JPH01215930A - Method for continuously annealing steel sheet - Google Patents
Method for continuously annealing steel sheetInfo
- Publication number
- JPH01215930A JPH01215930A JP4309488A JP4309488A JPH01215930A JP H01215930 A JPH01215930 A JP H01215930A JP 4309488 A JP4309488 A JP 4309488A JP 4309488 A JP4309488 A JP 4309488A JP H01215930 A JPH01215930 A JP H01215930A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- direct
- thin steel
- heating furnace
- steel sheet
- 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
- 229910000831 Steel Inorganic materials 0.000 title claims abstract description 85
- 239000010959 steel Substances 0.000 title claims abstract description 85
- 238000000137 annealing Methods 0.000 title claims description 36
- 238000000034 method Methods 0.000 title claims description 29
- 238000010438 heat treatment Methods 0.000 claims abstract description 88
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 15
- 239000001301 oxygen Substances 0.000 claims description 15
- 229910052760 oxygen Inorganic materials 0.000 claims description 15
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 7
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 7
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 7
- 239000001257 hydrogen Substances 0.000 claims description 7
- 229910052739 hydrogen Inorganic materials 0.000 claims description 7
- 238000007254 oxidation reaction Methods 0.000 abstract description 12
- 230000001105 regulatory effect Effects 0.000 abstract 2
- 239000000446 fuel Substances 0.000 description 14
- 239000007789 gas Substances 0.000 description 13
- 230000015572 biosynthetic process Effects 0.000 description 11
- 230000003647 oxidation Effects 0.000 description 10
- 238000010586 diagram Methods 0.000 description 9
- 238000002485 combustion reaction Methods 0.000 description 8
- 238000002791 soaking Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 238000001816 cooling Methods 0.000 description 6
- 238000002474 experimental method Methods 0.000 description 6
- 239000000567 combustion gas Substances 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000005246 galvanizing Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
Landscapes
- Heat Treatment Of Sheet Steel (AREA)
- 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〕
大発明は、連続的に搬送される冷間圧延薄鋼板(以下、
薄鋼板という)を所定温度に加熱した後、所定の焼鈍パ
ターンに沿って均熱、冷却する連続焼鈍方法に関し、特
に直火式により上記薄鋼板を加熱する際の酸化膜の生成
を回避できるようにした連続焼鈍方法に関する。[Detailed description of the invention] [Industrial field of application] The great invention is a continuously conveyed cold rolled thin steel plate (hereinafter referred to as
Regarding the continuous annealing method in which a thin steel plate (referred to as a thin steel plate) is heated to a predetermined temperature, then soaked and cooled along a predetermined annealing pattern, it is possible to avoid the formation of an oxide film when heating the thin steel plate using a direct flame method. This invention relates to a continuous annealing method.
従来、連続焼鈍炉において薄鋼板を加熱する場合は、ラ
ジアントチューブからの輻射熱を利用した間接加熱方法
が採用されていた。しかし近年では、省エネルギの観点
から上記薄鋼板を直火式バーナで直接加熱する方法が採
用されている。Conventionally, when heating thin steel sheets in a continuous annealing furnace, an indirect heating method using radiant heat from a radiant tube has been adopted. However, in recent years, from the viewpoint of energy saving, a method has been adopted in which the thin steel plate is directly heated with a direct burner.
ところで、上記直火式加熱炉に採用される直火式バーナ
は、理論空気比以下で燃料を燃焼させて、この高温で0
□濃度の低い無酸化ガスの噴流および火炎、バーナタイ
ルからの輻射により薄鋼板を加熱するように構成されて
いる。しかしながら、上記直火式バーナからの火炎には
、微量(40ppm程度)の酸素が残存していることか
ら、薄鋼板の近傍は弱酸化雰囲気と考えられ、その結果
酸化膜が生成し易いという問題がある。By the way, the direct-fired burner used in the above-mentioned direct-fired heating furnace burns fuel at a temperature below the stoichiometric air ratio, and achieves zero temperature at this high temperature.
□It is configured to heat a thin steel plate using a jet of low-concentration non-oxidizing gas, flame, and radiation from burner tiles. However, since a trace amount (approximately 40 ppm) of oxygen remains in the flame from the above-mentioned direct-fired burner, the vicinity of the thin steel plate is considered to be a weakly oxidizing atmosphere, resulting in the problem of easy formation of an oxide film. There is.
そこで、従来、上記直火式バーナによる酸化膜の付着を
抑制するために、例えば特開昭55−97432号公報
に提案されているものがある。これは、直火式加熱炉内
での薄銅板の表面温度、及び薄鋼板近傍の酸素量を検出
し、この検出表面温度、酸素量が′a鋼板表面の許容酸
化膜厚の上限値を超ることのないよう各バーナの空気比
、燃料流量を制御するものである。即ち、予め上記薄鋼
板の温度。Therefore, in order to suppress the deposition of oxide film due to the above-mentioned direct-fired burner, there has been proposed, for example, in Japanese Patent Application Laid-Open No. 55-97432. This detects the surface temperature of a thin copper plate in a direct-fired heating furnace and the amount of oxygen near the thin steel plate, and detects that the detected surface temperature and oxygen amount exceed the upper limit of the allowable oxide film thickness on the surface of the steel plate. The air ratio and fuel flow rate of each burner are controlled to prevent this. That is, the temperature of the thin steel plate is determined in advance.
雰囲気中の酸素濃度と薄鋼板表面の酸化膜厚との関係を
求め、検出酸化膜厚がこの加熱炉に続く均熱帯で還元可
能な酸化膜厚となるようなバーナの燃焼条件や薄鋼板温
度を設定し、この設定条件に基づいてバーナの空気比及
びTittiEr板の加熱炉出口温度を制御する方法で
ある。The relationship between the oxygen concentration in the atmosphere and the oxide film thickness on the surface of the thin steel sheet is determined, and burner combustion conditions and the thin steel sheet temperature are determined so that the detected oxide film thickness becomes an oxide film thickness that can be reduced in the soaking zone following this heating furnace. In this method, the air ratio of the burner and the heating furnace outlet temperature of the TittiEr plate are controlled based on the set conditions.
しかしながら、上記従来の酸素濃度及び薄鋼板温度を検
出して空気比や燃料流量を制御する方法では、酸化膜の
生成を防止しながら薄鋼板を充分に加熱するのは困難で
ある。即ち、上記公報に記載された出口温度と酸化膜厚
との関係(第6図参照)、及び02濃度と酸化膜厚との
関係(第7図参照)によれば、出口温度を高くすれば、
酸化膜厚が大幅に厚くなり、従ってこれを防止するには
0□濃度を極端に低下させなければならない。従って結
局、薄鋼板温度と02濃度だけに着目したこの従来方法
では、酸化膜厚を薄<シながら加熱炉出口温度を高くす
るには限度がある。However, with the conventional method of controlling the air ratio and fuel flow rate by detecting the oxygen concentration and the temperature of the thin steel sheet, it is difficult to sufficiently heat the thin steel sheet while preventing the formation of an oxide film. That is, according to the relationship between the outlet temperature and the oxide film thickness (see Figure 6) and the relationship between the 02 concentration and the oxide film thickness (see Figure 7) described in the above publication, if the outlet temperature is raised, ,
The oxide film thickness becomes significantly thicker, and therefore, in order to prevent this, the 0□ concentration must be extremely reduced. Therefore, in the end, with this conventional method that focuses only on the thin steel sheet temperature and O2 concentration, there is a limit to how high the heating furnace outlet temperature can be while keeping the oxide film thin.
本発明の目的は、薄鋼板の酸化膜の生成を抑制しながら
、必要な加熱炉出口温度を確保できる薄鋼板の連続焼鈍
方法を提供することにある。An object of the present invention is to provide a continuous annealing method for a thin steel sheet that can secure a necessary heating furnace exit temperature while suppressing the formation of an oxide film on the thin steel sheet.
本件発明者らは、上記目的を達成するために鋭意研究を
重ねたところ、直火式加熱による酸化膜の生成は、雰囲
気中の酸素濃度と薄鋼板の温度だけでは決定できず、こ
れに加え直火式加熱炉内の雰囲気ガス成分及び該加熱炉
での薄鋼板の加熱速度も影響していることに着目した。In order to achieve the above object, the inventors of the present invention have conducted intensive research and found that the formation of an oxide film by direct heating cannot be determined solely by the oxygen concentration in the atmosphere and the temperature of the thin steel sheet. We focused on the fact that the atmospheric gas components in the direct-fired heating furnace and the heating rate of the thin steel sheet in the heating furnace also have an effect.
特に直火式バーナにより低空気比で燃焼させても、燃焼
ガス中にはフリー酸素が未燃の状態で常に40PPm程
度存在しており、この状態における酸化膜の生成厚さは
、従来は単に薄鋼板温度が上昇するほど厚くなると考え
られていたが、実際は、雰囲気中の酸化性成分と還元性
成分とのバランス及び薄鋼板温度との関係により、所定
の温度領域でピークを示すことを見出した。さらに上記
酸化膜厚がピークを示す温度領域においては、加熱温度
により生成される酸化膜の厚さを調整できることを見出
した。In particular, even when combustion is carried out at a low air ratio using a direct-fired burner, about 40 PPm of free oxygen always exists in the unburned state in the combustion gas, and in the past, the thickness of the oxide film formed in this state was simply It was thought that the thickness of the thin steel sheet increases as the temperature rises, but it was discovered that the thickness actually peaks in a certain temperature range, depending on the balance between oxidizing and reducing components in the atmosphere and the relationship with the sheet temperature. Ta. Furthermore, it has been found that in the temperature range where the oxide film thickness peaks, the thickness of the oxide film produced can be adjusted by changing the heating temperature.
そこで、本願の特定発明は、薄鋼板を連続的に搬送しつ
つ直火式加熱炉内で所定温度に加熱し、しかる後所定の
焼鈍パターンに沿って熱処理するTR鋼板の連続焼鈍方
法において、上記直火式加熱炉の雰囲気を、例えばCO
G、LDGガスを燃料とし、空気比を0.8以下にする
ことにより、水素。Therefore, the specific invention of the present application provides a continuous annealing method for a TR steel plate, in which a thin steel plate is continuously conveyed and heated to a predetermined temperature in a direct-fired heating furnace, and then heat-treated along a predetermined annealing pattern. The atmosphere of the direct-fired heating furnace is, for example, CO
Hydrogen by using G, LDG gas as fuel and reducing the air ratio to 0.8 or less.
一酸化炭素等の還元性成分に微量の酸素を含む還元性雰
囲気に制御するとともに、上記FifA板の該直火式加
熱炉の出口温度を400℃以下、もしくは800℃以上
にすることを特徴としている。It is characterized by controlling the reducing atmosphere to include a trace amount of oxygen in reducing components such as carbon monoxide, and controlling the outlet temperature of the direct-fired heating furnace of the FifA plate to 400°C or lower or 800°C or higher. There is.
ここで出口温度を400℃以下又は800℃以上とした
のは、後述のように、還元性雰囲気下での直火加熱にお
いては、400〜800℃の温度範囲では、酸化膜厚が
大幅に厚くなるのに対し、400℃以下。The reason why the outlet temperature was set below 400°C or above 800°C is because, as described later, in direct flame heating in a reducing atmosphere, the oxide film thickness is significantly thicker in the temperature range of 400 to 800°C. However, the temperature is below 400℃.
800℃以上では加熱前(常温)の原板における酸化膜
厚と略同−にできることが判明したからである。This is because it has been found that at 800° C. or higher, the oxide film thickness can be made approximately the same as the oxide film thickness on the original plate before heating (at room temperature).
また、本願の関連発明は、上記薄鋼板の連続焼鈍方法に
おいて、上記直火式加熱炉の雰囲気を水素、一酸化炭素
等の還元性成分に微量の酸素を含む還元性雰囲気にする
とともに、上記薄鋼板の直火式加熱炉内での昇温速度を
、少なくとも400〜600℃の間は50℃/sec以
上とすることを特徴としている。Further, the related invention of the present application provides the continuous annealing method for thin steel sheets, in which the atmosphere in the direct-fired heating furnace is made into a reducing atmosphere containing a trace amount of oxygen in addition to reducing components such as hydrogen and carbon monoxide; The heating rate of the thin steel sheet in the direct-fired heating furnace is set to 50°C/sec or more at least between 400 and 600°C.
ここで、丘記400〜600℃間における昇温温度を5
0℃/sec以上としたのは、後述の説明からも明らか
なように、上記温度範囲は酸化し易い領域であり、従っ
て、少なくともこの領域を50℃/see以上とし、該
温度領域における滞在時間を可能な限り短縮することに
より酸化膜の成長を阻止できるからである。なお、上記
温度範囲以外の昇温速度は酸化膜の成長にほとんど影響
がないことから、特に限定するものではないが、勿論速
くする程処理時間を短縮できる。しかし実際にはバーナ
の配設方法や加熱能力等の問題があり、必要以上に速く
すると設備コストが過大になり、通常はむしろ遅くした
ほうがよい。Here, the heating temperature between 400 and 600℃ is 5
The reason why the above temperature range is set at 0°C/sec or higher is that, as will be clear from the explanation below, the above temperature range is a region where oxidation is easy. This is because the growth of the oxide film can be prevented by shortening as much as possible. Note that the rate of temperature increase outside the above-mentioned temperature range has almost no effect on the growth of the oxide film, and is not particularly limited, but it goes without saying that the faster the rate, the shorter the processing time can be. However, in reality, there are problems with the burner arrangement method, heating capacity, etc., and if the speed is faster than necessary, the equipment cost will be excessive, so it is usually better to slow it down.
次に、本願の特定発明における上述の数値を見出した実
験について説明する。Next, an experiment in which the above-mentioned numerical values were found in the specific invention of the present application will be explained.
この実験は、直火式バーナ用の燃料としてCOGガス及
びLDGガスを採用し、空気比を0.8とすることによ
り、燃焼ガス雰囲気を、水素、一酸化炭素等の還元性成
分に40PPm程度の微量酸素が含まれた還元性雰囲気
にするとともに、Fti板の出口温度の変化による酸化
膜厚さの変化を調べた。In this experiment, COG gas and LDG gas were used as fuel for the direct-fired burner, and by setting the air ratio to 0.8, the combustion gas atmosphere was changed to about 40 PPm of reducing components such as hydrogen and carbon monoxide. A reducing atmosphere containing a trace amount of oxygen was created, and changes in the oxide film thickness due to changes in the exit temperature of the Fti plate were investigated.
第1図はその実験結果を示す。この図は、’1ilti
@板の温度と酸化膜厚との関係を示す特性図であり、図
中、曲線aはCOGガス、曲vAbはLDGガスの特性
である。なお、加熱前の原板の酸化膜厚は20人程度で
ある。第1図から明らかになったことは、上述の還元性
雰囲気中における加熱では、薄鋼板の加熱温度が400
℃に達するまでは酸化が生しておらず、酸化未反応領域
■となっており、この領域Iを超えると酸化膜が生成し
始め、略600℃をピークとして酸化成長領域■が形成
されている。Figure 1 shows the experimental results. This figure is '1ilti
It is a characteristic diagram showing the relationship between the temperature of the @ plate and the oxide film thickness, in which the curve a is the characteristic of COG gas and the curve vAb is the characteristic of LDG gas. Note that the oxide film thickness of the original plate before heating is about 20 people. What is clear from Fig. 1 is that when heating in the above-mentioned reducing atmosphere, the heating temperature of the thin steel plate is 400°C.
Until the temperature reaches 600°C, no oxidation occurs, forming an oxidation unreacted region (■), and once this region I is exceeded, an oxide film begins to form, and an oxidized growth region (■) is formed with a peak temperature of about 600°C. There is.
そして、加熱温度が600℃を超えると還元作用が働き
始め、略800℃で酸化衰退領域■が形成され、この8
00℃を超えると略加熱以前の酸化膜厚(20人)まで
低下して還元領域■が形成されている。When the heating temperature exceeds 600°C, the reduction action begins to work, and at about 800°C, an oxidation decline region ■ is formed, and this 8
When the temperature exceeds 00.degree. C., the oxide film thickness decreases to approximately the thickness before heating (20 layers), and a reduced region (2) is formed.
いる。There is.
即ち、上記実験結果から判明したことは、還元性雰囲気
中で薄鋼板の出口温度が酸化未反応領域I、もしくは還
元領域■であれば、酸化膜厚を20Å以下にできる。こ
のことから、酸化膜の生成を防止するには、直火式加熱
炉の雰囲気を還元性雰囲気に制御するとともに、上記薄
鋼板の直火式加熱炉の出口温度を400℃以下、もしく
は800℃以上に設定してやればよいこととなる。なお
、上記薄鋼板の出口温度を800℃以上に設定した場合
は、このまま均熱帯に搬送し、しかる後冷却すればよい
。また、400℃以下に設定した場合は、上記直火式加
熱炉を予熱帯として利用し、次工程で所定の温度に加熱
した後、均熱、冷却すればよい。さらに上記薄鋼板の温
度コントロールは、バーナの燃焼量、vR鋼板の搬送速
度により調整すればよい。That is, it has been found from the above experimental results that the oxide film thickness can be reduced to 20 Å or less if the exit temperature of the thin steel sheet is in the oxidation unreacted region I or the reduced region (2) in a reducing atmosphere. Therefore, in order to prevent the formation of an oxide film, the atmosphere in the direct-fired heating furnace should be controlled to be a reducing atmosphere, and the outlet temperature of the direct-fired heating furnace for the thin steel sheet should be set to 400°C or less, or to 800°C. All you have to do is set it as above. In addition, when the outlet temperature of the thin steel plate is set to 800° C. or higher, it is sufficient to transport the thin steel plate as it is to a soaking zone and then cool it. Further, when the temperature is set to 400° C. or lower, the above-mentioned direct-fired heating furnace may be used as a preheating zone, and after heating to a predetermined temperature in the next step, soaking and cooling may be performed. Furthermore, the temperature control of the thin steel plate may be adjusted by the combustion amount of the burner and the conveyance speed of the vR steel plate.
次に本願の関連発明における上記数値を見い出した実験
について説明する。Next, an experiment in which the above numerical values were found in the related invention of the present application will be explained.
この実験では、上記特定発明における実験と同様に、直
火式バーナによる燃焼ガス雰囲気を、水素、一酸化炭素
等の還元性成分と微量酸素とからなる還元性雰囲気とし
、直火式加熱炉を通過する”a鋼板の昇温速度を変化さ
せた場合の酸化膜の表面性状について調べた。なお、上
記薄鋼板の加熱炉の出口温度は800℃以上になるよう
にした。In this experiment, similar to the experiment in the above-mentioned specific invention, the combustion gas atmosphere from the direct-fired burner was made into a reducing atmosphere consisting of reducing components such as hydrogen and carbon monoxide, and a trace amount of oxygen, and the direct-fired heating furnace was used. The surface properties of the oxide film were investigated by changing the heating rate of the passing "A" steel sheet.The outlet temperature of the heating furnace for the thin steel sheet was set to be 800° C. or higher.
第2図はその結果を示す。この図は、直火式加熱炉内で
の加熱時間と薄鋼板温度との関係を示す特性図であり、
図中、Cは昇温速度50℃/sec、 dは20℃/
secの特性を示し、○印は加熱前程度の酸化膜厚(2
0人)となった場合、X印はこれ以上の酸化膜厚になっ
た場合を示す。第2図から明らかになったことは、還元
雰囲気中での加熱では、薄鋼板の昇温速度が20℃八e
への場合は、400℃を超えると酸化膜が成長し始め出
口温度の800℃を超えても酸化膜厚は原板より厚く、
×である。これに対して50℃/secの場合は、酸化
膜は500℃、700℃付近で厚くなっているものの、
800℃を超えると原板程度となり、Oとなっている。Figure 2 shows the results. This figure is a characteristic diagram showing the relationship between heating time and thin steel plate temperature in a direct-fired heating furnace.
In the figure, C is a temperature increase rate of 50°C/sec, and d is 20°C/sec.
sec characteristics, and the circle mark indicates the oxide film thickness before heating (2
0), the mark X indicates the case where the oxide film thickness is greater than this. What has become clear from Figure 2 is that when heated in a reducing atmosphere, the temperature increase rate of the thin steel sheet is 20℃8e.
When the temperature exceeds 400°C, an oxide film starts to grow, and even if the exit temperature exceeds 800°C, the oxide film is thicker than the original plate.
×. On the other hand, in the case of 50°C/sec, although the oxide film becomes thicker around 500°C and 700°C,
When the temperature exceeds 800°C, the temperature becomes similar to that of the original plate, and it becomes O.
これは−度酸化したものが再び加熱前程度の酸化膜厚に
還元されたものと考えられる。即ち、上記実験結果から
判明したことは、薄鋼板の昇温速度を少なくとも400
〜600℃間において50℃/sec以上にすることに
より、酸化膜厚を原板程度に低減できる。This is considered to be because the oxidized material was reduced to the same oxide film thickness as before heating. That is, it was found from the above experimental results that the temperature increase rate of the thin steel plate was increased to at least 400%.
By increasing the heating rate to 50° C./sec or more between 600° C. and 600° C., the oxide film thickness can be reduced to the same level as that of the original plate.
本願の特定発明に係るFi鋼板の連続焼鈍方法によれば
、直火式加熱炉内を、還元性成分に微量の酸素を含む還
元性雰囲気とし、NfA板の直火式加熱炉の出口温度を
400℃以下、あるいは800℃以北としたので、40
0℃以下にした場合は酸化未反応頭載にあることから、
また800℃以上にした場合は一度酸化したものが再び
還元される還元領域にあることから、加熱前と同程度の
酸化膜厚の状態を確保できる。しかも上記還元性雰囲気
は、燃料をCO’G、LDGガス等の炭化水素系燃料と
するとともに、直火式バーナの空気比を0.8以下にす
ることにより実現できる。According to the continuous annealing method for Fi steel sheets according to the specific invention of the present application, the inside of the direct-fired heating furnace is made into a reducing atmosphere containing a trace amount of oxygen as a reducing component, and the outlet temperature of the direct-fired heating furnace for the NfA sheet is adjusted. Since it is below 400℃ or north of 800℃, 40
If the temperature is below 0℃, the oxidation remains unreacted, so
Furthermore, when the temperature is 800° C. or higher, the oxidized film is in the reduction region where what has been oxidized is reduced again, so it is possible to maintain the same oxide film thickness as before heating. Moreover, the above-mentioned reducing atmosphere can be realized by using a hydrocarbon fuel such as CO'G or LDG gas as the fuel and by setting the air ratio of the direct-fired burner to 0.8 or less.
また、本願の関連発明によれば、還元性雰囲気とすると
ともに、直火式加熱炉出口温度を800℃以上とし、か
つ該加熱炉内での昇温速度を、400〜600℃の間は
50℃/sec以上としたので、酸化膜生成温度領域に
おける時間が極力短かくなり、従って酸化膜の生成が抑
制され、かつ−炭酸化した薄鋼板は再び還元されること
となり、その結果加熱前と同程度の酸化膜厚の状態を確
保できる。そしてこの場合も上記特定発明と同様に、燃
料の選択、バーナの空気比、及び火力だけの調整で実現
できる。Further, according to the related invention of the present application, the reducing atmosphere is set, the outlet temperature of the direct-fired heating furnace is set to 800°C or higher, and the temperature increase rate in the heating furnace is set to 50°C between 400 and 600°C. ℃/sec or more, the time in the oxide film formation temperature region is minimized, and therefore the formation of oxide film is suppressed, and the carbonated thin steel sheet is reduced again, and as a result, the temperature is lower than that before heating. It is possible to maintain the same oxide film thickness. Also in this case, similar to the above-mentioned specific invention, it can be realized by adjusting only the selection of fuel, the air ratio of the burner, and the thermal power.
以下、本発明の実施例を図について説明する。 Hereinafter, embodiments of the present invention will be described with reference to the drawings.
まず、本発明の連続焼鈍方法を実現する連続焼鈍炉を第
4図及び第5図に示す。First, a continuous annealing furnace for realizing the continuous annealing method of the present invention is shown in FIGS. 4 and 5.
図において、1は連続焼鈍炉であり、これは入側ルーパ
2.直火式加熱炉31間接加熱式均熱帯4.5.ガスジ
ェット冷却帯6.及び図示していないが過時効処理帯、
急冷帯、出側ルーパをそれぞれ接続して構成されている
。また、上記入側ルーバ2及び各帯3〜6の上、下には
炉幅方向に多数の搬送ロール7が架設されており、薄鋼
板Wはこの各ロール7に順次巻回されている。さらに、
上記直火式加熱炉3の対向する両側壁3aには、上記薄
鋼板Wの搬送方向に沿って多数のラジアントカップ型直
火式バーナ8が挿入配設されており、この各バーナ8は
M鋼板Wに対向し、かつその火〜炎が酸3鋼板Wに直接
当たるように、これに近接して配設されている。また、
該各バーナ8には燃焼空気供給管8a及び燃料供給管8
bが接続されている。これにより薄鋼板Wは各帯2〜6
を順次通過しながら所定の焼鈍パターンに沿って熱処理
が施される。In the figure, 1 is a continuous annealing furnace, which has an entrance looper 2. Direct-fire heating furnace 31 Indirect heating soaking zone 4.5. Gas jet cooling zone6. and an overaging treatment zone (not shown),
It consists of a rapid cooling zone and an outlet looper connected to each other. Further, a large number of conveyor rolls 7 are installed above and below the input side louver 2 and each of the bands 3 to 6 in the furnace width direction, and the thin steel plate W is wound around each of the rolls 7 in sequence. moreover,
A large number of radiant cup-type direct-fired burners 8 are inserted into the opposite side walls 3a of the above-mentioned direct-fired heating furnace 3 along the conveyance direction of the thin steel sheet W, and each burner 8 has an M It is disposed opposite to the steel plate W and close to the acid 3 steel plate W so that the flame directly hits the acid 3 steel plate W. Also,
Each burner 8 has a combustion air supply pipe 8a and a fuel supply pipe 8.
b is connected. As a result, the thin steel plate W is
The heat treatment is performed according to a predetermined annealing pattern while sequentially passing through the annealing pattern.
次に、本願の特定発明による薄銅板Wの連続焼鈍方法の
一実施例について説明する。Next, an embodiment of a continuous annealing method for a thin copper plate W according to the specific invention of the present application will be described.
本実施例は、上記直火式バーナ8への燃料としてCOG
またはLDGガスを採用し、この燃料を理論空気比以下
、例えば0.8で燃焼させる。これにより水素、一酸化
炭素等の還元性成分に微量(40PPm程度)の酸素を
含む還元性雰囲気ガスが生成され、かつ火炎が薄鋼板W
に直接当たり、該鋼板Wは火炎で包まれた状態で加熱さ
れる。そしてこの場合に、上記薄鋼板Wの直火式加熱炉
3の出口温度Aが400℃以下、もしくは800℃以上
になるように、上記薄鋼板Wの搬送速度からバーナ8の
燃焼量を設定する。勿論この場合、バーナ8の燃焼量か
ら薄鋼板Wの搬送速度を設定してもよい。これにより、
上記薄鋼板Wは、直火式加熱炉3内で所定温度に加熱さ
れ後、均熱帯4.5に搬送され、しかる後冷却されるこ
ととなる。In this embodiment, COG is used as fuel for the direct-fired burner 8.
Alternatively, LDG gas is employed, and this fuel is combusted at a stoichiometric air ratio or lower, for example, 0.8. As a result, a reducing atmosphere gas containing reducing components such as hydrogen and carbon monoxide and a trace amount (about 40 PPm) of oxygen is generated, and the flame is
The steel plate W is heated while being surrounded by flame. In this case, the combustion amount of the burner 8 is set based on the conveyance speed of the thin steel sheet W so that the outlet temperature A of the direct-fired heating furnace 3 of the thin steel sheet W is 400° C. or lower or 800° C. or higher. . Of course, in this case, the conveyance speed of the thin steel plate W may be set based on the combustion amount of the burner 8. This results in
The thin steel sheet W is heated to a predetermined temperature in the direct-fired heating furnace 3, then transported to the soaking zone 4.5, and then cooled.
ここで、上記薄鋼板Wの加熱炉3の出口温度Aを800
℃以上に設定した場合は、この状態で均熱帯4.5に搬
送して、所定の焼鈍条件(例えば、600℃)で均熱し
、しかる後冷却処理を施せばよい。一方、薄鋼板Wの出
口温度Aを400℃以下に設定した場合は、上記均熱帯
4の温度を上記焼鈍条件に応じて再加熱できる温度に設
定してやればよい。Here, the outlet temperature A of the heating furnace 3 of the thin steel sheet W is set to 800.
When the temperature is set at .degree. C. or above, the material may be transported in this state to a soaking zone 4.5, soaked under predetermined annealing conditions (for example, 600.degree. C.), and then subjected to cooling treatment. On the other hand, when the outlet temperature A of the thin steel sheet W is set to 400° C. or lower, the temperature of the soaking zone 4 may be set to a temperature that allows reheating according to the annealing conditions.
このように本実施例の連続焼鈍方法によれば、直火式加
熱炉3内を、該加熱炉3に配設された直火式バーナ8か
らの燃焼ガスをH2,Co等の還元性成分に微量02を
含む還元性雰囲気とするとともに、薄tlllr板Wの
上記加熱炉3の出口温度Aを400℃以下、あるいは8
00℃以上と設定したので、薄鋼板Wの表面の酸化膜厚
は加熱前の20人程度を確保でき、表面性状の良好な薄
鋼板Wが得られる。As described above, according to the continuous annealing method of this embodiment, the combustion gas from the direct-fired burner 8 disposed in the heating furnace 3 is heated to contain reducing components such as H2 and Co. The atmosphere is reduced to a reducing atmosphere containing a trace amount of 02, and the outlet temperature A of the heating furnace 3 for the thin tllr plate W is set to 400°C or less, or 800°C or less.
Since the temperature was set at 00° C. or higher, the thickness of the oxide film on the surface of the thin steel sheet W before heating can be maintained at about 20, and the thin steel sheet W with good surface properties can be obtained.
即ち、第1図に示すように、400℃以下に設定した場
合は薄鋼板Wの表面に酸化膜が生成されることはほとん
どなく、また800℃以上に設定した場合は、−互生じ
た酸化膜も再び還元されるので、結局上述の良好な表面
性状が得られる。なお、800℃以上に設定した場合は
、第1図に示すように、酸化し易い400〜600℃の
領域■を通過させる必要があるが、この温度領域につい
ては、後述のように可能な限り短時間で上昇させるのが
よ<、50℃/sec以上の加熱速度が望ましい。That is, as shown in Fig. 1, when the temperature is set at 400°C or lower, an oxide film is hardly generated on the surface of the thin steel sheet W, and when the temperature is set at 800°C or higher, an Since the membrane is also reduced again, the above-mentioned good surface quality is finally obtained. If the temperature is set to 800°C or higher, as shown in Figure 1, it is necessary to pass through the 400-600°C region (2) where oxidation is likely to occur. It is preferable to raise the temperature in a short period of time, and a heating rate of 50° C./sec or more is desirable.
また、本実施例方法は、直火式バーナ8への燃料として
COG、LDGガスを採用し、該バーナ8の空気比を0
8以下に設定し、かつ燃焼量もしくは薄鋼板Wの搬送速
度を上記所定の出口温度Aに設定してやるだけで上記還
元性雰囲気を実現でき、酸化膜の生成を抑制でき、設備
費が増大することもない。さらに、本実施例の焼鈍方法
は、既設の連続焼鈍炉に直火式加熱炉を付加することに
より簡単に適用できる。In addition, in the method of this embodiment, COG and LDG gases are used as fuel for the direct-fired burner 8, and the air ratio of the burner 8 is set to 0.
8 or less, and by simply setting the combustion amount or the conveyance speed of the thin steel plate W to the predetermined exit temperature A, the above-mentioned reducing atmosphere can be achieved, the formation of an oxide film can be suppressed, and the equipment cost increases. Nor. Furthermore, the annealing method of this example can be easily applied by adding a direct-fired heating furnace to an existing continuous annealing furnace.
ここで、空気比を低下させると、それだけ燃料の有する
発熱量を有効に利用できず、燃料原単位が低下する。こ
れに対して本実施例では直火式バーナ8からの火炎を薄
鋼板Wに直接当て、火炎で薄鋼板Wを包んだ状態で加熱
するようにしており、それだけ加熱効率を向上できる。Here, if the air ratio is lowered, the calorific value of the fuel cannot be used effectively, and the fuel consumption rate decreases. On the other hand, in this embodiment, the flame from the direct-fired burner 8 is applied directly to the thin steel plate W, and the thin steel plate W is heated while being surrounded by the flame, so that the heating efficiency can be improved accordingly.
ちなみに従来方法では、火炎を直接薄鋼板に当てると、
該火炎中の残存0□によって酸化し易いと考え、バーナ
を薄鋼板と平行に配置したり、遠く離して配置していた
。これに対して、本発明者等の実験により、還元性雰囲
気の場合は火炎を直接当てても酸化はほとんど進行しな
いことが判明したので、上記構成を採用した。By the way, in the conventional method, if the flame is directly applied to the thin steel plate,
It was thought that the remaining 0□ in the flame would easily cause oxidation, so the burner was placed parallel to the thin steel plate or placed far away from it. On the other hand, experiments conducted by the present inventors have revealed that in a reducing atmosphere, oxidation hardly progresses even when directly exposed to flame, so the above configuration was adopted.
次に、本願の関連発明による薄鋼板Wの連続焼鈍方法の
一実施例について説明する。Next, an embodiment of a continuous annealing method for a thin steel plate W according to a related invention of the present application will be described.
本実施例では、上記実施例と同一の還元性雰囲気とする
とともに、第3図に示すような薄鋼板Wの昇温パターン
を設定した。即ち、400℃の0点から600℃のB点
までの昇温速度が50℃/secとなるように設定する
とともに、直火式加熱炉3の入口温度り点(常温)から
上記0点までの昇温速度及び上記B点から上記加熱炉3
の出口温度A点(800℃以上)までの昇温速度を上記
50℃/secより低く設定する。この場合、上記D−
C点及びB−A点の昇温速度は同一でもよく、また上記
0〜8点の50℃/secに設定してもよい。そして、
上記昇温パターンを実現する方法としては、薄鋼板Wの
搬送速度は加熱炉3のどの点においても一定であること
から、上記C−B点に対応する部分のバーナ8の火力を
大きくしたり、また該バーナ8の配設数を増やすことが
考えられる。なお、上記D−C点及びB−A点の昇温速
度をC−B点の50℃八eへより遅く設定したのは、酸
化膜厚の生成にほとんど影響がない温度領域であること
から、上記バーナ8の本数を増やしたり、火力を増大さ
せたりして燃焼コストが上昇するのを回避するためであ
る。これにより、上記薄鋼板Wは、直火式加熱炉3内で
所定温度に加熱され後、所定の焼鈍パターンに沿って均
熱、冷却されることとなる。In this example, the same reducing atmosphere as in the above example was used, and the temperature increase pattern of the thin steel plate W as shown in FIG. 3 was set. That is, the temperature increase rate from point 0 of 400°C to point B of 600°C is set to be 50°C/sec, and the rate of temperature increase from the inlet temperature point (room temperature) of the direct-fired heating furnace 3 to the above 0 point is set to be 50°C/sec. From the temperature increase rate and the above point B to the heating furnace 3
The rate of temperature increase to the outlet temperature point A (800° C. or higher) is set lower than the above 50° C./sec. In this case, the above D-
The temperature increase rate at point C and point B-A may be the same, or may be set at 50° C./sec at points 0 to 8 above. and,
As a method for realizing the above temperature increase pattern, since the conveyance speed of the thin steel plate W is constant at any point in the heating furnace 3, the heating power of the burner 8 at the portion corresponding to the above C-B point may be increased. It is also conceivable to increase the number of burners 8 provided. The reason why the temperature increase rate at points D-C and points B-A was set slower than that at point C-B at 50°C 8e is because the temperature range has almost no effect on the formation of oxide film thickness. This is to avoid an increase in combustion cost due to increasing the number of burners 8 or increasing the thermal power. Thereby, the thin steel plate W is heated to a predetermined temperature in the direct-fired heating furnace 3, and then soaked and cooled along a predetermined annealing pattern.
このように本実施例の焼鈍方法によれば、直火式加熱炉
3内を還元性雰囲気とするとともに、薄鋼板Wの昇温速
度を400−600℃の間は50℃/sec以上とした
ので、酸化し易い温度領域における時間が可能な限り短
縮され、従ってそれだけ酸化膜の生成が抑制される。ま
た、出口温度Aを800℃以上としたので一度酸化した
i鋼板Wは再び還元されてることとなり、結局酸化膜厚
を加熱前の20人程度に低減でき、上記実施例と同様の
効果が得られる。As described above, according to the annealing method of this embodiment, the inside of the direct-fired heating furnace 3 was made into a reducing atmosphere, and the temperature increase rate of the thin steel sheet W was set at 50°C/sec or more between 400 and 600°C. Therefore, the time in the temperature range where oxidation is likely to occur is shortened as much as possible, and therefore the formation of an oxide film is suppressed to that extent. In addition, since the outlet temperature A was set to 800°C or higher, the once-oxidized steel sheet W is reduced again, and the oxide film thickness can be reduced to about 20 layers before heating, and the same effect as in the above example can be obtained. It will be done.
なお、上記実施例では、連続焼鈍炉に適用した場合を例
にとって説明したが、本発明の連続焼鈍方法は連続亜鉛
メツキ設備にも適用できる。In addition, although the said Example demonstrated the case where it applied to the continuous annealing furnace as an example, the continuous annealing method of this invention can also be applied to continuous galvanizing equipment.
以上のように本発明に係る薄鋼板の連続焼鈍方法によれ
ば、直火式加熱炉の雰囲気を還元性雰囲気にするととも
に、特定発明では811A板の直火式加熱炉の出口温度
を400℃以下、もしくは800℃以上とし、関連発明
では薄鋼板の直火式加熱炉内での昇温速度を400〜6
00℃の間は十℃/sec以上とし、かつ出口温度を8
00℃以上としたので、薄鋼板の酸化膜厚を加熱前と同
程度にできる効果があり、しかも直火式バーナの空気比
と薄鋼板の加熱炉出口温度あるいは加熱速度を制御する
だけで実現できるから、設備費か増大することもない。As described above, according to the continuous annealing method for thin steel sheets according to the present invention, the atmosphere of the direct-fired heating furnace is reduced to a reducing atmosphere, and in the specific invention, the outlet temperature of the direct-fired heating furnace for 811A plate is set to 400°C. or below or above 800°C, and in the related invention, the temperature increase rate in a direct-fired heating furnace for thin steel sheets is set at 400°C to 600°C.
During 00°C, the rate should be 10°C/sec or more, and the outlet temperature should be 8°C.
00℃ or higher, it has the effect of making the oxide film thickness of the thin steel sheet the same as before heating, and this can be achieved simply by controlling the air ratio of the direct burner and the temperature at the outlet of the heating furnace for the thin steel sheet or the heating rate. Because it can be done, there is no increase in equipment costs.
第1図は本願の特定発明の成立過程を説明するための薄
鋼板温度と酸化膜厚との関係を示す特性図、第2図は関
連発明の成立過程を説明するための加熱時間と薄鋼板温
度との関係を示す特性図、第3図は関連発明の一実施例
を説明するための昇温パターンを示す図、第4図及び第
5図はそれぞれ本願発明の実施例方法を実施するための
連続焼鈍炉を示す概略構成図、第6図及び第7図はそれ
ぞれ従来の問題点を説明するための特性図である。
図において、lは連続焼鈍炉、3は直火式加熱炉、4.
5は均熱帯、6はガスジェット冷却帯(冷却)、8は直
火式バーナ、Aは出口温度、Wは8!I鋼板である。
特許出願人 株式会社 神戸製鋼所
代理人 弁理士 下 市 努
−−り寥對。2
一風W四礪 と
g母簗@9
←磁閂努始3Figure 1 is a characteristic diagram showing the relationship between thin steel plate temperature and oxide film thickness to explain the process of establishing the specific invention of the present application, and Figure 2 is a characteristic diagram showing the relationship between heating time and thin steel plate to explain the process of establishing the related invention. A characteristic diagram showing the relationship with temperature, FIG. 3 is a diagram showing a temperature increase pattern for explaining an embodiment of the related invention, and FIGS. 4 and 5 are diagrams for carrying out the embodiment method of the present invention, respectively. A schematic configuration diagram showing a continuous annealing furnace, and FIGS. 6 and 7 are characteristic diagrams for explaining conventional problems, respectively. In the figure, 1 is a continuous annealing furnace, 3 is a direct-fired heating furnace, and 4 is a continuous annealing furnace.
5 is the soaking zone, 6 is the gas jet cooling zone (cooling), 8 is the direct burner, A is the outlet temperature, and W is 8! It is an I steel plate. Patent applicant Kobe Steel Co., Ltd. Patent attorney Tsutomu Shimoichi. 2 Ippu W 4 礪 and G mother tongue @ 9 ← Tsutomuji Jikan 3
Claims (2)
バーナが配設された直火式加熱炉内で所定温度に加熱し
た後、所定の焼鈍パターンに沿って均熱、冷却するよう
にした薄鋼板の連続焼鈍方法において、上記直火式加熱
炉の雰囲気を水素、一酸化炭素等の還元性成分に微量の
酸素を含む還元性雰囲気に制御するとともに、上記薄鋼
板の該直火式加熱炉の出口温度を400℃以下、もしく
は800℃以上にすることを特徴とする薄鋼板の連続焼
鈍方法。(1) After continuously conveying a strip-shaped thin steel plate and heating it to a predetermined temperature in a direct-fired heating furnace equipped with multiple direct-fired burners, it is soaked and cooled according to a predetermined annealing pattern. In the continuous annealing method for thin steel sheets, the atmosphere of the direct-fired heating furnace is controlled to be a reducing atmosphere containing reducing components such as hydrogen and carbon monoxide, and a trace amount of oxygen, and A continuous annealing method for thin steel sheets, characterized in that the outlet temperature of a direct-fired heating furnace is set to 400°C or lower or 800°C or higher.
バーナが配設された直火式加熱炉内で所定温度に加熱し
た後、所定の焼鈍パターンに沿って均熱、冷却するよう
にした薄鋼板の連続焼鈍方法において、上記直火式加熱
炉の雰囲気を水素、一酸化炭素等の還元性成分に微量の
酸素を含む還元性雰囲気に制御するとともに、上記薄鋼
板の該直火式加熱炉の出口温度を800℃以上とし、か
つ該加熱炉内での昇温速度を、400〜600℃の間は
50℃/sec以上とすることを特徴とする薄鋼板の連
続焼鈍方法。(2) After continuously conveying a strip-shaped thin steel plate and heating it to a predetermined temperature in a direct-fired heating furnace equipped with multiple direct-fired burners, it is soaked and cooled according to a predetermined annealing pattern. In the continuous annealing method for thin steel sheets, the atmosphere of the direct-fired heating furnace is controlled to be a reducing atmosphere containing reducing components such as hydrogen and carbon monoxide, and a trace amount of oxygen, and Continuous annealing of a thin steel sheet, characterized in that the outlet temperature of a direct-fired heating furnace is 800°C or higher, and the temperature increase rate in the heating furnace is 50°C/sec or higher between 400 and 600°C. Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4309488A JPH01215930A (en) | 1988-02-24 | 1988-02-24 | Method for continuously annealing steel sheet |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4309488A JPH01215930A (en) | 1988-02-24 | 1988-02-24 | Method for continuously annealing steel sheet |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH01215930A true JPH01215930A (en) | 1989-08-29 |
Family
ID=12654250
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4309488A Pending JPH01215930A (en) | 1988-02-24 | 1988-02-24 | Method for continuously annealing steel sheet |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01215930A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009535512A (en) * | 2006-05-02 | 2009-10-01 | ファイブス シュタイン | Improvements to the rapid heating section of a continuous heat treatment line. |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5849621A (en) * | 1981-09-17 | 1983-03-23 | Otsuka Chem Co Ltd | Amorphous alkali titanate material and its preparation |
| JPS59577A (en) * | 1982-06-26 | 1984-01-05 | Masato Ito | Inertia propelled engine and inertia motor |
| JPS6145692A (en) * | 1984-08-09 | 1986-03-05 | Nec Corp | Generator of television special effect |
| JPS6231051A (en) * | 1985-03-11 | 1987-02-10 | Ricoh Co Ltd | Photomagnetic recording medium |
-
1988
- 1988-02-24 JP JP4309488A patent/JPH01215930A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5849621A (en) * | 1981-09-17 | 1983-03-23 | Otsuka Chem Co Ltd | Amorphous alkali titanate material and its preparation |
| JPS59577A (en) * | 1982-06-26 | 1984-01-05 | Masato Ito | Inertia propelled engine and inertia motor |
| JPS6145692A (en) * | 1984-08-09 | 1986-03-05 | Nec Corp | Generator of television special effect |
| JPS6231051A (en) * | 1985-03-11 | 1987-02-10 | Ricoh Co Ltd | Photomagnetic recording medium |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009535512A (en) * | 2006-05-02 | 2009-10-01 | ファイブス シュタイン | Improvements to the rapid heating section of a continuous heat treatment line. |
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