JPH07100826B2 - Continuous annealing furnace - Google Patents
Continuous annealing furnaceInfo
- Publication number
- JPH07100826B2 JPH07100826B2 JP16834991A JP16834991A JPH07100826B2 JP H07100826 B2 JPH07100826 B2 JP H07100826B2 JP 16834991 A JP16834991 A JP 16834991A JP 16834991 A JP16834991 A JP 16834991A JP H07100826 B2 JPH07100826 B2 JP H07100826B2
- Authority
- JP
- Japan
- Prior art keywords
- roll chamber
- chamber
- gas
- dff
- rtf
- 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 - Fee Related
Links
Landscapes
- Heat Treatment Of Strip Materials And Filament Materials (AREA)
Description
【0001】[0001]
【産業上の利用分野】この発明は、溶融亜鉛めっきライ
ン等に用いられる連続焼鈍炉に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a continuous annealing furnace used in hot dip galvanizing lines and the like.
【0002】[0002]
【従来の技術】通常、溶融亜鉛めっきラインには連続焼
鈍炉が設けられ、鋼帯を所望温度に焼鈍し、その後にめ
っき浴に浸漬する。2. Description of the Related Art Usually, a hot-dip galvanizing line is provided with a continuous annealing furnace, in which a steel strip is annealed to a desired temperature and then immersed in a plating bath.
【0003】めっきライン用の連続焼鈍炉は、特公昭6
2−57692号公報、特公昭62−59168号公
報、特公平1−21204号公報、特公平1−2185
2号公報、特開平1−283352号公報、並びに特開
平2−8331号公報にそれぞれ記載されている。A continuous annealing furnace for a plating line is disclosed in Japanese Patent Publication No.
No. 2-57692, Japanese Patent Publication No. 62-59168, Japanese Patent Publication No. 1-21204, and Japanese Patent Publication No. 1-2185.
No. 2, JP-A-1-283352, and JP-A No. 2-8331.
【0004】図2に示すように、このような連続焼鈍炉
には、直火加熱炉(以下、DFFという)3及びラジア
ントチュ−ブ炉(以下、RTFという)5が設けられて
いる。DFF3は、多数のバ−ナ−を有する竪型の加熱
炉であり、鋼帯に還元性火炎を直接吹き付けて加熱する
役割を有する。RTF5は、DFF3の下流側に設けら
れ、還元性雰囲気、例えば、水素ガスおよび窒素ガスの
混合ガスに置換した雰囲気下で、鋼帯を上下に複数回往
復させつつ、ドライな状態で鋼帯を均熱する役割を有す
る。As shown in FIG. 2, such a continuous annealing furnace is provided with a direct heating furnace (hereinafter referred to as DFF) 3 and a radiant tube furnace (hereinafter referred to as RTF) 5. The DFF 3 is a vertical heating furnace having a large number of burners, and has a role of directly blowing a reducing flame onto a steel strip to heat it. The RTF 5 is provided on the downstream side of the DFF 3, and in a reducing atmosphere, for example, an atmosphere in which a mixed gas of hydrogen gas and nitrogen gas is replaced, the steel strip is reciprocated up and down a plurality of times, and the steel strip is dried in a dry state. Has a role of soaking.
【0005】この場合に、DFF3の燃焼廃ガスがRT
F5内に侵入すると、廃ガス中の湿分によりRTF5の
還元性雰囲気が壊されるので、下部ロ−ル室4を炉下部
に設けると共に、ガス流が常にRTF5の側からDFF
3の側に向かって(鋼帯搬送路の下流側から上流側へ向
かって)流れるように、多量の還元性ガスをRTF5内
に供給し、RTF5の内圧を下部ロ−ル室4のそれより
も高くしている。In this case, the combustion waste gas of the DFF 3 is RT
When it enters the F5, the reducing atmosphere of the RTF5 is destroyed by the moisture in the waste gas, so that the lower roll chamber 4 is provided at the lower part of the furnace and the gas flow is always from the side of the RTF5 to the DFF.
A large amount of reducing gas is supplied into the RTF 5 so as to flow toward the 3 side (from the downstream side to the upstream side of the steel strip conveying path), and the internal pressure of the RTF 5 is set to be lower than that in the lower roll chamber 4. Is also high.
【0006】また、DFF3の廃ガスの一部が上部ロ−
ル室2内に侵入し、ロ−ル表面が酸化されて肌荒れを生
じ、これにより鋼帯表面を傷付ける所謂ロ−ルのピック
アップ防止のために、エジェクタ7を有するバイパス通
路6を炉上部に設けている。このバイパス通路6を介し
てRTF5の還元性ガスを上部ロ−ル室2へ供給し、さ
らに、窒素ガス供給源8からも窒素ガスを吹き込み、上
部ロ−ル室2のロ−ルの酸化を防止する。In addition, a part of the waste gas of DFF3 is in the upper region.
A bypass passage 6 having an ejector 7 is provided in the upper part of the furnace in order to prevent the so-called roll pick-up from penetrating into the roll chamber 2 and oxidizing the roll surface to roughen the surface of the steel strip. ing. The reducing gas in the RTF 5 is supplied to the upper roll chamber 2 through the bypass passage 6, and nitrogen gas is blown from the nitrogen gas supply source 8 to oxidize the roll in the upper roll chamber 2. To prevent.
【0007】[0007]
【発明が解決しようとする課題】しかしながら、上部バ
イパス通路6は廃ガスの逆流防止を目的とするものでは
ないため、下部ロ−ル室4を経由して廃ガスの逆流が生
じる。すなわち、下部ロ−ル室4の圧力制御の応答性を
上回る操業上の種々の条件および変動に起因して、ガス
流が一時的にDFF3からRTF5へ向かって逆流する
ことがある。However, since the upper bypass passage 6 is not intended to prevent the backflow of the waste gas, the backflow of the waste gas occurs via the lower roll chamber 4. That is, due to various operational conditions and fluctuations that exceed the pressure control response of the lower roll chamber 4, the gas flow may temporarily flow back from the DFF 3 toward the RTF 5.
【0008】このような逆流は、DFF3のゾ−ン点火
時、またはDFF3の燃焼量が急激に増加したときに、
下部ロ−ル室4の圧力がRTF5のそれを一時的に上回
ることにより生じる。Such backflow is caused when the zone ignition of the DFF 3 is performed or when the combustion amount of the DFF 3 is rapidly increased.
It occurs because the pressure in the lower roll chamber 4 temporarily exceeds that of the RTF 5.
【0009】DFF3の燃焼排ガスがRTF5へ向かっ
て逆流すると、RTF5のドライな還元性雰囲気が壊さ
れ、鋼帯表面が酸化されてしまい、その後のめっき処理
に悪影響が及び、製品の品質低下を生じる。RTF以降
の炉内容積は大きいので、通常、還元雰囲気の回復には
長時間を要する。この間の製品の品質低下は重大な損失
となる。When the combustion exhaust gas of the DFF 3 flows back toward the RTF 5, the dry reducing atmosphere of the RTF 5 is destroyed and the surface of the steel strip is oxidized, which adversely affects the subsequent plating process and deteriorates the quality of the product. . Since the furnace volume after the RTF is large, it usually takes a long time to recover the reducing atmosphere. During this period, the deterioration of product quality is a serious loss.
【0010】逆に、DFF3の一部ゾ−ンを消火または
燃焼量を急激に低下させる場合は、下部ロ−ル室4の内
圧が制御圧力より瞬時低下し、これがRTF5以降の雰
囲気炉へ直接的に炉圧変動を引き起こし、炉体各部シ−
ル部からの外気侵入の危険性を招く。On the contrary, when the partial zone of the DFF 3 is extinguished or the combustion amount is drastically lowered, the internal pressure of the lower roll chamber 4 is instantly lowered from the control pressure, and this is directly fed to the atmosphere furnace after RTF 5. Cause furnace pressure fluctuations, and
There is a risk of invasion of outside air from the cable.
【0011】同時に、RTF5の雰囲気ガスのDFF3
への流量が一時的に増大し、DFF火炎の還元力を低下
させる。DFF3での還元性低下は製品品質に直接影響
を及ぼす。At the same time, the DFF3 of the atmosphere gas of the RTF5
The flow rate to the air flow temporarily increases and reduces the reducing power of the DFF flame. The reduction in the reducibility of DFF3 directly affects the product quality.
【0012】また、下部ロ−ル室4の内圧の急変は炉圧
制御の外乱となり、安定制御までの回復時間を増大させ
ることになる。炉圧制御性に与える影響はDFFゾ−ン
点火時と同様の問題がある。Further, a sudden change in the internal pressure of the lower roll chamber 4 becomes a disturbance of the furnace pressure control, which increases the recovery time until the stable control. The influence on the furnace pressure controllability has the same problem as in the DFF zone ignition.
【0013】この発明は、上記課題を解決するためにな
されたものであり、DFF側の変動の影響がRTF側へ
実質的に及ばず、安定に操業することができ、製品の品
質向上を図ることができる連続焼鈍炉を提供することを
目的とする。The present invention has been made in order to solve the above-mentioned problems, and the influence of fluctuations on the DFF side does not substantially affect the RTF side, which enables stable operation and improves product quality. It is an object of the present invention to provide a continuous annealing furnace that can be used.
【0014】[0014]
【課題を解決するための手段】従来、RTFへの雰囲気
ガス量が多量であるために、一時的に逆流が発生して
も、多量の還元性ガスによりDFFの燃焼ガスが緩和さ
れ、DFF及びRTFの間のロ−ル室においては特別な
シ−ル対策が取られていなかった。Conventionally, since the amount of atmospheric gas to the RTF is large, even if a reverse flow occurs temporarily, a large amount of reducing gas relaxes the combustion gas of the DFF. No special sealing measures were taken in the roll room during the RTF.
【0015】しかしながら、近時の需要家による品質上
の要求は高く、このような要望に応えるために、発明者
らは、操業上の変動に応じてDFFとRTFとの間の雰
囲気をロ−ル室にて遮断することにつき鋭意研究した。However, there is a recent high demand for quality from consumers, and in order to meet such demand, the inventors have set the atmosphere between DFF and RTF in accordance with the fluctuation in operation. I conducted a diligent study on shutting off in a room.
【0016】この発明に係る連続焼鈍炉は、直火還元火
炎を用いて被処理体を加熱する直火加熱帯と、還元性雰
囲気下で被処理体を均熱する無酸化均熱帯とを有する連
続焼鈍炉において、前記直火加熱帯の上方に設けられ、
被処理体を前記直火加熱帯へ送るロ−ルを備えた上部ロ
−ル室と、前記直火加熱帯の下方に設けられ、被処理体
を前記直火加熱帯から前記無酸化均熱帯へ向かって送る
ロ−ルを備えた下部ロ−ル室と、この下部ロ−ル室に設
けられたシ−ル機構と、前記下部ロ−ル室から前記上部
ロ−ル室へ連通するバイパス通路と、を有することを特
徴とする。さらに、ガス供給手段をバイパス通路の途中
経路に設け、バイパス通路内に非酸化性のガスを供給す
ることが望ましい。The continuous annealing furnace according to the present invention has an open flame heating zone for heating an object to be treated by using a direct reduction flame and an oxidation-free soaking zone for soaking the object in a reducing atmosphere. In a continuous annealing furnace, provided above the open flame heating zone,
An upper roll chamber having a roll for feeding the object to be processed to the open flame heating zone and a lower part of the open flame heating zone for transferring the object to be treated from the open flame heating zone to the non-oxidizing soaking zone. Lower roll chamber provided with a roll for sending toward, a seal mechanism provided in the lower roll chamber, and a bypass communicating from the lower roll chamber to the upper roll chamber. And a passage. Furthermore, it is desirable to provide a gas supply means in the middle of the bypass passage and supply a non-oxidizing gas into the bypass passage.
【0017】[0017]
【作用】この発明に係る連続焼鈍炉においては、シ−ル
機構を下部ロ−ル室内に設けているので、湿分を含む廃
ガスが下部ロ−ル室を経由して直火加熱帯から無酸化均
熱帯へ侵入しなくなる。In the continuous annealing furnace according to the present invention, since the seal mechanism is provided in the lower roll chamber, waste gas containing moisture passes through the lower roll chamber from the open flame heating zone. It will not enter the non-oxidizing soaking zone.
【0018】また、バイパス通路を下部ロ−ル室および
上部ロ−ル室の間に設けているので、直火加熱帯の内圧
が上昇し、下部ロ−ル室に多量の廃ガスが流入した場合
に、無酸化均熱帯に流れ込むことなく、廃ガスはバイパ
ス通路を経由して上部ロ−ル室に逃がされる。このた
め、下部ロ−ル室にて直火加熱帯の側と無酸化均熱帯の
側との雰囲気が遮断され、無酸化均熱帯の還元性雰囲気
が壊されなくなる。Further, since the bypass passage is provided between the lower roll chamber and the upper roll chamber, the internal pressure of the open flame heating zone rises and a large amount of waste gas flows into the lower roll chamber. In this case, the waste gas is released to the upper roll chamber via the bypass passage without flowing into the non-oxidizing soaking zone. Therefore, in the lower roll chamber, the atmosphere between the direct-fired heating zone side and the non-oxidizing soaking zone side is shut off, and the reducing atmosphere of the non-oxidizing soaking zone is not destroyed.
【0019】[0019]
【実施例】以下、添付の図面を参照してこの発明の実施
例について説明する。Embodiments of the present invention will be described below with reference to the accompanying drawings.
【0020】図1に示すように、上部ロ−ル室10がD
FF12の上部に設けられ、上部ロ−ル室のロ−ル10
aにより鋼帯9の送給方向が水平から垂直に変換される
ようになっている。上部ロ−ル室10の上流側は、図示
しない予熱炉に連通している。廃ガス通路11が上部ロ
−ル室10およびDFF12の間に設けられ、DFF1
2の燃焼廃ガスが排気されるようになっている。As shown in FIG. 1, the upper roll chamber 10 is D
The roll 10 provided in the upper part of the FF 12 and in the upper roll chamber
By a, the feeding direction of the steel strip 9 is changed from horizontal to vertical. The upstream side of the upper roll chamber 10 communicates with a preheating furnace (not shown). A waste gas passage 11 is provided between the upper roll chamber 10 and the DFF 12, and the DFF 1
2 combustion waste gas is exhausted.
【0021】下部ロ−ル室14は、DFF12の最下部
にてDFF12及びRTF21の間に水平に設けられ、
二つの小部屋15,18を有する。因みに、上部ロ−ル
10と下部ロ−ル室14との高低差は約20mである。The lower roll chamber 14 is horizontally installed between the DFF 12 and the RTF 21 at the bottom of the DFF 12.
It has two small rooms 15 and 18. By the way, the height difference between the upper roll 10 and the lower roll chamber 14 is about 20 m.
【0022】上流側の小部屋15は搬送ロ−ル15aを
内臓しており、DFF12から垂直搬送された鋼帯9が
搬送ロ−ル15aにより搬送方向を水平に変更されるよ
うになっている。また、下流側の小部屋18も搬送ロ−
ル18aを内臓しており、上流側から水平搬送された鋼
帯9が搬送ロ−ル18aにより搬送方向を垂直に変更さ
れ、さらに、RTF21に搬送されるようになってい
る。RTF21の内部には多数対の上下ロ−ル21aが
設けられている。鋼帯2は、RTF21内を上下往復し
つつ、水素ガスおよび窒素ガスの混合ガスからなる還元
性ガスにより均熱されるようになっている。The small chamber 15 on the upstream side has a conveying roll 15a therein, and the steel strip 9 vertically conveyed from the DFF 12 can be changed in the conveying direction horizontally by the conveying roll 15a. . In addition, the small room 18 on the downstream side also has a transport roll.
The steel strip 9 that has a built-in roll 18a is horizontally transported from the upstream side, the transport direction is changed to a vertical direction by the transport roll 18a, and the steel strip 9 is further transported to the RTF 21. Inside the RTF 21, a plurality of pairs of upper and lower rolls 21a are provided. The steel strip 2 reciprocates up and down in the RTF 21, and is uniformly heated by a reducing gas composed of a mixed gas of hydrogen gas and nitrogen gas.
【0023】シ−ル機構17が下部ロ−ル室14の内部
に設けられ、シ−ル機構17により下流側小部屋18が
上流側小部屋15から有効にシ−ルされている。シ−ル
機構17は、鋼帯9が通過するに必要十分なだけの矩形
ボックス(図示せず)を有している。このシ−ルボック
スおよびロ−ル室内壁の間隙に断熱部材(図示せず)が
詰め込まれ、上流側小部屋15から下流側小部屋18へ
通気しないようにされている。A seal mechanism 17 is provided inside the lower roll chamber 14, and the seal mechanism 17 effectively seals the downstream small chamber 18 from the upstream small chamber 15. The seal mechanism 17 has enough rectangular boxes (not shown) for the steel strip 9 to pass through. A heat insulating member (not shown) is packed in the gap between the seal box and the inner wall of the roll to prevent ventilation from the upstream small chamber 15 to the downstream small chamber 18.
【0024】バイパス通路22,24が、下部ロ−ル室
14及び上部ロ−ル室10のそれぞれに連通している。
バイパス通路22は、下部ロ−ル室14の上流側小部屋
15のほうに連通している。この場合に、バイパス通路
22を下流側小部屋18に連通させてもよい。また、バ
イパス通路24は上部ロ−ル室10の適所に連通してい
る。The bypass passages 22 and 24 communicate with the lower roll chamber 14 and the upper roll chamber 10, respectively.
The bypass passage 22 communicates with the upstream small chamber 15 of the lower roll chamber 14. In this case, the bypass passage 22 may be communicated with the downstream small chamber 18. Further, the bypass passage 24 communicates with an appropriate place in the upper roll chamber 10.
【0025】バイパス通路22及び通路24の間にエジ
ェクタ23が設けられている。このエジェクタ23には
ダンパ25を介してガス供給源26の供給口が連通して
いる。ガス供給源26には窒素ガスが貯えられている。
ダンパ25は開閉および流量調節機能を有する。次に、
上記装置の動作について説明する。An ejector 23 is provided between the bypass passage 22 and the passage 24. A supply port of a gas supply source 26 communicates with the ejector 23 via a damper 25. Nitrogen gas is stored in the gas supply source 26.
The damper 25 has opening / closing and flow rate adjusting functions. next,
The operation of the above device will be described.
【0026】DFF12を点火した時は、DFF12の
内圧上昇によりRTF21の内圧を上回り、燃焼廃ガス
が下部ロ−ル室14に侵入する。しかしながら、廃ガス
はシ−ル装置17により遮られ、下流側のRTF21へ
流れ込まない。また、ロ−ル室14の上流側小部屋15
の内圧が上昇すると、エジェクタ23が作動し、小部屋
15の内部ガスを吸引する。これにより、上流側小部屋
15の内圧が降下し、下流側小部屋18との差圧が維持
され、逆流が防止される。When the DFF 12 is ignited, the internal pressure of the DFF 12 rises and exceeds the internal pressure of the RTF 21, and the combustion waste gas enters the lower roll chamber 14. However, the waste gas is blocked by the seal device 17 and does not flow into the RTF 21 on the downstream side. In addition, the small room 15 on the upstream side of the roll room 14
When the internal pressure of rises, the ejector 23 operates and sucks the internal gas of the small chamber 15. As a result, the internal pressure of the upstream small chamber 15 drops, the differential pressure with the downstream small chamber 18 is maintained, and backflow is prevented.
【0027】また、このとき、ダンパ25を開け、窒素
ガスを供給源26からバイパス通路24に供給する。窒
素ガスの流入によりバイパス通路22,24を介する吸
引力が増し、小部屋15からの排気が円滑になる。な
お、ダンパ25にはリミットスイッチが設けられ、ダン
パ25は一定時間だけ開になる。At this time, the damper 25 is opened and nitrogen gas is supplied from the supply source 26 to the bypass passage 24. The inflow of nitrogen gas increases the suction force through the bypass passages 22 and 24, and the exhaust from the small chamber 15 becomes smooth. It should be noted that the damper 25 is provided with a limit switch, and the damper 25 is opened for a fixed time.
【0028】さらに、DFF12を消火したときは、R
TF21の側から多量の還元性ガスがDFF12の側へ
流れ込もうとするが、この場合も消火条件をダンパ25
の閉条件に組み込み、ダンパ25が所定時間だけ開き、
バイパス通路22,24に窒素ガスが流入するように
し、RTF21からDFF12への還元性ガスの流入を
阻止させる。Furthermore, when the DFF 12 is extinguished, R
A large amount of reducing gas tries to flow into the DFF 12 side from the TF 21 side, but in this case as well, the fire extinguishing condition is set by the damper 25.
Built in the closing condition of, the damper 25 opens for a predetermined time,
Nitrogen gas is allowed to flow into the bypass passages 22 and 24 to prevent the reducing gas from flowing from the RTF 21 to the DFF 12.
【0029】上記実施例によれば、逆流防止によりRT
F21の炉内雰囲気を維持するのみならず、RTF21
側からDFF12側への過剰なガス流入をも阻止するこ
とができるので、DFF12炉内の雰囲気が所望の雰囲
気に保たれ、非定常状態から定常状態へ円滑に運転する
ことができる。According to the above embodiment, RT is prevented by backflow prevention.
In addition to maintaining the F21 furnace atmosphere, RTF21
Since it is possible to prevent an excessive gas inflow from the DFF12 side to the DFF12 side, the atmosphere in the DFF12 furnace is maintained at a desired atmosphere, and the unsteady state can be smoothly operated to the steady state.
【0030】[0030]
【発明の効果】この発明によれば、直火加熱帯と無酸化
均熱帯との雰囲気を下部ロ−ル室のシ−ル装置により遮
断するので、無酸化均熱帯のドライな還元性雰囲気が壊
されず、鋼帯表面が清浄に保たれる。さらに、下部ロ−
ル室に侵入した廃ガスをバイパス通路を介して上部ロ−
ル室に逃がすので、無酸化均熱帯の雰囲気の保護効果が
高まる。このため、鋼帯表面の酸化を有効に防止するこ
とができ、めっき付着性が害なわれず、良好な品質のめ
っき鋼板を得ることができる。また、上部ロ−ル室にバ
イパス通路を介してガスを流入させるので、上部ロ−ル
室のロ−ルがガス冷却され、ロ−ルのピックアップが有
効に防止される。According to the present invention, since the atmosphere between the open flame heating zone and the non-oxidizing soaking zone is shut off by the seal device in the lower roll chamber, a dry reducing atmosphere of the non-oxidizing soaking zone is created. It is not broken and the surface of the steel strip is kept clean. In addition, the lower
The waste gas that has entered the chamber is routed through the bypass passage to the upper roll.
As it escapes to the room, the effect of protecting the atmosphere of non-oxidizing soaking zone is enhanced. For this reason, it is possible to effectively prevent the oxidation of the surface of the steel strip, the plating adhesion is not impaired, and it is possible to obtain a plated steel sheet of good quality. Further, since the gas is made to flow into the upper roll chamber through the bypass passage, the roll in the upper roll chamber is cooled by gas, and the pickup of the roll is effectively prevented.
【図1】この発明の実施例に係る連続焼鈍炉を示す模式
図。FIG. 1 is a schematic diagram showing a continuous annealing furnace according to an embodiment of the present invention.
【図2】従来の連続焼鈍炉を示す模式図。FIG. 2 is a schematic diagram showing a conventional continuous annealing furnace.
9;鋼帯、10;上部ロ−ル室、12;直火加熱帯(D
FF)、14;下部ロ−ル室、17;シ−ル機構、2
1;無酸化均熱帯(RTF)、22,24;バイパス通
路、23;エジェクタ、25;ダンパ、26;ガス供給
源。9: Steel strip, 10: Upper roll chamber, 12: Open flame heating zone (D
FF), 14; lower roll chamber, 17; seal mechanism, 2
1; non-oxidizing soaking zone (RTF), 22, 24; bypass passage, 23; ejector, 25; damper, 26; gas supply source.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 中村 秋彦 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 (72)発明者 田口 昇 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 (72)発明者 堤 道明 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 (72)発明者 岩崎 秀雄 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 (56)参考文献 特開 平2−236229(JP,A) 特公 昭60−46162(JP,B2) ─────────────────────────────────────────────────── ─── Continued Front Page (72) Inventor Akihiko Nakamura 1-2-1, Marunouchi, Chiyoda-ku, Tokyo Japan Steel Pipe Co., Ltd. (72) Inventor Noboru Taguchi 1-2-1 Marunouchi, Chiyoda-ku, Tokyo Inside the Steel Pipe Co., Ltd. (72) Inventor Michiaki Tsutsumi 1-2-2 Marunouchi, Chiyoda-ku, Tokyo Japan Inside Steel Pipe Co., Ltd. (72) Hideo Iwasaki 1-2-1 Marunouchi, Chiyoda-ku, Tokyo Japan Steel Pipe Incorporated (56) References JP-A-2-236229 (JP, A) JP 60-46162 (JP, B2)
Claims (1)
る直火加熱帯と、還元性雰囲気下で被処理体を均熱する
無酸化均熱帯とを有する連続焼鈍炉において、前記直火
加熱帯の上方に設けられ、被処理体を前記直火加熱帯へ
送るロ−ルを備えた上部ロ−ル室と、前記直火加熱帯の
下方に設けられ、被処理体を前記直火加熱帯から前記無
酸化均熱帯へ向かって送るロ−ルを備えた下部ロ−ル室
と、この下部ロ−ル室に設けられたシ−ル機構と、前記
下部ロ−ル室から前記上部ロ−ル室へ連通するバイパス
通路と、を有することを特徴とする連続焼鈍炉。1. A continuous annealing furnace having a direct fire heating zone for heating an object to be treated using a direct flame reducing flame, and a non-oxidizing soaking zone for soaking the object to be treated in a reducing atmosphere. An upper roll chamber provided above the fire heating zone and provided with a roll for feeding the object to be treated to the open flame heating zone, and provided below the open flame heating zone to treat the article to be treated directly A lower roll chamber provided with a roll for sending from the fire heating zone toward the non-oxidizing soaking zone, a seal mechanism provided in the lower roll chamber, and the lower roll chamber through the A continuous annealing furnace having a bypass passage communicating with the upper roll chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16834991A JPH07100826B2 (en) | 1991-07-09 | 1991-07-09 | Continuous annealing furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16834991A JPH07100826B2 (en) | 1991-07-09 | 1991-07-09 | Continuous annealing furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH059591A JPH059591A (en) | 1993-01-19 |
| JPH07100826B2 true JPH07100826B2 (en) | 1995-11-01 |
Family
ID=15866420
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16834991A Expired - Fee Related JPH07100826B2 (en) | 1991-07-09 | 1991-07-09 | Continuous annealing furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07100826B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2011040303A1 (en) * | 2009-10-01 | 2011-04-07 | 新日本製鐵株式会社 | Facility used for both continuous hot-dip coating and continuous annealing |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6046162B2 (en) | 2011-12-28 | 2016-12-14 | ラッツンデ ウント コー ゲーエムベーハーRattunde & Co Gmbh | Asymmetric gear |
-
1991
- 1991-07-09 JP JP16834991A patent/JPH07100826B2/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6046162B2 (en) | 2011-12-28 | 2016-12-14 | ラッツンデ ウント コー ゲーエムベーハーRattunde & Co Gmbh | Asymmetric gear |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH059591A (en) | 1993-01-19 |
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