JPH0441623A - Direct-fired heating furnace for steel strip - Google Patents
Direct-fired heating furnace for steel stripInfo
- Publication number
- JPH0441623A JPH0441623A JP14741490A JP14741490A JPH0441623A JP H0441623 A JPH0441623 A JP H0441623A JP 14741490 A JP14741490 A JP 14741490A JP 14741490 A JP14741490 A JP 14741490A JP H0441623 A JPH0441623 A JP H0441623A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- direct
- heating
- steel strip
- fired
- 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.)
- Pending
Links
Landscapes
- Heat Treatment Of Strip Materials And Filament Materials (AREA)
Abstract
Description
【発明の詳細な説明】 [産業上の利用分野] この発明は鋼帯の直火加熱炉に関する。[Detailed description of the invention] [Industrial application field] This invention relates to a direct-fire heating furnace for steel strip.
この発明は、冷延深絞り鋼板、ステンレス鋼板の連続焼
鈍ライン、電磁鋼板の熱処理ライン、連続熱処理を含む
溶融めっきラインなどに利用される。The present invention is utilized in continuous annealing lines for cold-rolled deep-drawn steel sheets, stainless steel sheets, heat treatment lines for electrical steel sheets, hot-dip plating lines including continuous heat treatment, and the like.
[従来の技術]
鋼帯の連続熱処理設備では、ラジアントチューブによる
間接加熱炉に代えて直火加熱炉を備えたものがある。直
火加熱炉は、走行する鋼帯の表面に向かうバーナー群を
備えており、バーナーからの燃焼炎により鋼帯を直接加
熱する。また、バーナーとして無酸化燃焼バーナーが用
いられている。無酸化燃焼バーナーは、燃焼炎により鋼
帯を直接加熱するとともに、酸化スケールの生成を防止
し、さらにはすてに生成した酸化スケールを還元してス
ケール量を減少する。[Prior Art] Some continuous heat treatment equipment for steel strips is equipped with a direct heating furnace instead of an indirect heating furnace using a radiant tube. A direct-fire heating furnace is equipped with a group of burners directed toward the surface of a running steel strip, and directly heats the steel strip with combustion flame from the burners. Further, a non-oxidizing combustion burner is used as a burner. The non-oxidizing combustion burner directly heats the steel strip with a combustion flame, prevents the formation of oxidized scale, and further reduces the amount of scale by reducing the oxidized scale that has already been generated.
直火加熱炉ては、バーナーからの燃焼炎か乱ねないこと
か望ましい。燃焼炎か乱れると、鋼帯か燃焼炎の還元領
域に十分にさらされず、還元能力か低下することかある
。一方、直火加熱炉ては鋼帯の入側 (鋼帯の通板方向
とは反対方向)へ向かうトラフトか加わっているので、
燃焼排ガスは鋼帯入側に向かフて流れる。したがって、
鋼帯入側寄りに位置するバーナー23aの燃焼炎Fは、
第4図に示すように鋼帯出側より流れてきたバーナー2
3の燃焼カスGにより流れが乱される。燃焼炎Fの乱れ
により、上述のように還元能力か低下する。For direct-fired heating furnaces, it is desirable that the combustion flame from the burner is not disturbed. If the combustion flame is turbulent, the steel strip may not be fully exposed to the reducing area of the combustion flame, reducing its reducing ability. On the other hand, in a direct-fired heating furnace, a draft is added that goes toward the entrance side of the steel strip (in the opposite direction to the direction in which the steel strip passes).
The combustion exhaust gas flows toward the entrance side of the steel strip. therefore,
The combustion flame F of the burner 23a located closer to the steel strip entry side is
As shown in Figure 4, the burner 2 flowing from the steel strip outlet side
The flow is disturbed by the combustion scum G of No.3. Due to the turbulence of the combustion flame F, the reducing ability decreases as described above.
このような問題を解決する技術として、たとえば実開昭
59−9074号公報、特開昭59−59833号公報
あるいは特開昭62−20828号公報で開示された技
術かある。Techniques for solving such problems include those disclosed in, for example, Japanese Unexamined Utility Model Publication No. 59-9074, Japanese Unexamined Patent Publication No. 59-59833, or Japanese Unexamined Patent Publication No. 62-20828.
実開昭59−9074号公報で開示された鋼帯の直火加
熱炉は、鋼帯の長さ方向および加熱カス流の形成方向を
横断して、バーナーからの燃焼ガス流を鋼帯の幅方向に
導くための仕切りを設けている。The direct-fired heating furnace for steel strip disclosed in Japanese Utility Model Application Publication No. 59-9074 has a combustion gas flow from a burner that crosses the length direction of the steel strip and the direction in which the heated waste flow is formed. There are partitions to guide you in the right direction.
特開昭59−59833号公報で開示された鋼帯の直火
加熱炉は、加熱室の相対向する側壁の各々に、相対向す
る複数組の排ガスポートを設けている。鋼帯を加熱した
のちの燃焼排ガスは、バーナー上方に近接する上記排ガ
スポートから炉外に排出される。The direct-fire heating furnace for steel strips disclosed in Japanese Patent Application Laid-Open No. 59-59833 has a plurality of pairs of exhaust gas ports facing each other on each of the facing side walls of the heating chamber. After heating the steel strip, the combustion exhaust gas is discharged from the furnace through the exhaust gas port located above and close to the burner.
また、特開昭62−20828号公報で開示された連続
焼鈍炉では、予熱炉と直火炉との間および直火炉と間接
加熱炉との間にそれぞれ炉内ガスの移動を阻止する中間
室を設けている。また、直火炉内の燃焼排ガスを完全燃
焼させて予熱炉に内に供給するアフターバーニング室を
設けている。Furthermore, in the continuous annealing furnace disclosed in JP-A No. 62-20828, intermediate chambers are provided between the preheating furnace and the direct-fired furnace and between the direct-fired furnace and the indirect heating furnace to prevent the movement of gas in the furnace. It is set up. Additionally, an afterburning chamber is provided in which the combustion exhaust gas in the direct-fired furnace is completely combusted and supplied to the preheating furnace.
[発明が解決しようとする課題]
実開昭59−9074号公報で開示された鋼帯の直火加
熱炉は、次のような問題があった。一般に、炉体をコン
パクトにするために、鋼帯表面と炉壁面との間の間隔は
あまり大きくない、たとえば】50〜300 mm程度
である。また、炉内を高速て走行する鋼帯は、気流によ
りはためくことがある。したがって、鋼帯が仕切りに接
触して板疵を生じたり、あるいは仕切りを破損したりす
る虞れがある。[Problems to be Solved by the Invention] The direct-fire heating furnace for steel strips disclosed in Japanese Utility Model Application Publication No. 59-9074 had the following problems. Generally, in order to make the furnace body compact, the distance between the steel strip surface and the furnace wall surface is not very large, for example, about 50 to 300 mm. Additionally, the steel strip running at high speed inside the furnace may flap due to air currents. Therefore, there is a risk that the steel strip may come into contact with the partition and cause plate flaws or damage the partition.
特開昭59−5!11833号公報で開示された鋼帯の
直火加熱炉は、排ガスポートが加熱室の側壁を貫通して
おり、また貫通部の気密を必要とする。さらに、排ガス
通路を加熱室の外側に設けなければならない。したがっ
て、炉の構造が複雑になり、設備が高額となる。In the direct-fire heating furnace for steel strips disclosed in Japanese Patent Application Laid-Open No. 59-511833, the exhaust gas port penetrates the side wall of the heating chamber, and the penetrating portion needs to be airtight. Furthermore, exhaust gas channels must be provided outside the heating chamber. Therefore, the structure of the furnace becomes complicated and the equipment becomes expensive.
特開昭62−20828号公報で開示された連続焼鈍炉
では、中間室を設けているので燃焼排ガスの煙道が長く
なり、さらにはアフターバーニング室を設けているので
、設備が高額となる。さらに、中間室あるいはアフター
バーニング室を設けことにより、燃焼排カスの流路が長
くまた複雑になるのて、炉圧制御の精度および応答性が
低下し、炉圧制御か複雑、困難になる。The continuous annealing furnace disclosed in Japanese Patent Application Laid-open No. 62-20828 has an intermediate chamber, so the flue for the flue gas becomes long, and an afterburning chamber, which makes the equipment expensive. Furthermore, by providing an intermediate chamber or an afterburning chamber, the flow path for the combustion waste becomes long and complicated, which reduces the accuracy and responsiveness of furnace pressure control, making furnace pressure control complicated and difficult.
そこで、この発明は設備費の低減および炉圧制御の容易
化を図るとともに、板疵などの発生しない鋼帯の連続熱
処理設備を提供しようとするものである。Therefore, the present invention aims to reduce equipment costs, facilitate furnace pressure control, and provide continuous heat treatment equipment for steel strips that does not cause plate defects.
[課題を解決するための手段]
この発明の鋼帯の直火加熱炉は、予熱炉の出側に接続さ
れ、鋼帯に向かうバーナー群が鋼帯通板方向に沿って配
列された直火加熱炉において、ほぼ等しい長さの複数の
直火加熱帯が鋼帯通板方向に沿って配置され、隣り合う
直火加熱帯の間と前記予熱炉とを連絡する燃焼排ガスダ
クトが設けられている。[Means for Solving the Problems] The direct-fired heating furnace for steel strip of the present invention includes a direct-fired heating furnace connected to the outlet side of a preheating furnace, in which a group of burners facing the steel strip is arranged along the steel strip threading direction. In the heating furnace, a plurality of direct-fired heating zones having approximately equal lengths are arranged along the steel strip threading direction, and a combustion exhaust gas duct is provided to communicate between adjacent direct-fired heating zones and the preheating furnace. There is.
直火加熱帯の数は、直火加熱炉の炉室横断面積、バーナ
ーの燃焼容量、ドラフトの強さなどによって決められる
。直火加熱帯の数か多いほど、燃焼排ガスによるバーナ
ー燃焼炎の乱れは少ないことになるが、それだけ炉の構
造が複雑となる。The number of direct-fired heating zones is determined by the cross-sectional area of the furnace chamber of the direct-fired heating furnace, the combustion capacity of the burner, the draft strength, etc. The greater the number of direct-fired heating zones, the less disturbance of the burner combustion flame caused by the combustion exhaust gas, but the more complicated the structure of the furnace becomes.
これらの点から、直火加熱帯の数は2〜3程度が適当で
ある。直火加熱帯の長さはそれぞれ等しくしてもよいが
、互いに若干具なってもよい。From these points, it is appropriate that the number of direct flame heating zones be about 2 to 3. The lengths of the open flame heating zones may be equal to each other, or may be slightly different from each other.
燃焼排ガスダクトの横断面積は、直火加熱炉の炉室横断
面積とほぼ等しい。燃焼排ガスダクトの途中に、流量調
整弁あるいは絞り弁を設けてもよい。流量調整弁あるい
は絞り弁は、直火加熱炉から燃焼排ガスダクトを経て予
熱炉へ流れ込む燃焼排カスの流量を調整する。The cross-sectional area of the combustion exhaust gas duct is approximately equal to the cross-sectional area of the furnace chamber of the direct-fired heating furnace. A flow rate regulating valve or a throttle valve may be provided in the middle of the combustion exhaust gas duct. The flow rate adjustment valve or throttle valve adjusts the flow rate of the combustion waste flowing from the direct-fired heating furnace to the preheating furnace via the combustion exhaust gas duct.
直火加熱炉は、竪型あるいは横型であってもよい。The direct-fired heating furnace may be vertical or horizontal.
[イ乍用]
直火加熱帯が、上部加熱帯および下部加熱帯の二っであ
るとする。直火加熱炉に加わるドラフトにより燃焼排ガ
スは炉入側に向って逆流しているので、上部加熱帯の燃
焼排ガスのほとんどは、直火加熱炉の入側を軽で予熱炉
に流れ込む。一方、下部加熱帯の燃焼排カスおよび上部
加熱帯の燃焼排カスの一部 (上部加熱帯の出側寄りで
生じたもの)は、上下両加熱帯を区切る分離帯を通り、
燃焼排ガスダクトを経て予熱炉内に流れ込む。[For I] It is assumed that there are two direct flame heating zones: an upper heating zone and a lower heating zone. Because the draft applied to the direct-fired heating furnace causes the flue gas to flow back toward the entrance side of the furnace, most of the flue gas in the upper heating zone flows through the inlet side of the direct-fired heating furnace into the preheating furnace. On the other hand, the combustion waste from the lower heating zone and part of the combustion waste from the upper heating zone (generated near the exit side of the upper heating zone) pass through the separation zone that separates the upper and lower heating zones.
The flue gas flows into the preheating furnace through the flue gas duct.
上部加熱帯の入側での燃焼排ガス流量は、上下両加熱帯
を合わせた燃焼排ガス流量のほぼ1/2となり、したが
フて流速もほぼ1/2となる。この結果、上部加熱帯で
のバーナー燃焼炎の燃焼排ガス流による乱れは著しく減
少する。なお、下部加熱帯の入側での燃焼排ガス流量は
下部加熱帯で発生した燃焼排ガスの流量であるので、バ
ーナー燃焼炎の燃焼排ガス流による乱れは小さい。The flow rate of the combustion exhaust gas on the inlet side of the upper heating zone is approximately 1/2 of the combined flow rate of the combustion exhaust gas in both the upper and lower heating zones, and therefore the flow rate is also approximately 1/2. As a result, turbulence of the burner combustion flame in the upper heating zone due to the flue gas flow is significantly reduced. Note that since the flow rate of the combustion exhaust gas on the inlet side of the lower heating zone is the flow rate of the combustion exhaust gas generated in the lower heating zone, the turbulence caused by the combustion exhaust gas flow of the burner combustion flame is small.
直火加熱帯が2以上である場合も、同様であ0る。The same applies if there are two or more open heating zones.
[実施例]
第1図はこの発明の連続熱処理設備を併設した溶融めフ
き設備の概略構成図である。[Example] Fig. 1 is a schematic diagram of a melt wiping facility equipped with a continuous heat treatment facility according to the present invention.
第1図に示すように、連続熱処理設備1は予熱炉2、直
火加熱炉3、均熱炉4、徐冷炉5および急冷炉6とから
なっている。溶融めっき設備8は連続熱処理設備1に続
いて設けられており、溶融めっき糟9を備えている。As shown in FIG. 1, the continuous heat treatment equipment 1 includes a preheating furnace 2, a direct-fired heating furnace 3, a soaking furnace 4, a slow cooling furnace 5, and a rapid cooling furnace 6. The hot-dip plating equipment 8 is provided following the continuous heat treatment equipment 1 and includes a hot-dip plating bath 9.
第2図は、上記直火加熱炉3の詳細を示す縦断面図であ
る。FIG. 2 is a longitudinal sectional view showing details of the direct-fired heating furnace 3. As shown in FIG.
直火加熱炉3の入側は連結路11を介して予熱炉2に、
また出側は連絡路21を介して均熱炉 (第1図の参照
符号4)にそれぞれ接続されている。直火加熱炉3の直
火加熱帯は、上部加熱帯13および下部加熱帯14の二
つに等分されている。各加熱帯13.14は、鋼帯Sに
向かうバーナー群 (図示しない)が鋼帯通板方向に沿
って配列されている。両顎熱帯13.14の間は分離帯
】6となっている。予熱炉2と分離帯16との間に、こ
れらを連絡する燃焼排ガスダクト】8が設けられている
。燃焼排カスダクト18の断面積は、直火加熱炉3の炉
室断面積と等しくなフている。また、燃焼排ガスダクト
18には、流量調整弁19が取り付けられている。流量
調整弁19は、燃焼排ガスダクト18を経て予熱炉2へ
流れ込む燃焼排ガスbの流量を調整し、予熱炉2と分離
帯16との間の圧力差を適当な値に保持する。The inlet side of the direct-fired heating furnace 3 is connected to the preheating furnace 2 via a connecting passage 11.
Further, the outlet sides are respectively connected to soaking furnaces (reference numeral 4 in FIG. 1) via connecting passages 21. The direct-fired heating zone of the direct-fired heating furnace 3 is equally divided into two, an upper heating zone 13 and a lower heating zone 14. In each heating zone 13, 14, a group of burners (not shown) facing the steel strip S are arranged along the steel strip threading direction. Between the two-jaw tropics 13 and 14 there is a separation zone]6. A combustion exhaust gas duct 8 is provided between the preheating furnace 2 and the separation zone 16 to communicate them. The cross-sectional area of the combustion waste duct 18 is equal to the cross-sectional area of the furnace chamber of the direct-fired heating furnace 3. Further, a flow rate regulating valve 19 is attached to the combustion exhaust gas duct 18. The flow rate adjustment valve 19 adjusts the flow rate of the flue gas b flowing into the preheating furnace 2 via the flue gas duct 18, and maintains the pressure difference between the preheating furnace 2 and the separation zone 16 at an appropriate value.
上記のように構成された直火加熱炉3において、直火加
熱炉3に加わるトラフトにより燃焼排ガスは炉入側に向
って逆流しているので、上部加熱帯13の燃焼排ガスa
のほとんどは、直火加熱炉3の入側を経て予熱炉2に流
れ込む。一方、下部加熱帯14の燃焼排ガスbおよび上
部加熱帯13の燃焼排ガスaの一部は分離帯16を通り
、燃焼排ガスダクト18を経て予熱炉2内に流れ込む。In the direct-fired heating furnace 3 configured as described above, the flue gas flows backward toward the furnace entry side due to the raft applied to the direct-fired heating furnace 3, so that the flue gas a in the upper heating zone 13
Most of it flows into the preheating furnace 2 via the inlet side of the direct-fired heating furnace 3. On the other hand, part of the combustion exhaust gas b in the lower heating zone 14 and the combustion exhaust gas a in the upper heating zone 13 pass through the separation zone 16 and flow into the preheating furnace 2 via the combustion exhaust gas duct 18.
上部加熱帯13の入側ての燃焼排ガス流量は、両顎熱帯
13゜14を合わせた燃焼排ガス流量のほぼ1/2とな
のるで、上部加熱帯13でのバーナー燃焼炎の燃焼排ガ
ス流による乱れは著しく減少する。また、下部加熱帯1
4の入側ての燃焼排ガス流量は下部加熱帯14で発生し
た燃焼排ガスの流量であるので、バーナー燃焼炎の燃焼
排ガス流による乱れは小さい。The flue gas flow rate at the entrance side of the upper heating zone 13 is approximately 1/2 of the combined flue gas flow rate of both jaws 13 and 14, and is due to the flue gas flow of the burner combustion flame in the upper heating zone 13. Disturbances are significantly reduced. In addition, lower heating zone 1
Since the combustion exhaust gas flow rate on the inlet side of No. 4 is the flow rate of the combustion exhaust gas generated in the lower heating zone 14, the turbulence caused by the combustion exhaust gas flow of the burner combustion flame is small.
第3図は、上記直火加熱炉3を含む設備により亜鉛溶融
めっきした製品のめっき評価例を、従来の直火加熱炉に
よる場合と比較して示している。FIG. 3 shows an example of plating evaluation of a product hot-dipped with zinc using equipment including the above-mentioned direct-fired heating furnace 3, in comparison with a case using a conventional direct-fired heating furnace.
この発明による場合、めっき原板のスケール厚は100
人てあり、めっき原板のスケール付着によるめっき疵は
、はとんと発生しながった。これに対して、従来の直火
加熱炉てはめっき原板のスケール厚が1000人であっ
た。なお、直火加熱炉に設けられたハースロールに、め
っき原板のスケールが付着することもなかフた。According to this invention, the scale thickness of the plating original plate is 100
As a result, plating defects due to scale adhesion on the plating original plate hardly occurred. On the other hand, in a conventional direct-fired heating furnace, the scale thickness of the plated original plate was 1000 mm. Additionally, scale from the plating original plate did not adhere to the hearth roll installed in the direct-fired heating furnace.
[発明の効果]
この発明によれば、燃焼排ガスダクトにより燃焼排ガス
の一部を抽気して予熱炉にバイパスし、上部の直火加熱
帯を流れる燃焼排カス流量を減らして、燃焼炎の乱れを
防ぐようにしている。したかって、加熱室の外側の排ガ
ス通路、加熱室内の什切り、中間室あるいはアフターバ
ーニング室を設ける必要はないのて、炉体の構造は簡単
になり、設備費の低減を図ることができ、さらには炉圧
制御か容易となる。また、加熱室内に仕切りなどの突出
物かないために、鋼帯が突出物に突き当たって疵を生じ
るようなこともない。[Effects of the Invention] According to the present invention, a part of the combustion exhaust gas is extracted by the combustion exhaust gas duct and bypassed to the preheating furnace, and the flow rate of the combustion exhaust gas flowing through the upper direct-fired heating zone is reduced, thereby reducing the turbulence of the combustion flame. I try to prevent this. Therefore, there is no need to provide an exhaust gas passage outside the heating chamber, a cutoff inside the heating chamber, an intermediate chamber, or an afterburning chamber, so the structure of the furnace body is simplified, and equipment costs can be reduced. Furthermore, furnace pressure control becomes easier. Further, since there are no protruding objects such as partitions in the heating chamber, there is no possibility that the steel strip will hit against any protruding objects and cause flaws.
第1図はこの発明の直火加熱炉を含む連続熱処理設備を
併設した溶融めフき設備の概略構成図、第2図は第1図
に示す連続熱処理設備の直火加熱炉の縦断面図、第3図
はこの発明の直火加熱炉を含む設備により亜鉛溶融めっ
きした製品のめっき評価例を、従来の直火加熱炉による
場合と比較して示す線図、および第4図はバーナーから
の燃焼炎が燃焼排ガスにより乱される状態を説明する図
面である。
1・・・連続熱処理設備、2・・・予熱炉2.3・・・
直火加熱炉、4・・・均熱炉、5・・・徐冷炉、6・・
・急冷炉、8・・・溶融めフき設備、9・・・溶融めっ
き槽、月・・・連絡路、I 3−・・上部加熱帯、+
4−・・下部加熱帯、】6・・・分離帯、I8・・・燃
焼排ガスダクト、19−・・流量調整弁、21・・・連
絡路、23−・・バーナー a−上部加熱帯の燃焼排ガ
ス、b・・・下部加熱帯の燃焼排ガス、F−・バーナー
からの燃焼炎、G・・・燃焼排ガス、S・・・鋼帯。Fig. 1 is a schematic configuration diagram of a melt-blanking facility equipped with continuous heat treatment equipment including a direct-fired heating furnace of the present invention, and Fig. 2 is a vertical cross-sectional view of the direct-fired heating furnace of the continuous heat treatment equipment shown in Fig. 1. , Fig. 3 is a diagram showing an example of plating evaluation of a product hot-dipped with zinc using the equipment including the direct-fired heating furnace of the present invention, in comparison with a case using a conventional direct-fired heating furnace, and Fig. 4 is a diagram illustrating the results of plating evaluation from the burner. 2 is a diagram illustrating a state in which a combustion flame of a combustion engine is disturbed by combustion exhaust gas. 1... Continuous heat treatment equipment, 2... Preheating furnace 2.3...
Direct-fired heating furnace, 4... Soaking furnace, 5... Slow cooling furnace, 6...
・Quiet cooling furnace, 8...Hot-dip coating equipment, 9...Hot-dip plating tank, Moon...Connection path, I 3-...Upper heating zone, +
4--Lower heating zone, ]6--Separation zone, I8--Combustion exhaust gas duct, 19--Flow rate adjustment valve, 21--Connection path, 23--Burner a--Upper heating zone Combustion exhaust gas, b: Combustion exhaust gas from the lower heating zone, F-: Combustion flame from the burner, G: Combustion exhaust gas, S: Steel strip.
Claims (1)
が鋼帯通板方向に沿って配列された直火加熱炉において
、ほぼ等しい長さの複数の直火加熱帯が鋼帯通板方向に
沿って配置され、隣り合う直火加熱帯の間と前記予熱炉
とを連絡する燃焼排ガスダクトが設けられていることを
特徴とする鋼帯の直火加熱炉。1. In a direct-fired heating furnace connected to the outlet side of the preheating furnace and in which a group of burners facing the steel strip are arranged along the steel strip threading direction, a plurality of direct-fired heating strips of approximately equal length are connected to the steel strip threading direction. A direct-fired heating furnace for steel strip, characterized in that a combustion exhaust gas duct is arranged along the plate direction and communicates between adjacent direct-fired heating zones and the preheating furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14741490A JPH0441623A (en) | 1990-06-07 | 1990-06-07 | Direct-fired heating furnace for steel strip |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14741490A JPH0441623A (en) | 1990-06-07 | 1990-06-07 | Direct-fired heating furnace for steel strip |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0441623A true JPH0441623A (en) | 1992-02-12 |
Family
ID=15429766
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14741490A Pending JPH0441623A (en) | 1990-06-07 | 1990-06-07 | Direct-fired heating furnace for steel strip |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0441623A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015511995A (en) * | 2012-03-09 | 2015-04-23 | バオシャン アイアン アンド スティール カンパニー リミテッド | Method for producing normalized silicon steel substrate |
-
1990
- 1990-06-07 JP JP14741490A patent/JPH0441623A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015511995A (en) * | 2012-03-09 | 2015-04-23 | バオシャン アイアン アンド スティール カンパニー リミテッド | Method for producing normalized silicon steel substrate |
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