JPH04116127A - Bright annealing furnace - Google Patents

Bright annealing furnace

Info

Publication number
JPH04116127A
JPH04116127A JP23253090A JP23253090A JPH04116127A JP H04116127 A JPH04116127 A JP H04116127A JP 23253090 A JP23253090 A JP 23253090A JP 23253090 A JP23253090 A JP 23253090A JP H04116127 A JPH04116127 A JP H04116127A
Authority
JP
Japan
Prior art keywords
furnace
gas
ventilation
wall
shell
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
JP23253090A
Other languages
Japanese (ja)
Other versions
JP2567140B2 (en
Inventor
Yunosuke Uda
宇田 勇之助
Tadashi Yamamoto
忠 山本
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.)
Chugai Ro Co Ltd
Nippon Yakin Kogyo Co Ltd
Original Assignee
Chugai Ro Co Ltd
Nippon Yakin Kogyo 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 Chugai Ro Co Ltd, Nippon Yakin Kogyo Co Ltd filed Critical Chugai Ro Co Ltd
Priority to JP2232530A priority Critical patent/JP2567140B2/en
Publication of JPH04116127A publication Critical patent/JPH04116127A/en
Application granted granted Critical
Publication of JP2567140B2 publication Critical patent/JP2567140B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

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

Abstract

PURPOSE:To shorten the standby time in the start and resumption of operation without decreasing heat efficiency by providing an air pipe having many air ports opened toward the shell in a gap between the lining refractory and shell. CONSTITUTION:A metallic thin strip 1 is continuously traveled in an airtight furnace consisting of a heating zone 2 provided with a heating element 8 and a cooling zone 3, directly heated in a reducing atmosphere and then cooled. In this bright annealing furnace, slit air passage gaps 38 are provided in plural lines in the boundary between the lining refractory 11 of the furnace wall and the shell 14. An air pipe 39 is set in the gap 38. The pipe 39 is detained on the inner wall of the shell 14 by a fixture 47 and pierced with many air ports 39a opened toward the shell 14. The gas in the furnace is sucked from the air port 39a and discharged outside the furnace through the pipe 39, and the gas is freed of impurities outside the furnace, purified and recirculated into the furnace. Consequently, the standby time in the start and resumption of operation is reduced without decreasing heat efficiency.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、光輝焼鈍炉に関し、とくに新設炉の操業開始
時および補修後の再開時における立上げ所要時間(シー
ズニング時間)の大幅な短縮を可能ならしめた縦型およ
び横型の連続光輝焼鈍炉である。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a bright annealing furnace, and in particular significantly shortens the start-up time (seasoning time) at the start of operation of a newly installed furnace and at the time of restarting after repair. This is a vertical and horizontal continuous bright annealing furnace that has been made possible.

〔従来の技術〕[Conventional technology]

鉄、ニッケル、クロム、コバルト、アルミニウム、チタ
ン、銅、亜鉛および錫ならびにそれらの合金薄帯の製造
に際しては、冷間圧延後の表面性状を保持したまま材質
の改善を図る目的で、いわゆる光輝焼鈍が施される。
When manufacturing iron, nickel, chromium, cobalt, aluminum, titanium, copper, zinc, tin, and their alloy ribbons, so-called bright annealing is used to improve the material quality while maintaining the surface quality after cold rolling. will be applied.

かような光輝焼鈍に際しては、焼鈍中に酸化が生じない
ように、炉内を還元性雰囲気に保持しておくことが重要
である。炉内が完全に還元性の雰囲気になっているかど
うかは、通常、炉内ガスの水蒸気の露点を測定すること
によって知ることができる。
In such bright annealing, it is important to maintain the inside of the furnace in a reducing atmosphere so that oxidation does not occur during the annealing. Whether the inside of the furnace has a completely reducing atmosphere can usually be determined by measuring the dew point of the water vapor in the furnace gas.

ところで、例えばステンレス鋼の光輝焼鈍は、800〜
1200°C程度の高温で行う必要があることから、焼
鈍炉、例えば直火型の焼鈍炉としては、炉内壁を耐火物
で内張すするとともに、炉外壁を鉄皮で覆って炉内を気
密に保持した構造になる炉が用いられる。このような構
造にかかる炉は、炉内に導入した薄帯を、同じく炉内に
設置した電熱ヒータやラジアントチューブなどの発熱体
および耐火れんがからの輻射熱によって加熱するしくみ
になっている。
By the way, for example, bright annealing of stainless steel is 800~
Since it is necessary to carry out the annealing at a high temperature of about 1200°C, annealing furnaces, such as direct-fired annealing furnaces, are lined with refractories on the inner walls of the furnace, and the outer walls of the furnace are covered with iron skin to protect the inside of the furnace. A furnace with an airtight structure is used. A furnace having such a structure is designed to heat the ribbon introduced into the furnace by radiant heat from a heating element such as an electric heater or a radiant tube and refractory bricks also installed in the furnace.

しかしながら、このような構造の焼鈍炉では、炉を新設
した場合、および補修のために炉を一旦開放して大気に
さらした場合に、大気中の水分及び酸素、炭酸ガス等が
耐火れんが内に浸入する。
However, in an annealing furnace with such a structure, when a new furnace is installed, or when the furnace is once opened and exposed to the atmosphere for repairs, moisture, oxygen, carbon dioxide, etc. in the atmosphere can enter the refractory bricks. Infiltrate.

そのために、焼鈍処理開始または再開後に、炉内を還元
性雰囲気とするまでに長時間が必要であった。
Therefore, after starting or restarting the annealing process, a long time was required to create a reducing atmosphere in the furnace.

すなわち、炉内のれんが内部に水分等が浸入している場
合、直ちに高温になる炉内壁側は比較的早い時期に脱水
及び脱気が起る。しかしながら、炉壁の中間層から鉄皮
側(外層部)に位置するものは、温度勾配の関係から結
晶水の分解温度に近い部分では不安定で、沸点や結晶水
の分解温度に到達せず、脱水に長時間を要し、そのた゛
めに長時間、炉内を還元性雰囲気にできなかったのであ
る。
That is, if moisture or the like has entered the bricks in the furnace, dehydration and deaeration occur relatively quickly on the inner wall side of the furnace, which immediately becomes hot. However, those located from the middle layer of the furnace wall to the shell side (outer layer) are unstable near the decomposition temperature of crystallized water due to the temperature gradient, and do not reach the boiling point or the decomposition temperature of crystallized water. However, dehydration took a long time, and therefore it was not possible to maintain a reducing atmosphere in the furnace for a long period of time.

そこでもし、充分な脱水を行わず、充分な還元性雰囲気
にならないままに炉操業を実施した場合、耐火れんが内
の残留水分が徐々に炉内に出てくるので露点が下がらず
、従って、例えばステンレス鋼のような反応性に冨む金
属(Cr、 Mn、 Alなど)を含む薄帯を焼鈍しよ
うとしても、所期した光輝焼鈍ができない。結局、従来
は満足いく低露点での光輝焼鈍を行うには、1ケ月から
2ケ月の長時間のシーズニングを余儀なくされていたの
である。
Therefore, if the furnace is operated without sufficient dehydration and without creating a sufficiently reducing atmosphere, the residual moisture in the refractory bricks will gradually come out into the furnace, and the dew point will not drop, resulting in, for example, Even if an attempt is made to anneal a ribbon containing highly reactive metals (Cr, Mn, Al, etc.) such as stainless steel, the desired bright annealing cannot be achieved. As a result, conventionally, in order to perform bright annealing at a satisfactory low dew point, a long seasoning period of one to two months was required.

ところで、上記の問題を解決するものとして、従来、第
5図に示したような、マツフル24と呼ばれる耐熱鋼製
の円筒を炉内に装入し、このマツフル24内を清浄ガス
(還元性ガス)で充填して、発熱体からの輻射熱はマツ
フル24を介して薄帯に伝達する間接加熱方式の炉が提
案された。
By the way, in order to solve the above problem, conventionally, a cylinder made of heat-resistant steel called Matsufuru 24 as shown in FIG. ) was proposed, and an indirect heating type furnace was proposed in which the radiant heat from the heating element was transmitted to the ribbon through the matsufuru 24.

このような構造の焼鈍炉は、炉操業の開始および再開時
であっても、マツフル24内の雰囲気ガスを完全に置換
すれば、露点を容易に低下させることはできるけれども
、 i)マツフルとして高価な耐熱鋼を必要とする、11)
マツフルが熱による変形を起こしやすく、寿命が短いた
め、定期的な修理または取り替えが頻繁に必要となる、 iii )間接加熱方式であるため、熱効率が悪く、同
一能力では炉長が長くなる、 などの欠点があるため、小型炉ではともがく、大型炉で
は実際の使用に供することはできながった。
In an annealing furnace with such a structure, the dew point can be easily lowered by completely replacing the atmospheric gas in the Matsufuru 24 even at the start and restart of furnace operation; 11)
Matsufuru is easily deformed by heat and has a short lifespan, requiring frequent periodic repairs or replacement; iii) Since it is an indirect heating method, thermal efficiency is poor and the length of the furnace is long for the same capacity. Due to these drawbacks, small reactors struggled and large reactors could not be put to practical use.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

そこで、本発明者は、上述のような従来技術が抱える問
題点、すなわち、新設時および再開時における炉内雰囲
気調整と立上げの時間かがかりすぎることや、さらには
大型炉への適用が困難なことなどが解消できる連続光輝
焼鈍炉の開発を目指して鋭意研究を行った。
Therefore, the inventor of the present invention solved the problems of the conventional technology as described above, namely, that it takes too much time to adjust the atmosphere inside the furnace and start up the furnace at the time of new construction and restart, and furthermore, it is difficult to apply it to large furnaces. We conducted intensive research with the aim of developing a continuous bright annealing furnace that would solve these problems.

その結果、炉内が早期に還元性雰囲気にならない原因は
、鉄皮近くの低温耐火れんが部に滞留した水分や酸素が
、長時間にわたって炉内に浸出してくることにあること
が判った。従って、かような水分や酸素を、早期に、積
極的に炉外に排出し、正常な雰囲気ガスと置換すること
ができれば、新設時および再開時における炉内雰囲気(
還元性雰囲気)の早期の実現が果たせるわけである。
As a result, it was found that the reason why the inside of the furnace did not quickly become a reducing atmosphere was that the moisture and oxygen that had accumulated in the low-temperature refractory bricks near the steel shell leached into the furnace over a long period of time. Therefore, if such moisture and oxygen can be actively discharged outside the furnace at an early stage and replaced with normal atmospheric gas, the atmosphere inside the furnace (
This allows for the early realization of a reducing atmosphere.

本発明者は、上記の観点に立脚して数多くの実験と検討
を加えた末に、先に特願平2−115740号として、
かような要請に応えられる新規な光輝焼鈍炉を開発した
After numerous experiments and studies based on the above viewpoint, the present inventor previously published Japanese Patent Application No. 2-115740.
We have developed a new bright annealing furnace that can meet these demands.

この焼鈍炉の構成の特徴は、炉壁の内張り耐火物中に、
通気用条孔を複数列設けると共に、この通気用条孔内に
、周面に多数の吸引口を開口した吸引パイプを配設し、
炉内で生成するガス(内張り中に滞留する不純ガス)を
この吸引パイプを通じて炉外に積極的に排出するように
したことにある。そして、吸引した炉内(雰囲気)ガス
中の不純物を除去したのちの清浄化(還元性)ガスは、
循環装置を介して再び、炉内に炉内ガスとして供給する
ようにした光輝焼鈍炉を提案した。
The structure of this annealing furnace is characterized by:
A plurality of rows of ventilation holes are provided, and a suction pipe with a large number of suction ports opened on the circumferential surface is arranged within the ventilation holes,
The reason is that the gas generated inside the furnace (impure gas that remains in the lining) is actively discharged outside the furnace through this suction pipe. After removing impurities from the sucked furnace (atmosphere) gas, the cleaning (reducing) gas is
We have proposed a bright annealing furnace in which the gas is supplied back into the furnace as in-furnace gas through a circulation device.

ところが、上記提案にかかる光輝焼鈍炉は、炉内ガス吸
引能力の面でなお改善すべき点が残されており、また、
吸引パイプを耐火物中に埋設するとはいえ、どちらかと
いうと炉内に近いために保護に欠けるという課題もあっ
た。
However, the bright annealing furnace proposed above still has some points to be improved in terms of gas suction capacity in the furnace, and
Although the suction pipe was buried in refractory material, there was also the problem that it lacked protection because it was rather close to the inside of the furnace.

そこで、本発明では、先行提案にかかる前記光輝焼鈍炉
の機能をより一層向上させることを目的として以下に述
べるような光輝焼鈍炉を開発した。
Therefore, in the present invention, a bright annealing furnace as described below was developed for the purpose of further improving the functions of the bright annealing furnace proposed previously.

[課題を解決するための手段] 上掲の目的に適合する新規な光輝焼鈍炉として、本発明
は、 外壁鉄皮の内側に、耐火物の内張りを設けて構成される
炉壁を有し、内部が主として加熱帯とそれの下流側に連
設された冷却帯とからなる気密式の炉であって、前記加
熱帯から連続的に導入される金属薄帯を、還元性雰囲気
にて直接的に加熱し引続き冷却する形式の焼鈍炉におい
て、 前記炉壁の内張り耐火物と外壁鉄皮との境界部に、条孔
状の通気間隙を複数列に亘って設け、これらの通気間隙
内には、周面の鉄皮側に向けて多数の通気口を開口させ
てなる通気パイプを配設すると共に、この通気パイプを
前記鉄皮の内面に係止したことを特徴とする光輝焼鈍炉
、 を提案する。
[Means for Solving the Problems] As a novel bright annealing furnace that meets the above objectives, the present invention has a furnace wall configured by providing a refractory lining inside an outer wall iron skin, It is an airtight furnace whose interior mainly consists of a heating zone and a cooling zone connected downstream of the heating zone, in which the metal ribbon continuously introduced from the heating zone is directly heated in a reducing atmosphere. In an annealing furnace that heats to a temperature and then cools, a plurality of rows of strip-shaped ventilation gaps are provided at the boundary between the refractory lining of the furnace wall and the outer wall steel, and in these ventilation gaps, A bright annealing furnace, characterized in that a ventilation pipe having a large number of vents opening toward the iron skin side of the peripheral surface is disposed, and the ventilation pipe is locked to the inner surface of the iron skin. suggest.

そして、本発明の別の光輝焼鈍炉は、上記の構成に加え
て、炉内ガスを前記通気パイプを通じて炉外に排出する
ようにしてなり、かつ炉外には、吸引排出した前記ガス
中の不純物成分を除去して清浄化したのち、炉内に再供
給する炉内ガスの循環装置を付帯して設けたものである
In addition to the above configuration, another bright annealing furnace of the present invention is configured such that the gas inside the furnace is discharged to the outside of the furnace through the ventilation pipe, and the gas in the suctioned and discharged gas is discharged to the outside of the furnace. A furnace gas circulation device is attached to the furnace to remove impurity components and clean it, and then re-supply the gas into the furnace.

[作 用] さて、新しく築炉する場合、れんがの接合に当ってはモ
ルタルが使用される。ここに、炉内壁の高温部は、モル
タル内の結晶水が早い時期に分解するので容易に炉外に
放出されるけれども、炉外壁近傍ではなかなか分解温度
(通常350〜600°C)に到達せず、操業温度およ
び時間に応じて徐々に分解し、これが操業中受しづつ炉
内に侵入してくるために、炉内の露点は下がりにくかっ
た。
[Function] When building a new furnace, mortar is used to join the bricks. Here, in the high-temperature part of the furnace inner wall, the crystallized water in the mortar decomposes at an early stage and is easily released outside the furnace, but in the vicinity of the furnace outer wall it is difficult to reach the decomposition temperature (usually 350 to 600°C). First, it gradually decomposes depending on the operating temperature and time, and as this decomposes gradually enters the furnace during operation, the dew point inside the furnace is difficult to lower.

また、長時間の処理によって完全に乾燥した炉であって
も、操業中、被処理材から微量ではあるが、マンガンや
ボロンなどの揮発し易い金属成分が蒸気となって雰囲気
ガス中を拡散し、これが炉壁の凝結温度に近い所(主に
耐火れんがの目地や裏側)に晶出し付着する。従って゛
、保守のために炉を開放したとき、これらの金属成分が
大気中の水や酸素と反応して結晶水をもった金属酸化物
となり、しかもかかる金属酸化物の付着個所は比較的低
温部であるため、操業再開時に結晶水の分解に長時間を
要していた。
In addition, even in a furnace that has been completely dried through long-term processing, volatile metal components such as manganese and boron can become vapor and diffuse in the atmospheric gas, albeit in trace amounts, from the material to be treated during operation. This crystallizes and adheres to the furnace walls near the condensation temperature (mainly at the joints and back sides of refractory bricks). Therefore, when the furnace is opened for maintenance, these metal components react with water and oxygen in the atmosphere to form metal oxides with water of crystallization, and the locations where these metal oxides adhere are at relatively low temperatures. Because of this, it took a long time to decompose the crystal water when restarting operations.

上記の解決策として、従来は第5図に示したような、被
処理材1と発熱部との間に耐熱鋼製のマツフル24を配
設した間接加熱方式の焼鈍炉が提案されたわけであるが
、かような焼鈍炉には種々の問題が残されていることは
前述したとおりである。
As a solution to the above problem, an indirect heating type annealing furnace has been proposed in which a heat-resistant steel Matsufuru 24 is disposed between the workpiece 1 and the heat generating part, as shown in Fig. 5. However, as mentioned above, such annealing furnaces still have various problems.

そこで本発明では、上記した直火方式焼鈍炉の問題を解
決するため、第3図(a)に示すように、炉内雰囲気ガ
スの吸引排出のために、鉄皮と内張り耐火物との境界部
分に、炉内雰囲気ガス吸引のための通気用間隙、その間
隙内に配設する吸引口つき吸引パイプおよび排出口から
なるガス排出構造を、炉体のとくに加熱帯に設けること
にしたのである。かようなガス吸引排出構造、とくに通
気用の間隙、吸引パイプ内に流入した炉内雰囲気ガスを
、排出口を通じて、炉外に速やかに吸引排出するように
すれば、たとえ鉄皮近傍耐火物中の低渦部で結晶水が分
解したとしても、発生した水分は前記ガス吸引排出構造
を通じて雰囲気ガスとともに炉外に排出できるので、炉
内に侵入して炉操業に悪影響を及ぼすことがなくなるの
である。
Therefore, in the present invention, in order to solve the problem of the above-mentioned direct-fire annealing furnace, as shown in FIG. We decided to install a gas exhaust structure in the furnace body, especially in the heating zone, consisting of a ventilation gap for suctioning gas from the furnace atmosphere, a suction pipe with a suction port disposed within the gap, and a discharge port. . In such a gas suction and discharge structure, in particular, if the furnace atmosphere gas that has flowed into the ventilation gap or suction pipe is quickly sucked and discharged outside the furnace through the exhaust port, even if the gas inside the refractory near the steel shell is Even if the crystal water decomposes in the low vortex section of the furnace, the generated water can be discharged to the outside of the furnace along with the atmospheric gas through the gas suction and discharge structure, so it will not enter the furnace and adversely affect the furnace operation. .

このような構成にしたことによって本発明は、炉内で生
成したガスを吸引負荷の少ない状態で効率よく吸引排出
でき、そのために、上述した従来技術の欠点を有利に解
決することができる他、それによって炉内温度を均一に
分布させ得るという波及効果も生まれる。
With such a configuration, the present invention can efficiently suck and discharge the gas generated in the furnace with a small suction load, and therefore can advantageously solve the above-mentioned drawbacks of the prior art. This also creates the ripple effect of uniformly distributing the temperature inside the furnace.

[実施例] 以下、この発明の好適実施例を詳しく説明する。[Example] Preferred embodiments of the present invention will be described in detail below.

第1図は、本発明における継型連続光輝焼鈍炉の好適例
を模式的に示すものである。図中の符号1は被処理材で
ある金属薄帯、2は加熱帯、3は冷却帯であって、これ
らで連続光輝焼鈍炉を構成し、金属薄帯1は、炉入口の
シール部4を通って気密に保持された炉内に導入され、
加熱帯2および冷却帯3を搬送される間に所定の熱処理
が施されたのち、炉出口シール部5から炉外に導出され
るしくみになっている。なお、6はガスクーラー7はブ
ロワ−である。
FIG. 1 schematically shows a preferred example of the continuous bright annealing furnace of the present invention. In the figure, reference numeral 1 is a metal ribbon which is the material to be processed, 2 is a heating zone, and 3 is a cooling zone, which constitute a continuous bright annealing furnace. is introduced into the furnace which is kept airtight through the
After being subjected to a predetermined heat treatment while being conveyed through the heating zone 2 and the cooling zone 3, it is led out of the furnace from the furnace outlet seal portion 5. In addition, 6 is a gas cooler 7 is a blower.

第3図(a)は、加熱帯域における炉壁部の拡大図であ
り、同図のB−B矢視面を(b)図として示す。図に符
号8として示すものは、電熱ヒータからなる発熱体でっ
て、給電部材9から通電し、投入電力量の加減により、
炉内の温度を調節するものである。10は電熱ヒータの
支持金具である。そして、炉壁を構成している内張りは
、図示の符号11、12として示す耐火断熱れんがと、
キャスタブルを好適例とする保温材工3からなり、外壁
は鉄皮14で構成されている。
FIG. 3(a) is an enlarged view of the furnace wall in the heating zone, and FIG. 3(b) is a view taken along line B--B in the figure. What is indicated by reference numeral 8 in the figure is a heating element consisting of an electric heater, which is energized from the power supply member 9, and depending on the input power amount,
This is to adjust the temperature inside the furnace. 10 is a support metal fitting for the electric heater. The lining that makes up the furnace wall is made of fireproof and insulating bricks shown as 11 and 12 in the diagram.
It consists of a heat insulating material 3 preferably made of castable material, and the outer wall is made of an iron skin 14.

本発明においては、第3図(a) 、 (d)に示すよ
うに鉄皮14と前記内張り、とくに鉄皮14と耐火断熱
れんが12との間、すなわち、鉄皮14に接する保温材
13を欠設することによって得られる条孔状の通気間隙
38を、特に横型の例で言えば、炉殻の上部を中心とし
て炉室を取り囲むように複数列に亘って設けてあり、か
つこの鉄皮14に隣接して欠設された通気間隙38内に
は、炉内ガス吸引のため、または還流ガスの炉内への吐
出に用いる金属製の通気パイプ39を遊挿配設する。
In the present invention, as shown in FIGS. 3(a) and 3(d), a heat insulating material 13 is provided between the steel shell 14 and the lining, particularly between the steel shell 14 and the refractory insulation bricks 12, that is, in contact with the steel shell 14. In particular, in the case of a horizontal type, the ventilation gaps 38 in the form of strips obtained by cutting holes are provided in multiple rows so as to surround the furnace chamber with the upper part of the furnace shell as the center. A metal ventilation pipe 39 is loosely inserted into the ventilation gap 38 adjacent to the ventilation gap 38, which is used for suction of gas in the furnace or for discharging reflux gas into the furnace.

上記通気パイプ39を通気間隙38内の鉄皮14内面に
沿って固定する方法としては、第3図(d)に示すよう
に、クリプバンド状の固定金具47を介して鉄皮14に
直接取付ける方法などが好適である。それは、通気パイ
プ39の温度差による伸縮を吸収できる状態で取付けな
ければならないからである。
As a method for fixing the ventilation pipe 39 along the inner surface of the steel shell 14 within the ventilation gap 38, as shown in FIG. etc. are suitable. This is because the ventilation pipe 39 must be installed in a state that can absorb expansion and contraction due to temperature differences.

さて、本発明においては、炉の加熱帯2の炉壁構造を、
上述のように、鉄皮14に接する部分に多数の通気間隙
38と通気パイプ39を列設したことにより、第1に、
この加熱帯域2の炉内雰囲気中で生成した反応ガスの吸
引排出ができるようになると共に、第2には、還流ガス
を再び炉内に吐出させることができるようになる。また
、このような構造とすることにより、炉内部を気密に保
持することができるようになると共に、熱を無駄に炉外
へ流出させるようなことがなくなる。
Now, in the present invention, the furnace wall structure of the heating zone 2 of the furnace is as follows:
As mentioned above, by arranging a large number of ventilation gaps 38 and ventilation pipes 39 in a row in the part that contacts the iron skin 14, firstly,
The reaction gas generated in the furnace atmosphere of the heating zone 2 can be sucked and discharged, and secondly, the reflux gas can be discharged into the furnace again. Moreover, by adopting such a structure, the inside of the furnace can be kept airtight, and heat will not be wasted out of the furnace.

なお、前記通気パイプ39に設ける通気口39aは、パ
イプの周面の、とくに鉄皮14側に臨んで開口させるこ
とが望ましく、そしてこれらは2列位に分けて開口して
いることが望ましく、このような構成によると、炉壁鉄
皮の内側に沿って流通する炉内ガスを効果的に吸引でき
る。
The vent holes 39a provided in the vent pipe 39 are desirably opened on the circumferential surface of the pipe, particularly facing the iron shell 14 side, and these are desirably opened in two rows. According to such a configuration, the furnace gas flowing along the inside of the furnace wall shell can be effectively sucked.

第3図(c)は、上記の炉壁構造において、炉内を12
00’Cに加熱したときの炉壁の厚み方向の温度分布を
示すものである。同図より明らかなように、炉壁の温度
は鉄皮14に近づくほど低くなっており、このことから
、二〇鉄皮14と内張り耐火物13との境界部分に前記
通気パイプ39を配設することの意義が判る。
FIG. 3(c) shows that the inside of the furnace is 12 in the above furnace wall structure.
It shows the temperature distribution in the thickness direction of the furnace wall when heated to 00'C. As is clear from the figure, the temperature of the furnace wall becomes lower as it approaches the steel shell 14, and for this reason, the ventilation pipe 39 is arranged at the boundary between the steel shell 14 and the lining refractory 13. I understand the significance of what I do.

次に、本発明を縦形光輝焼鈍炉に適用した場合について
、第1図に基づき、それの雰囲気ガスの流れを説明する
Next, in the case where the present invention is applied to a vertical bright annealing furnace, the flow of atmospheric gas in the vertical bright annealing furnace will be explained based on FIG.

新鮮な雰囲気ガスの供給系統■は、冷却帯3に設けたガ
ス供給口16より、炉の入側・出側の各シール部4,5
からの漏洩分を補充し、炉内の圧力を大気圧よりも常に
高い状態を維持するように供給される。なお、冷却帯3
では、炉内ガスを、ブロワ−にてガスクーラー6を経由
させて吸引冷却し、加圧したのち、再び吹付はノズルを
介して炉内に冷風として戻している。従来の焼鈍炉にお
ける雰囲気ガスの供給系統はこれだけである。
The fresh atmospheric gas supply system (■) connects the gas supply port 16 provided in the cooling zone 3 to each seal section 4, 5 on the inlet and outlet sides of the furnace.
It is supplied to replenish the leakage from the furnace and maintain the pressure inside the furnace higher than atmospheric pressure at all times. In addition, cooling zone 3
In this case, the gas in the furnace is sucked and cooled by a blower via the gas cooler 6, and after being pressurized, the gas is blown back into the furnace as cold air through a nozzle. This is the only atmospheric gas supply system in a conventional annealing furnace.

この点、本発明の光輝焼鈍炉では、上記した新規ガス供
給系統■の他、内張り耐火物中に配設した通気パイプ3
9を通じて、それの周面に設けた多数の通気口39aか
ら加熱炉内の雰囲気ガスおよび炉の入・出側部の雰囲気
ガスを集めて吸引する■。
In this regard, in the bright annealing furnace of the present invention, in addition to the above-mentioned new gas supply system
9, the atmospheric gas inside the heating furnace and the atmospheric gas at the inlet and outlet sides of the furnace are collected and sucked through a large number of vent holes 39a provided on the circumferential surface thereof.

■の系統からなる循環ガス系統が付加されている。A circulating gas system consisting of system (2) is added.

まず、その■の循環ガス系統は、ブロワ−17と、雰囲
気ガスの露点を計測する露点計18と、薄帯1に付着し
て炉内に侵入した遊離酸素を雰囲気中の水素と反応させ
て水に変換するデオキソ19と、雰囲気ガス中の水分や
炭酸ガスを吸着除去する脱水装置20で構成されており
、この循環ガス系統■を経て清浄化された雰囲気ガスは
、前記系統■のガスと共に、あるいは単独にガス供給口
16より炉内の冷却帯3中に吹込まれる。
First, the circulating gas system (①) includes a blower 17, a dew point meter 18 that measures the dew point of the atmospheric gas, and a system that reacts free oxygen that has adhered to the ribbon 1 and entered the furnace with hydrogen in the atmosphere. It is composed of deoxo 19, which converts it into water, and a dehydrator 20, which adsorbs and removes moisture and carbon dioxide in the atmospheric gas. Alternatively, the gas may be blown into the cooling zone 3 inside the furnace from the gas supply port 16.

また、■の循環ガス系統は、炉の入側・出側のシール部
近傍から吸引した雰囲気ガスを、露点計21にて露点計
測後、ブロワ−22を経て、前記■の循環ガス系統とデ
オキソ19の手前で合流させた循環ガス系統である。
In addition, in the circulating gas system (2), atmospheric gas is sucked in from near the seals on the inlet and outlet sides of the furnace, and after measuring the dew point with a dew point meter 21, the gas is passed through the blower 22 and connected to the circulating gas system (2) and deoxo. This is a circulating gas system that merges just before No. 19.

なお、上述のガス排出構造は、炉の形式が縦型と横型と
では若干の違いはあるが、第1図に示すような、加熱帯
3の全長に亘る長い通気パイプ39を炉壁に沿って平行
に配設する場合の他、第2図に示すように短い通気パイ
プ39を例えば千鳥状に配設し、それぞれのパイプから
は1〜複数個の排出口15につながる排出パイプ15a
を接続してもよい。いずれにしても、通気間隙38およ
び通気パイプ39の配列は、炉体を取りかこむように設
置する。
Although there are some differences between vertical and horizontal furnaces, the above-mentioned gas exhaust structure has a long ventilation pipe 39 that runs the entire length of the heating zone 3 along the furnace wall, as shown in Figure 1. In addition to the case where short ventilation pipes 39 are arranged in parallel, for example, as shown in FIG.
may be connected. In any case, the ventilation gaps 38 and the ventilation pipes 39 are arranged so as to surround the furnace body.

また、このようなガス排出構造は加熱帯のみならず、入
口側の部分に配設してもよい。
Furthermore, such a gas exhaust structure may be provided not only in the heating zone but also in the inlet side portion.

上述したように、本発明によれば、主として加熱帯2の
鉄皮14の内面沿いに設けた通気間隙38および通気パ
イプ39に流入する炉内雰囲気ガスを、循環ガス系統0
を通じて吸引すると共に、炉の入側・出側の部分からも
循環ガス@を通じて吸引し、吸引・排出したこれらの炉
内雰囲気ガスを炉内に還流させることにより、早期に正
常な炉内雰囲気にすることができるから、直火式連続光
輝焼鈍炉の操業開始および再開時における待機時間を大
幅に短縮することができる。
As described above, according to the present invention, the furnace atmosphere gas flowing mainly into the ventilation gap 38 and the ventilation pipe 39 provided along the inner surface of the iron shell 14 of the heating zone 2 is transferred to the circulating gas system 0.
In addition to suctioning gas through the inlet and outlet sides of the furnace, the atmosphere gas inside the furnace is also sucked through the circulating gas @, and these suctioned and discharged furnace atmosphere gases are circulated back into the furnace, thereby quickly achieving a normal atmosphere inside the furnace. Therefore, it is possible to significantly shorten the waiting time when starting and restarting the operation of the direct-fired continuous bright annealing furnace.

次に、本発明光輝焼鈍炉の実際の炉操業における各供給
系統の運転要領について説明する。
Next, the operating procedures of each supply system in actual furnace operation of the bright annealing furnace of the present invention will be explained.

まず、新規ガス供給系統■については、操業全期間にわ
たり、炉内を所定圧力に保持するのに必要なガス量を供
給する。
First, regarding the new gas supply system (2), the amount of gas necessary to maintain the inside of the furnace at a predetermined pressure will be supplied throughout the entire operation period.

次に、循環ガス系統のうちの■は、操業開始時または再
開時はフル運転し、露点計18を監視しながら、乾燥が
進むに従って吸引力を次第に弱めていき、乾燥が完全に
終了したならば、ブロワ−17による吸引を停止すると
同時に、ストップバルブ23を閉止する。このように乾
燥終了後、■系統を止める理由は、前述したように炉内
の揮発金属蒸気が耐火物に不必要に沈着することを回避
するためである。
Next, the circulating gas system (■) is operated at full capacity when starting or resuming operation, and while monitoring the dew point meter 18, the suction power is gradually weakened as the drying progresses. For example, the stop valve 23 is closed at the same time as the suction by the blower 17 is stopped. The reason why the system (1) is stopped after drying is completed is to prevent volatile metal vapor in the furnace from unnecessarily depositing on the refractories, as described above.

なお、より有利な揮発金属蒸気の沈着防止策としては、
乾燥終了後は、脱水処理を終えた清浄ガスをストップパ
ルプ23を閉じ、26を開けて、ブロワ−17を止め、
炉殻鉄皮に設けた排出口15および通気パイプ39を通
じて、炉内外の圧力差を利用して、逆に炉内に送り込ん
で還流させることも可能である。
In addition, as a more advantageous measure to prevent the deposition of volatile metal vapors,
After the drying is completed, the clean gas that has completed the dehydration process is supplied by closing the stop pulp 23, opening the stop pulp 26, and stopping the blower 17.
Conversely, it is also possible to send it into the furnace and reflux it through the discharge port 15 and the ventilation pipe 39 provided in the furnace shell, by utilizing the pressure difference between the inside and outside of the furnace.

また、循環ガス系統@は、炉の出入口であって外気との
接点である。したがって、常時atの空気が侵入するか
ら、露点計21を監視しながら、所望の低露点を保持す
るために積極的に吸引し、常時低露点に維持するのに必
要である。
Further, the circulating gas system @ is the entrance and exit of the furnace and the point of contact with the outside air. Therefore, since AT air constantly enters, it is necessary to monitor the dew point meter 21 and actively suck the air in order to maintain the desired low dew point at all times.

以上の■およびOの各循環ガス系統の説明は、主として
吸引した雰囲気ガスを再利用する場合についてのもので
ある。しかしながら、本発明では、必ずしも吸引した雰
囲気ガスを清浄化して再吹込みを行う循環供給系統だけ
が必要なわけではない。
The above explanations of the circulating gas systems (1) and (0) are mainly for the case where the sucked atmospheric gas is reused. However, the present invention does not necessarily require only a circulation supply system for cleaning and re-blowing the sucked atmospheric gas.

その他に、例えば少なくとも炉壁部から単に雰囲気ガス
を吸引し、排出するだけという、いわゆる吸引排出系統
だけでも良いのである。なお、このケースにおいて、吸
引した雰囲気ガスを清浄化したり再利用しない場合には
、吸引したガスをストソプハルブ25を開放する一方、
■の循環ガス系統内ストップバルブ23を閉止してその
まま放散ブリグーから大気中に放散しても良い。
Alternatively, a so-called suction and discharge system may be used, which simply sucks and discharges atmospheric gas from at least the furnace wall. Note that in this case, if the sucked atmospheric gas is not cleaned or reused, the sucked gas is released by opening the gas valve 25;
The stop valve 23 in the circulating gas system (2) may be closed and the gas may be directly released into the atmosphere from the dissipation brigoo.

第1図にもとづく以」二の説明は、焼鈍炉の各部の構成
が継型;すなわち加熱帯入口から冷却帯出口に至るまで
の薄板通板経路の各帯域配置が、縦配列にかかる例であ
るが、本発明としては、その他に、かかる各帯域の配列
を横並びに配列することも可能であり、この場合でも本
発明の作用・効果は特に変わるものではない。
The second explanation based on Fig. 1 is an example in which the structure of each part of the annealing furnace is a joint type; that is, the arrangement of each zone of the sheet passing path from the heating zone inlet to the cooling zone outlet is vertically arranged. However, in the present invention, it is also possible to arrange the respective bands side by side, and even in this case, the operation and effect of the present invention does not particularly change.

すなわち、本発明の他の実施例について、第4図にその
構成を例示する。図において、水平に搬送される金属薄
帯1は、炉入口シール部41を経て、順次水平に配置さ
れている加熱帯42、徐冷帯43、冷却帯44を通過し
、炉出口シール部45に到達するが、その間薄帯1は第
1図示例の場合と異なり、−貫して水平に搬送されるこ
とになる。そのために、各帯域42.43.44には薄
帯支持のための支持ロール46を炉内搬送ラインに沿っ
て複数個列設し、通板材の垂れ下がりを防止するように
構成する。
That is, FIG. 4 illustrates the configuration of another embodiment of the present invention. In the figure, the metal ribbon 1 conveyed horizontally passes through a furnace inlet sealing section 41, a heating zone 42, an annealing zone 43, and a cooling zone 44 which are arranged horizontally in order, and then passes through a furnace outlet sealing section 45. However, during this time, the ribbon 1 is conveyed horizontally, unlike in the first illustrated example. For this purpose, a plurality of support rolls 46 for supporting the ribbon are arranged in rows along the furnace conveyance line in each zone 42, 43, 44 to prevent the threaded material from sagging.

なお、図中に示す符号6.7.14.15〜23.25
26は、いずれも第1図に示す焼鈍炉の構造と同じ構成
を示し、それらは継型のものを単に横型配置に適合する
ようにアレンジされるだけで十分である。
In addition, the symbols 6.7.14.15 to 23.25 shown in the figure
26 all have the same construction as that of the annealing furnace shown in FIG. 1, and it is sufficient for them to simply arrange the joint molds to suit the horizontal arrangement.

〔発明の効果〕〔Effect of the invention〕

か(してこの発明によれば、直火式の利点である熱効率
を低下させることなしに、従来に比べて操業開始又は再
開までの待機時間を大幅に短縮することができ、工業的
に寄与するところ大である。
(According to this invention, the waiting time before starting or resuming operation can be significantly shortened compared to the conventional method without reducing the thermal efficiency, which is an advantage of the direct-fired type. It's a big deal.

しかも本発明によれば、炉内雰囲気ガスの吸引。Moreover, according to the present invention, the furnace atmosphere gas is sucked.

排出を、温度の最も低い鉄皮内面沿いに設けた通気用間
隙内に吸引パイプを設置して行うので、吸引パイプの保
護とともに、炉内ガスの吸引・排出を円滑なものにする
ことができる。
Since the suction pipe is installed in the ventilation gap along the inner surface of the steel shell, where the temperature is lowest, the suction pipe is protected and the gas in the furnace can be suctioned and discharged smoothly. .

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

第1図は、縦型の例である本発明の連続光耀焼鈍炉の好
適例を示す模式図、 第2図は、通気パイプを分割したときの本発明の他の実
施例の継型連続焼鈍炉を示す模式図、第3図(a)は第
1図A部の拡大断面図、同図(b)は通気パイプ固定の
もようを示すもので、(a)図のB−B矢視方向から見
た炉内部分正面図、同図(c)は炉壁厚み方向の温度分
布図、同図(d)は通気パイプ取付は状態の部分断面図
、および同図(e)は(a)図のX−X矢視部断面図、
第4図は、本発明の他実施例である横型連続光註焼鈍炉
の好適例を示す模式図、 第5図は、加熱帯にマツフルを具える従来の縮型連続光
輝焼鈍炉の模式図である。 ■・・・金属薄帯、2・・・加熱帯、3・・・冷却帯、
4・・・炉入口シール部、 5・・・炉出口シール部、
6・・・ガスクーラー 7・・・ブロワ−訃・・発熱体
、 9・・・給電部材、 1o・・・支持金具、11・
・・内張り耐火れんが、 12・・・断熱れんが、13
・・・保温材、 14・・・鉄皮、 15・・・排出口
、15a・・・排出パイプ、 16・・・ガス供給口、
17、22・・・ブロワ−18,21・・・露点計、1
9・・・デオキソ、 20・・・脱水装置、23、25
.26・・・ストップパルプ、 24・・・マツフル、
3I・・・入口シール部、32・・・加熱帯、 33・
・・徐冷帯、34・・・冷却帯、 35・・・出口シー
ル部、36、37・・・支持ロール、 38・・・通気
間隙、39・・・通気パイプ、 39a・・・通気口、
41・・・炉入口シール部、 42・・・加熱帯、43
・・・徐冷帯、 44・・・冷却帯、45・・・炉出口
シール部、 46・・・支持ロール、47・・・固定金
具 特許出願人 日本冶金工業株式会社 同   中外炉工業株式会社 代理人 弁理士  小 川 順 三 同  弁理士  中 村 盛 夫 第1 図 第゛3 図 第2 区 (d) (e)
Fig. 1 is a schematic diagram showing a preferable example of the continuous light annealing furnace of the present invention, which is a vertical example, and Fig. 2 is a joint type continuous annealing furnace of another embodiment of the present invention when the ventilation pipe is divided. A schematic diagram showing the furnace. Figure 3 (a) is an enlarged sectional view of part A in Figure 1, and Figure 3 (b) shows how the ventilation pipe is fixed. (c) is a temperature distribution diagram in the thickness direction of the furnace wall, (d) is a partial cross-sectional view of the ventilation pipe installed, and (e) is (a). ) A cross-sectional view taken along the line X-X in the figure,
Fig. 4 is a schematic diagram showing a preferred example of a horizontal continuous bright annealing furnace which is another embodiment of the present invention, and Fig. 5 is a schematic diagram of a conventional contracted continuous bright annealing furnace equipped with a matzuru in the heating zone. It is. ■...Metal thin strip, 2...Heating zone, 3...Cooling zone,
4...Furnace inlet seal part, 5...Furnace outlet seal part,
6... Gas cooler 7... Blower end... Heating element, 9... Power supply member, 1o... Supporting metal fitting, 11...
...Inner refractory brick, 12...Insulating brick, 13
...Heat insulation material, 14...Iron shell, 15...Discharge port, 15a...Discharge pipe, 16...Gas supply port,
17, 22... Blower 18, 21... Dew point meter, 1
9... Deoxo, 20... Dehydration device, 23, 25
.. 26...Stop pulp, 24...Matsuful,
3I...Inlet seal part, 32...Heating zone, 33.
... slow cooling zone, 34... cooling zone, 35... outlet seal section, 36, 37... support roll, 38... ventilation gap, 39... ventilation pipe, 39a... ventilation port ,
41...Furnace inlet seal part, 42...Heating zone, 43
...Annealing zone, 44...Cooling zone, 45...Furnace outlet seal portion, 46...Support roll, 47...Fixing metal patent applicant Nippon Yakin Kogyo Co., Ltd. Chugai Roko Kogyo Co., Ltd. Agent Patent Attorney Jun Ogawa Sando Patent Attorney Morio Nakamura Figure 1 Figure 3 Figure 2 Wards (d) (e)

Claims (1)

【特許請求の範囲】 1、外壁鉄皮の内側に耐火物の内張りを設けて構成され
る炉壁を有し、内部が主として加熱帯とそれの下流側に
連設された冷却帯とからなる気密式の炉であって、前記
加熱帯から連続的に導入される金属薄帯を、還元性雰囲
気にて直接的に加熱し引続き冷却する形式の焼鈍炉にお
いて、前記炉壁の内張り耐火物と外壁鉄皮との境界部に
、条孔状の通気間隙を複数列に亘って設け、これらの通
気間隙内には、周面の鉄皮側に向けて多数の通気口を開
口させてなる通気パイプを配設すると共に、この通気パ
イプを前記鉄皮の内面に係止したことを特徴とする光輝
焼鈍炉。 2、外壁鉄皮の内側に耐火物の内張りを設けて構成され
る炉壁を有し、内部が主として加熱帯とそれの下流側に
連設された冷却帯とからなる気密式の炉であって、前記
加熱帯から連続的に導入される金属薄帯を、還元性雰囲
気にて直接的に加熱し引続き冷却する形式の焼鈍炉にお
いて、前記炉壁の内張り耐火物と外壁鉄皮との境界部に
、条孔状の通気間隙を複数列に亘って設け、これらの通
気間隙内には、周面の鉄皮側に向けて多数の通気口を開
口させてなる通気パイプを配設すると共に、この通気パ
イプを前記鉄皮の内面に係止し、かつ 前記通気パイプを通じて炉内のガスを炉外に排出するよ
うにしてなり、かつ炉外には、吸引排出した前記ガス中
の不純物成分を除去して清浄化したのち、炉内に再供給
する炉内ガスの循環装置を付帯して設けたことを特徴と
する光輝焼鈍炉。
[Claims] 1. It has a furnace wall constructed by providing a refractory lining inside an outer wall iron skin, and the interior mainly consists of a heating zone and a cooling zone connected downstream of the furnace wall. In an annealing furnace which is an airtight furnace and which directly heats a metal ribbon continuously introduced from the heating zone in a reducing atmosphere and then cools it, the furnace wall lining refractory and Multiple rows of strip-shaped ventilation gaps are provided at the boundary with the outer wall steel skin, and within these ventilation gaps, a large number of ventilation holes are opened toward the steel skin side of the surrounding surface. A bright annealing furnace characterized in that a pipe is provided and the ventilation pipe is locked to the inner surface of the iron shell. 2. It is an airtight furnace with a furnace wall consisting of a refractory lining on the inside of the outer shell, and the interior mainly consists of a heating zone and a cooling zone connected downstream of it. In an annealing furnace of the type in which a metal ribbon continuously introduced from the heating zone is directly heated in a reducing atmosphere and then cooled, the boundary between the refractory lining of the furnace wall and the outer wall steel is A plurality of rows of strip-shaped ventilation gaps are provided in the section, and within these ventilation gaps, ventilation pipes with a large number of ventilation holes opening toward the iron shell side of the circumferential surface are arranged. , the ventilation pipe is fixed to the inner surface of the iron shell, and the gas inside the furnace is discharged to the outside of the furnace through the ventilation pipe, and impurity components in the suctioned and discharged gas are discharged outside the furnace. What is claimed is: 1. A bright annealing furnace characterized in that a bright annealing furnace is additionally provided with a circulation device for re-supplying furnace gas to the inside of the furnace after the gas is removed and cleaned.
JP2232530A 1990-09-04 1990-09-04 Bright annealing furnace Expired - Fee Related JP2567140B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2232530A JP2567140B2 (en) 1990-09-04 1990-09-04 Bright annealing furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2232530A JP2567140B2 (en) 1990-09-04 1990-09-04 Bright annealing furnace

Publications (2)

Publication Number Publication Date
JPH04116127A true JPH04116127A (en) 1992-04-16
JP2567140B2 JP2567140B2 (en) 1996-12-25

Family

ID=16940784

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2232530A Expired - Fee Related JP2567140B2 (en) 1990-09-04 1990-09-04 Bright annealing furnace

Country Status (1)

Country Link
JP (1) JP2567140B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013150710A1 (en) 2012-04-06 2013-10-10 Jfeスチール株式会社 Continuous hot-dip zinc plating facility
WO2014087452A1 (en) 2012-12-04 2014-06-12 Jfeスチール株式会社 Facility and method for manufacturing continuous hot-dip zinc-coated steel sheet

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5071551B2 (en) 2010-12-17 2012-11-14 Jfeスチール株式会社 Continuous annealing method for steel strip, hot dip galvanizing method
JP5505430B2 (en) 2012-01-17 2014-05-28 Jfeスチール株式会社 Continuous annealing furnace and continuous annealing method for steel strip
JP5505461B2 (en) 2012-05-24 2014-05-28 Jfeスチール株式会社 Continuous annealing furnace for steel strip, continuous annealing method for steel strip, continuous hot dip galvanizing equipment and method for manufacturing hot dip galvanized steel strip
JP5510495B2 (en) 2012-05-24 2014-06-04 Jfeスチール株式会社 Continuous annealing furnace for steel strip, continuous annealing method, continuous hot dip galvanizing equipment and manufacturing method of hot dip galvanized steel strip
US10106867B2 (en) 2012-06-13 2018-10-23 Jfe Steel Corporation Method for continuously annealing steel strip and method for manufacturing galvanized steel strip
EP2862946B1 (en) 2012-06-13 2019-03-06 JFE Steel Corporation Method for continuously annealing steel strip, apparatus for continuously annealing steel strip, method for manufacturing hot-dip galvanized steel strip, and apparatus for manufacturing hot-dip galvanized steel strip
EP3067434B1 (en) 2013-11-07 2018-04-18 JFE Steel Corporation Continuous annealing equipment and continuous annealing method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61253327A (en) * 1985-04-30 1986-11-11 Sumitomo Metal Ind Ltd Method for decreasing dew point of heating furnace
JPS62177126A (en) * 1986-01-31 1987-08-04 Nisshin Steel Co Ltd Method for continuously annealing strip

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61253327A (en) * 1985-04-30 1986-11-11 Sumitomo Metal Ind Ltd Method for decreasing dew point of heating furnace
JPS62177126A (en) * 1986-01-31 1987-08-04 Nisshin Steel Co Ltd Method for continuously annealing strip

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013150710A1 (en) 2012-04-06 2013-10-10 Jfeスチール株式会社 Continuous hot-dip zinc plating facility
KR20140145586A (en) 2012-04-06 2014-12-23 제이에프이 스틸 가부시키가이샤 Continuous hot-dip zinc plating facility
US9713823B2 (en) 2012-04-06 2017-07-25 Jfe Steel Corporation Continuous galvanizing line having an annealing furnace
WO2014087452A1 (en) 2012-12-04 2014-06-12 Jfeスチール株式会社 Facility and method for manufacturing continuous hot-dip zinc-coated steel sheet
US10233526B2 (en) 2012-12-04 2019-03-19 Jfe Steel Corporation Facility having a continuous annealing furnace and a galvanization bath and method for continuously manufacturing hot-dip galvanized steel sheet

Also Published As

Publication number Publication date
JP2567140B2 (en) 1996-12-25

Similar Documents

Publication Publication Date Title
JP2009019786A (en) Device and method for exhaust gas treatment of rotary hearth-type reducing furnace
JPH04116127A (en) Bright annealing furnace
KR20020010577A (en) A method of heating metal strip and apparatus therefor
JP2567130B2 (en) Bright annealing furnace
JP2002243368A (en) Continuous kiln for flat sheet glass
US2057518A (en) Apparatus for bright annealing metallic products
KR20080084531A (en) Continuous firing furnace
JP2567113B2 (en) Bright annealing furnace
KR100424095B1 (en) Batch-type brazing furnace system
JPS62290830A (en) Continuous annealing method for steel strip and annealing furnace therefor
JP4210833B2 (en) Continuous firing furnace
KR100885884B1 (en) Apparatus for preventing gas intrusion in annealing furnace
KR20090121242A (en) Heat treatment device
JP4042812B2 (en) Semiconductor manufacturing equipment
CN110964879A (en) Cooling section structure of heat treatment kiln
JP2003247025A (en) Production line used for both cold-rolled steel sheet and galvanized steel sheet
JPS6040657A (en) Device for recovering heat from equipment behind continuous casting machine
EP1338659A1 (en) White powder removing device for continuous annealing furnace
JP2002275546A (en) Facility used for both continuous annealing and hot dipping
JPH06323738A (en) Roller hearth kiln
KR100424097B1 (en) Preheating system of brazing object for batch-type brazing furnace system
JPH047506Y2 (en)
KR200260916Y1 (en) Cooling Water Leakage Monitoring and Automatic Discharge Device in Annealing Furnace
JP2002285235A (en) Vertical type continuous annealing apparatus
JPH02274821A (en) Method for feeding atmospheric gas in continuous heat treatment furnace

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313117

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20071003

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081003

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091003

Year of fee payment: 13

LAPS Cancellation because of no payment of annual fees