に洩出し、その結果高温の炉内は、概ねマツフル内と
同様な雰囲気となり、熱処理雰囲気ガス中に、上記のよ
うにN2を含むとき、炉内ガスが外気に触れて爆発に至
るおそれが、とくに多数のストリップコイルの逐次的な
炉内装入−速進の間に熱処理を進行させる連続炉で殊の
外懸念される。
Here, so-called sand seals, ceramic wool seals, etc. are generally applied to the hem of the matsufuru, and it is difficult to achieve a complete seal. During the heat treatment, the atmosphere gas supplied to the Matsufuru passes through the hem seal and leaks into the furnace. As a result, the high-temperature interior of the furnace becomes an atmosphere similar to that inside the Matsufuru, and the above-mentioned gas is contained in the heat treatment atmosphere gas. When the furnace gas contains N2, there is a risk that the gas inside the furnace will come into contact with the outside air and cause an explosion, which is a particular concern in continuous furnaces where heat treatment proceeds between the sequential insertion and rapid advance of a large number of strip coils into the furnace. be done.

そこで従来は、第1図、第2図に台車式トンネル炉の代
表例で示した連続炉1の人、出側にそれぞれ二重しゃ断
層2,3を設け、それらによるしゃ画室4,5の内部を
、−たん不活性雰囲気たとえばN2ガスと置換するよう
なはん雑な操作が、ストリップコイルの装入、搬出の度
毎に必要であり、また第2図に示したトンネル炉の断面
にあられれているような炉壁を貫通する配管、配線類6
.7のまわり、あるいはさらに二重しゃ断層2.3自体
のシールを確実にするための築炉構造の複雑化がさけら
れなかったのである。
Therefore, in the past, double barrier layers 2 and 3 were provided on the upper and outlet sides of the continuous furnace 1 shown as a typical example of a trolley-type tunnel furnace in Figures 1 and 2, respectively, and the barrier compartments 4 and 5 were A complicated operation such as replacing the inside with an inert atmosphere such as N2 gas is required every time a strip coil is loaded or unloaded. Piping and wiring that penetrate the furnace wall that looks like hail 6
.. In order to ensure the sealing around the double barrier layer 2.3 or even the double barrier layer 2.3 itself, the furnace construction structure had to be complicated.

なお図中8は台車、9はマツフル、10は裾シール、1
1はストリップコイル、12は電熱ヒーター、13は熱
処理雰囲気ガスの供給管、14はその接続の脱着を司る
カプラである。
In the figure, 8 is a trolley, 9 is a matsufuru, 10 is a hem seal, 1
1 is a strip coil, 12 is an electric heater, 13 is a supply pipe for heat treatment atmosphere gas, and 14 is a coupler for connecting and disconnecting the coils.

なお上記したところのほか、N2を含む雰囲気ガスが炉
内に洩出すと、これが炉壁に浸透してその断熱性を害し
、熱効率の低下をもたらす不利も加わるけれどもそれは
ともかくとして、炉内ガスについての上記のシール対策
は、一般に可燃性ガスたとえばCOの如きを熱処理雰囲
気ガスとして用いるときも、その炉外への逸出阻止が、
安全衛生管理の面でも不可欠とされるところから同様に
要請される。
In addition to the above, if atmospheric gas containing N2 leaks into the furnace, it will penetrate the furnace wall and impair its insulation properties, resulting in a reduction in thermal efficiency. The above-mentioned sealing measures generally prevent flammable gases such as CO from escaping out of the furnace, even when using them as the heat treatment atmosphere gas.
This is also requested because it is considered essential in terms of safety and health management.

この点について出願人会社の先行的な開発努力はたとえ
ば、特開昭54−96408号公報に示されるように、
炉中へ予熱空気を導入して炉内ガス中の可燃成分の着火
燃焼をもって無害化を図ることにより、数多くのメリッ
トをもたらしたところで゛ある。
The applicant company's prior development efforts in this regard include, for example, as shown in Japanese Patent Application Laid-Open No. 54-96408.
Numerous benefits have been brought about by introducing preheated air into the furnace and igniting and burning the combustible components in the gas inside the furnace to render it harmless.

この発明は、その成果を踏まえて一層の開発努力を重ね
、とくに炉内の低温域における漏出可燃性ガスの一層適
切、簡便な処理を可能ならしめたものである。
This invention is the result of further development efforts based on the results, and has made it possible to more appropriately and easily treat leaked combustible gas, especially in the low temperature range inside the furnace.

すなわち第1図にaで示した低温域で、とくに可燃性ガ
スを燃焼させようとする場合には、点火装置を不可欠と
し、その失調防止と管理に難点があったのを、とくに有
利に解決するものである。
In other words, especially when attempting to burn flammable gas in the low-temperature region indicated by a in Figure 1, an ignition system is essential, and the difficulty of preventing and managing the ignition system has been solved particularly advantageously. It is something to do.

この発明は、マツフルをかぶせたストリップコイルを、
マツフルの裾シールを施して炉内に順次装入する入側開
口と、炉内の加熱帯より均熱帯を経て冷却帯に送り進め
てから搬出する出側開口と、さらには炉内の高温域と低
温域との中間とに、それぞれしゃ断層をそなえるトンネ
ル炉からなり、炉内で逐次に送り進められるマツフルの
内部に可燃性ガスを含む雰囲気ガスを導入する供給系統
と、マツフルの裾シールを通り抜けて炉内に洩出した該
可燃性ガスを、炉内高温域では完全燃焼させ、また炉内
低温域では燃焼限界未満の濃度に希釈させる、それぞれ
の空気供給系統とを有するストリップコイルの逐次熱処
理用連続炉である。
This invention uses a strip coil covered with Matsufuru.
There is an inlet opening where matsufuru is sealed and sequentially charged into the furnace, an outlet opening where the matsufuru are sent from the heating zone through the soaking zone to the cooling zone and then taken out, and the high temperature area inside the furnace. It consists of a tunnel furnace equipped with a barrier layer between the upper and lower temperature regions, and a supply system that introduces atmospheric gas containing flammable gas into the inside of the Matsufuru that are successively fed through the furnace, and a seal at the bottom of the Matsufuru. A series of strip coils each having an air supply system for completely combusting the flammable gas leaked into the furnace in the high temperature region of the furnace and diluting it to a concentration below the flammability limit in the low temperature region of the furnace. This is a continuous furnace for heat treatment.

この発明の実施において連続炉の高温域に適用する熱源
は、従来どおり電熱ヒーターやラジアントチューブを用
いてもよいが、その少くとも一部としてガスまたは液体
燃料を用いる直火式バーナに代え、とくにその燃焼用空
気を、理論混合比に対し過剰としてこれを高温域の炉内
漏出可燃性ガスの完全燃焼に利用することが可能である
In carrying out this invention, the heat source applied to the high temperature range of the continuous furnace may be an electric heater or a radiant tube as usual, but instead of a direct-fired burner that uses gas or liquid fuel at least in part, It is possible to use the combustion air in excess of the stoichiometric mixture ratio for complete combustion of the flammable gas leaking into the furnace in the high temperature range.

第3図、第4図には、電熱ヒータを熱源に用いた例につ
いてこの発明の実施例を示し、上述先行技術では不可欠
であった二重しゃ断層2,3、従ってしゃ画室4,5を
全廃しこれらに代りそれぞれ単一板状構成のしゃ断層2
’、 3’を、とくに炉内の低温域aを高温域すに対
して区画する中間仕切り用しゃ断層15とともに設け、
また高温域すおよび低温域aのそれぞれの炉底に開口さ
せた空気供給系統16と、同じく炉頂に配設した排気系
統17とを設けた点のほかは第1図、第2図につきさき
にのべた構成とほは゛同様する。
3 and 4 show an embodiment of the present invention in which an electric heater is used as a heat source, and the double barrier layers 2, 3, which are indispensable in the above-mentioned prior art, and therefore the barrier chambers 4, 5 are eliminated. These have been completely abolished and replaced with a single plate-shaped barrier layer 2.
', 3' together with an intermediate partitioning barrier layer 15 that partitions the low-temperature area a from the high-temperature area in the furnace,
1 and 2 except that an air supply system 16 opened at the bottom of the furnace in the high temperature zone and low temperature zone a, and an exhaust system 17 similarly placed at the top of the furnace. The structure is almost the same as the one described above.

第3図で18は排気管、19はスタック、20はファン
である。
In FIG. 3, 18 is an exhaust pipe, 19 is a stack, and 20 is a fan.

なお第5図には、熱処理雰囲気ガスも供給管13から、
各マツフル9内への配管6に対する給気を行う脱着操作
系の一例を示し、可撓管21によりガス元管22に供給
管13を接続し、この供給管13には炉中で所定位置に
停止する台車8から垂下させた配管6のそれぞれに気密
適合するカプラ14を配設するほかその脱着操作のため
に昇降シリンダ23を設け、それによる供給管13の降
下位置で台車8の順送り速進を行わせる。
In addition, in FIG. 5, the heat treatment atmosphere gas is also supplied from the supply pipe 13.
An example of an attachment/detachment operation system for supplying air to the piping 6 into each Matsufuru 9 is shown. A supply pipe 13 is connected to the gas main pipe 22 by a flexible pipe 21, and the supply pipe 13 is connected to a predetermined position in the furnace. A coupler 14 that airtightly fits each of the pipes 6 hanging down from the bogie 8 to be stopped is provided, and an elevating cylinder 23 is provided for the attachment/detachment operation of the coupler. have them do it.

なおこの際の給気停止を司る自閉弁をカプラ14に設け
るを可とする。
Note that the coupler 14 may be provided with a self-closing valve that controls the air supply stop at this time.

空気供給系統16は、゛連続炉1の高温域すと低温域a
とについて個別独立の系統とするを可とするが、空気供
給量についてあとでのべるような分配が可能ならば、共
通の加圧源によってもかまわない。
The air supply system 16 is connected to a high temperature region a and a low temperature region a of the continuous furnace 1.
It is possible to use separate and independent systems for these, but if it is possible to distribute the air supply amount as described later, a common pressurizing source may be used.

かように構成される連続炉の操業は、まず空気供給系統
16から炉内に空気供給を行い、ついで加熱帯、引続き
均熱帯を所定温度に昇温させる準備を経て扉2′を開き
台車8を進めて、マツフル9で囲ったストリップコイル
11を炉内に装入し、マツフル9の内部に可燃性ガスを
含む熱処理雰囲気ガスを導入する熱処理段階を逐次に進
め、高温域すが満たされたのちには中間のしゃ断層15
、さらに低温域aが満され2からは出側しゃ断層3′も
、入側しゃ断層2′と同時に開閉して、次のコイルの装
入と、処理済みコイルの搬出とが同時に行われる。
To operate the continuous furnace configured as described above, air is first supplied into the furnace from the air supply system 16, and then preparations are made to raise the temperature of the heating zone and then the soaking zone to a predetermined temperature, and then the door 2' is opened and the trolley 8 is opened. Then, the strip coil 11 surrounded by Matsufuru 9 is charged into the furnace, and the heat treatment step of introducing a heat treatment atmosphere gas containing flammable gas into the interior of Matsufuru 9 is successively carried out, until the high temperature region is filled. Later, the intermediate barrier layer15
Further, when the low temperature region a is filled, the outlet insulation layer 3' is also opened and closed at the same time as the input insulation layer 2', and the next coil is loaded and the processed coil is taken out at the same time.

この操業中、マツフル9の裾シールを通り抜ケて炉内に
洩出した可燃性ガスは、熱処理温度が一般に760℃以
上であることから、高温域すにおいては、着火温度57
0℃であるH2が雰囲気ガスとして用いられたときも直
ちに燃焼する。
During this operation, the flammable gas that passed through the hem seal of Matsuful 9 and leaked into the furnace had an ignition temperature of 57°C in the high temperature range, since the heat treatment temperature is generally 760°C or higher.
When H2 at 0° C. is used as an atmospheric gas, it also burns immediately.

ここに供給空気量は、N2が燃焼する濃度は、対空気比
率で4〜74%でありそれ故H21m3に対して0.4
〜24m3に定め、燃焼排ガスは、排気系統17から排
気管18を介してスタック19へ放出させる。
The amount of air supplied here is that the concentration of N2 that burns is 4% to 74% of the air ratio, so the amount of air supplied is 0.4% to H21m3.
~24 m3, and the combustion exhaust gas is discharged from the exhaust system 17 to the stack 19 via the exhaust pipe 18.

冷却帯つまり低温域a内でマツフル9の裾から洩出しな
N2ガスは、空気供給系16からとくに大量に送られる
空気によって燃焼の下限界である4%以下に希釈し、燃
焼することなく排気系統17からスタック19を経て大
気中へ放出する。
The N2 gas leaking from the hem of the Matsuful 9 in the cooling zone, that is, the low-temperature area a, is diluted to 4% or less, which is the lower limit of combustion, by a particularly large amount of air sent from the air supply system 16, and is exhausted without being combusted. It is discharged from the system 17 through the stack 19 into the atmosphere.

この場合炉内低温域へ吹き込まれる空気量はN2ガス1
m”に対して24m3以上が必要である。
In this case, the amount of air blown into the low temperature area inside the furnace is N2 gas 1
m” requires 24 m3 or more.

その後、同様にして被焼鈍材を順次炉内へ装入して炉内
の加熱域す及び冷却域aを通過させた後、出側しゃ断扉
3′から炉外へ取り出して焼鈍を終了する。
Thereafter, in the same manner, the materials to be annealed are sequentially charged into the furnace and passed through the heating zone and the cooling zone a in the furnace, and then taken out from the furnace through the outlet shutoff door 3' to complete the annealing.

炉内に洩出しなN2ガスを完全に処理する場合に、この
発明の方式を用いれば特に複雑な炉制御は必要としない
If the method of the present invention is used to completely treat N2 gas leaking into the furnace, no particularly complicated furnace control is required.

即ち、マツフル内に供給されるN2ガス量はマツフル1
個につき0.5〜8m3/hの範囲で供給する場合には
高温域すにおいてはマツフル1個当り供給空気量2〜1
2m・/hの範囲にあればN2の燃焼範囲4〜74%に
入るのでファン20は定吐出量でよい。
In other words, the amount of N2 gas supplied into Matsufuru is
When supplying air in the range of 0.5 to 8 m3/h per piece, in high temperature range, the amount of air supplied per piece of Matsufuru is 2 to 1.
If it is in the range of 2 m/h, it falls within the combustion range of N2 of 4 to 74%, so the fan 20 may have a constant discharge rate.

すなわちN2ガス供給量が0.5〜5.11=/hの範
囲で変化しても供給空気量が2〜12m3/hの範囲内
の値であれば次のように必ず4〜74%という範囲に入
る。
In other words, even if the N2 gas supply amount changes in the range of 0.5 to 5.11 = /h, if the supplied air amount is within the range of 2 to 12 m3/h, it will always be 4 to 74% as shown below. fall within range.

N2:0.5m3/h時、必要空気量:Xとおくと、ま
た低温域aではマツフル1個当り供給空気量を120m
”/h以上であればやはり定吐出量のファンでよい。
When N2: 0.5m3/h, the required air volume is set as
”/h or more, a fan with a constant discharge amount may be used.

つまり燃焼しない範囲にN2ガスを希釈するには、N2
濃度を4%以下にしたら良い。
In other words, in order to dilute N2 gas to a range where it will not burn, N2
It is best to keep the concentration below 4%.

従ってN2供給量が最大である時の希釈空気量があれば
、それ以下のN2ガス量については十分である。
Therefore, the amount of dilution air when the amount of N2 supplied is at its maximum is sufficient for the amount of N2 gas below that amount.

すなわち0.5〜5 m”/hという供給N2量に対し
ては、 が供給空気量の下限である。
That is, for a supplied N2 quantity of 0.5 to 5 m"/h, the lower limit of the supplied air quantity is:

この値以上のファンであれば一定量のファンで必要、十
分な空気を炉内へ送給できる。
If the fan is above this value, a certain amount of fan can feed the necessary and sufficient air into the furnace.

従って両ファン20は、予備機を併設し、停電時の電源
としてジーゼル発電機を常備しておく程度の安全対策で
足りる。
Therefore, safety measures such as providing a backup unit for both fans 20 and always having a diesel generator on hand as a power source in case of a power outage are sufficient.

以上にの発明の実施例を直通したトンネル炉からなる連
続炉について説明したが、回転炉床型の連続炉について
も同様の方法で応用できるのはいうまでもない。
Although the above embodiments of the invention have been described with respect to a continuous furnace consisting of a direct tunnel furnace, it goes without saying that the same method can be applied to a rotary hearth type continuous furnace.

念のため、回転炉床8′を用いた連続炉を第6図に示し
すでにのべたところと同一の構成に共通の番号記号を付
したところから作用効果は容易に理解されよう。
For the sake of clarity, a continuous furnace using a rotary hearth 8' is shown in FIG. 6, with common numbers and symbols attached to the same structures as those already described, so that the operation and effect will be easily understood.

■ 従来炉においては、マツフルから炉内へ洩出しなN
2など可燃性ガスを空気と接触させぬため、連続炉の入
口、出口に炉内と開閉自在な二重のしゃ断扉で区画され
た入口室、出口室を必要とし、これら各室にN2等の不
活性ガスを多量に必要とし、これら入口室、或いは出口
室と炉内を区画する開閉扉部の外気とのシール或いは、
炉内温度測定用カップル、雰囲気ガス、供給ガス管等炉
外から炉内へ貫通している配管配線などのシールが複雑
な構造となっていたのに対してこの発明の方式によれば
炉構造が極めて簡単となる。
■ In conventional furnaces, N leaks from the Matsufuru into the furnace.
In order to prevent combustible gases such as 2 from coming into contact with air, the inlet and outlet of a continuous furnace are separated from the inside of the furnace by double shutoff doors that can be opened and closed, and each of these rooms is equipped with N2, etc. A large amount of inert gas is required, and sealing between the inlet chamber or the outlet chamber and the opening/closing door that separates the inside of the furnace from the outside air, or
Whereas seals for piping and wiring penetrating from outside the furnace to the inside of the furnace, such as couples for measuring furnace temperature, atmospheric gas, and supply gas pipes, had a complicated structure, the method of the present invention reduces the furnace structure. becomes extremely simple.

■ N2雰囲気中での断熱材の熱伝導率は空気中または
燃焼ガス中のそれより非常に高く、2〜2.7倍にも達
して炉体からの放散熱が大きくなるがこの発明でN2を
雰囲気ガスを用いたときでもこの炉内での停滞なく、従
って熱効率の改善に大きく寄与する。
■ The thermal conductivity of a heat insulating material in an N2 atmosphere is much higher than that in air or combustion gas, reaching 2 to 2.7 times, increasing the heat radiated from the furnace body. Even when atmospheric gas is used, there is no stagnation in the furnace, which greatly contributes to improving thermal efficiency.

■ N2ガス燃焼によって2.572kcal/ms
−N2の熱量を炉温上昇に利用できるから、炉の加熱の
ためにCガス使用の場合に、N2ガス1 m”に対して
約0.6m”のCガス節減、また灯油使用の場合でもN
2ガス1m”に対して約0.31の節減につながりその
他電熱ヒーターやラジアントチューブによる場合には更
に著しい省エネルギー効果がある。
■ 2.572kcal/ms by N2 gas combustion
- Since the calorific value of N2 can be used to raise the furnace temperature, when using C gas to heat the furnace, you can save approximately 0.6 m'' of C gas for 1 m'' of N2 gas, and even when using kerosene. N
This leads to an energy saving of approximately 0.31 for 1 m'' of 2 gases, and an even more significant energy saving effect is achieved when using electric heaters or radiant tubes.

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

第1図は従来の金属ストリップコイルの連続式雰囲気熱
処理装置の一例の縦断面図、第2図はその横断面図、第
3図はこの発明による連続熱処理装置の縦断面図、第4
図は横断面図、第5図は雰囲気ガスの供給配管系統を示
す説明図であり、第6図は回転炉床型連続炉の平面配置
図である。 1・・・・・・連続炉、2’、 3’・・・・・・人
出側各開口のしや断層、6・・・・・・配管、9・・・
・・・マツフル、10・・・・・・裾シール、15・・
・・・・中間しゃ断層、13・・・・・・雰囲気ガス供
給管、16・・・・・・空気供給系統。
FIG. 1 is a longitudinal cross-sectional view of an example of a conventional continuous atmosphere heat treatment apparatus for metal strip coils, FIG. 2 is a cross-sectional view thereof, FIG. 3 is a longitudinal cross-section of a continuous heat treatment apparatus according to the present invention, and FIG.
The figure is a cross-sectional view, FIG. 5 is an explanatory diagram showing an atmospheric gas supply piping system, and FIG. 6 is a plan layout diagram of a rotary hearth type continuous furnace. 1...Continuous furnace, 2', 3'...Shiya fault at each opening on the exit side, 6...Piping, 9...
...Matsuful, 10...Hem sticker, 15...
. . . Intermediate isolation layer, 13 . . . Atmosphere gas supply pipe, 16 . . . Air supply system.

Claims (1)

【特許請求の範囲】[Claims] 1 マツフルをかぶせたストリップコイルを、マツフル
の裾シールを施して炉内に順次装入する入側開口と、炉
内の加熱帯より均熱帯を経て冷却帯に送り進めてから搬
出する出側開口と、さらには炉内の高温域と低温域との
中間とに、それぞれしゃ断層をそなえるトンネル炉から
なり、炉内で逐次に送り進められるマツフルの内部に可
燃性ガスを含む雰囲気ガスを導入する供給系統と、マツ
フルの裾シールを通り抜けて炉内に洩出した該可燃性ガ
スを炉内高温域では、完全燃焼させ、また炉内低温域で
は燃焼限界未満の濃度に希釈させるそれぞれの空気供給
系統とを有することを特徴とするストリップコイルの逐
次熱処理用連続炉。
1 An entry opening where strip coils covered with Matsufuru are sequentially charged into the furnace with a Matsufuru hem seal applied, and an exit opening where the strip coils are sent from the heating zone in the furnace through the soaking zone to the cooling zone and then taken out. The furnace consists of a tunnel furnace that is equipped with a barrier layer between the high-temperature region and the low-temperature region in the furnace, and an atmospheric gas containing flammable gas is introduced into the matsufuru, which are successively fed through the furnace. Air supply system that completely burns the combustible gas leaked into the furnace through the supply system and the Matsufuru hem seal in the high-temperature region of the furnace, and dilutes it to a concentration below the flammability limit in the low-temperature region of the furnace. A continuous furnace for sequential heat treatment of strip coils, characterized in that it has a system.
JP14763579A 1979-11-16 1979-11-16 Continuous furnace for sequential heat treatment of strip coils Expired JPS5952933B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14763579A JPS5952933B2 (en) 1979-11-16 1979-11-16 Continuous furnace for sequential heat treatment of strip coils

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14763579A JPS5952933B2 (en) 1979-11-16 1979-11-16 Continuous furnace for sequential heat treatment of strip coils

Publications (2)

Publication Number Publication Date
JPS5672130A JPS5672130A (en) 1981-06-16
JPS5952933B2 true JPS5952933B2 (en) 1984-12-22

Family

ID=15434784

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14763579A Expired JPS5952933B2 (en) 1979-11-16 1979-11-16 Continuous furnace for sequential heat treatment of strip coils

Country Status (1)

Country Link
JP (1) JPS5952933B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH026015U (en) * 1988-06-28 1990-01-16

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4406618A (en) * 1980-12-19 1983-09-27 Kawasaki Steel Corporation Method of operating continuous heat treatment furnace for metal strip coils

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH026015U (en) * 1988-06-28 1990-01-16

Also Published As

Publication number Publication date
JPS5672130A (en) 1981-06-16

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