JPS6254375B2 - - Google Patents
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- JPS6254375B2 JPS6254375B2 JP57114069A JP11406982A JPS6254375B2 JP S6254375 B2 JPS6254375 B2 JP S6254375B2 JP 57114069 A JP57114069 A JP 57114069A JP 11406982 A JP11406982 A JP 11406982A JP S6254375 B2 JPS6254375 B2 JP S6254375B2
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- overaging
- sec
- temperature
- minutes
- cooling
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Description
本発明は、絞り用冷延鋼帯の連続焼鈍方法に関
するもので、熱サイクルを最適化することにより
短時間の過時効処理で耐時効性の優れた鋼板を製
造することを目的とする。
従来、絞り用冷延鋼帯の連続焼鈍方法は、短時
間加熱・均熱工程、急速冷却工程、過時効工程の
連続した3工程により構成されていることは周知
である。
この連続焼鈍方法の開発過程において、前記3
工程のそれぞれに対しさまざまな提案がなされて
いるけれども、プロセス上最も特徴を発揮し得る
工程は急速冷却工程から過時効工程に至る処理工
程であり、ハード(装置)、ソフト(熱サイク
ル)の両面からこの工程に関しても多くの提案が
なされている。その基本となる2つの方法を次に
挙げる。
(i) 特公昭49−1969号の提案の方法では、焼鈍後
しかるべき温度から墳流水中に鋼帯を焼き入れ
し、一旦鋼中固溶Cを高過飽和状態としたの
ち、所定の温度(過時効処理温度)まで再加
熱・均熱することにより、固溶Cの過飽和度を
よりどころ(起動源)として固溶C短時間析出
を図るものである。
(ii) 特公昭51−5335号の提案の方法では、焼鈍後
ガスジエツト冷却にて所定の過時効温度まで冷
却した後、その温度で均熱することにより、固
溶Cの析出を図ろうとしている。この方法で
は、焼鈍温度からの冷却が前記(i)に比べて緩慢
なため、過時効処理開始時点での固溶Cの過飽
和度が低く、C析出のよりどころ(起動源)と
するには低過ぎるため、前記(i)の方法に比べて
過時効処理時間を長くとる必要がある。
上記2つの従来の基本的方法に加えて、冷却媒
体を温水とする方法、アルコールとする方法、水
冷したロールに接触させて冷却する方法、ガスと
水の混合状態であるミストを冷媒とする方法、な
ど種々の冷却方法も提案されているけれども、基
本的な考え方は、如何に焼鈍均熱温度からエネル
ギー的に有利に急冷を行ない、フエライト中の固
溶Cを非平衡状態で過時効温度まで持続させ、短
時間の過時効処理によつて固溶Cの析出を図る
か、ということであり、上記の2つの従来の基本
的方法における熱サイクルと熱処理パターンは結
局同一思想に基づくものである。
そして、従来上記2つの基本的熱サイクルにつ
いて、材質上、鋼成分上、プロセス上、エネルギ
ー上の観点から、改善技術が提案されていた。そ
の多くは過時効処理の最適化を目的としてなされ
たものではあるが、過飽和固溶C状態からの固溶
Cの析出という技術的思想に基づいてこれらを統
一的に最適化しようとする試みはなされていない
のは現状である。
本発明は上述の従来技術の問題点に鑑み、焼鈍
均熱温度からの冷却速度により、過時効過程での
固溶Cの析出サイトが変る、すなわち水焼入れの
如く速い冷却速度のもと(過砲和固溶Cが多い)
では、フエライト粒内に微細炭化物として析出
し、ガスジエツト冷却の如く遅い冷却速度のもと
(過飽和固溶Cが小ない)では、フエライト粒界
に析出する、という根本的な違いを配慮し、各々
の条件下で固溶Cの析出を最も速かに進行させる
ための最適過時効サイクルについて規定するもの
である。
本発明は、絞り用冷延鋼帯の連続焼鈍方法に関
するもので、特に短時間過時効処理で鋼中固溶C
を十分に析出させることを主眼としている。
本発明は、加熱焼鈍後、均熱帯以降の一次平均
冷却速度v(℃/秒)にて冷却終点温度Ts
(℃)迄冷却後、過時効開始温度T1(℃)より過
時効終了温度T2(℃)に至る時間t(分)過時
効処理する冷延鋼帯の熱サイクルにおいて、下記
に示す(1)〜(3)条件の中から選ばれた1条件で連続
焼鈍する鋼帯の連続焼鈍方法であり、その条件
は、
(1) v300℃/秒
Ts<T1;T1500℃;T2200℃T1−T2
50℃;1分t5分;−0.5T2+500℃T1
−0.5T2+650℃
(2) v<300℃/秒
0T1−Ts<50℃;T1450℃;T2320
℃;0T1−T250℃;2分t5分;
(3) 50℃/秒v<300℃/秒
T1−Ts50℃;T1450℃;T2300℃;0
T1−T270℃;1分t5分;
である。
次に、本発明を構成する要件について、実施例
に基づいて詳細に説明する。
本発明は、既に説明した通り、連続焼鈍熱サイ
クルの内、所定の過時効処理前の冷却速度と冷却
終点温度の組合せのもとで、過時効開始温度、過
時効終了温度、過時効時間を規定するものであつ
て、その前の加熱、均熱条件は、本質的に本発明
の効果を損うものではなく、通常の連続焼鈍熱サ
イクル、つまり再結晶温度以上での加熱焼鈍をす
るものである点については従来と変りがない。
さて、連続焼鈍において、焼鈍均熱後の冷却速
度と過時効効果との間に密接な関係があることは
良く知られている。即ち、冷却速度を速めること
は、冷却途中でのフエライト中固溶Cの析出を阻
止し、過時効前の固溶Cの過飽和度を高める結果
となり、所定の過時効温度で保持した場合、より
短時間で固溶Cが析出する。第1図は前記の関係
を、後に示す第1表中の鋼1を素材として示した
ものであり、現場出鋼材を熱延後200℃で巻取つ
た鋼帯を0.8mmまで冷圧し、急速加熱焼鈍炉にて
700℃に加熱焼鈍後、平均冷却速度約20〜約1500
℃/秒の冷却条件で室温まで冷却した後、350℃
まで再加熱保持して過時効処理をした場合と、
350℃まで冷却して均熱過時効処理を行つた場合
の一次冷却速度と、350℃で均熱後空冷したとき
得られる時効指数(8%引張り変形後100℃×1
時間時効して再び引張り変形を加えたときの応力
上昇量で評価)が4Kgf/mm2未満となるに要する
均熱時間および過時効終了時にフエライト粒内に
観察される微細析出炭化物の数の関係を示したも
のである。この第1図から明らかなように過時効
処理過程での固溶Cの析出速度は、一次冷却速度
および過時効前の過冷却に大きく依存する。これ
は過飽和固溶Cの増大に伴うフエライト粒内への
炭化物析出により、固溶Cの平均析出経路が短く
なつたことに他ならない。
本発明は、上記実験の知見に基づき、微細炭化
物が認められず固溶Cが主として粒界に析出する
ような一次冷却速度の遅い場合、ほとんどの固溶
Cが粒内に微細析出するような一次冷却速度の速
い場合、両者の中間的な一次冷却速度の場合の3
つの状態について過時効熱サイクルを最適化しよ
うとするものである。
第2〜5図は過時効開始温度T1と過時効終了
温度T2の最適組合せを見極めるための図であ
る。こられの図はいずれも第1図と同一条件で
熱、冷延した鋼1を、各々第11図A〜Dに示す
熱サイクルで焼鈍したときの等時効指数曲線を示
したものである。
第2〜5図の結果から、粒内析出炭化物が存在
する場合、T1からT2に温度勾配を持たせた方が
好ましく(第2図)、粒内析出炭化物が存在しな
い場合(第3図)および粒内析出炭化物が少ない
場合(第4図)はT1T2の状態で過時効するの
が好ましい。さらに第4図の条件でT1前にTs
(250℃)まで過冷を行つた場合(第5図)は時
効指数の低下が認められる。本発明は、基本的に
は後述する過時効時間、過冷条件に加えて、これ
らT1とT2の最適組合せについて規定することを
骨子とする。
第6図は、上述した時効指数が最低になるT1
とT2の組合せのもとで、T1からT2に至る時間を
変えたときの時効指数変化を示したものである。
本来、時効指数は低い方が好ましく、その意味
からは出来る限り長い時間過時効処理をするのが
好ましい。しかし、連続焼鈍ラインとしては必要
以上の過時効処理はラインの長大化を招くので好
ましくない。また一方、連続焼鈍では熱サイクル
だけで時効指数を0とすることが不可能であるか
ら、実用上歪時効が問題とならないと考えられる
時効指数レベル以下で割切る必要がある。
本発明では上記の観点から時効指数4Kgf/mm2
未満を前提として第6図から一次冷却速度が300
℃/秒以上の場合は過時効時間tを1分から5分
に、一次冷却速度が300℃/秒未満の場合は過時
効時間tを2分から5分に、一次冷却速度が300
℃/秒未満50℃/秒以上の場合は過時効時間tを
1分から5分に、夫々規定した条件の中から1条
件を選択するものである。
第1図、第5図、第6図に示す時効指数低下に
対する過冷の効果は第7図に示す通りである。こ
の図は第1図と同一前処理条件で、過時効前冷却
速度が50℃/秒と、200℃/秒の条件について、
過冷度(T1=350〜400℃の場合についての一次
冷却終点温度TsとT1の差ΔT)と粒内析出炭化
物数の関係を示したもので、過冷度が50℃以上の
場合は、粒内析出炭化物数が増大することがわか
る。これは過冷によつて固溶Cの析出サイトが増
大したことによるもので、50℃/秒以上の過冷で
は、たとえ一次冷却速度が遅くとも固溶Cの析出
速度を速めることが可能であることを示してい
る。そこで、本発明では冷延鋼帯の熱サイクルの
条件として、平均一次冷却速度が300℃/秒以上
の場合、平均一次冷却速度が300℃/秒未満で過
冷度が50℃未満の場合、平均一冷却速度が50℃/
秒以上300℃/秒未満で過冷度が50℃以上の場合
の3つのケースについてそれぞれ第8〜10図に
示すT1とT2の組合せ領域を規定しこれらの熱サ
イクルの条件の中から1条件を選択するものであ
る。
第1表は本発明の実施例に用いた鋼の化学組成
を示し、第2〜5表は第1表の鋼1、2を、本発
明で規定するTs、T1、T2、t、の熱サイクルに
よつて連続焼鈍した場合に如何なる材質が得られ
るかにつき、従来法と対比して示した。は本発
明法によるもの、Cは従来法によるものである。
尚、第2表における一次冷却速度は約1500℃/秒
(560℃水冷)であり、第3表における一次冷却速
度は約30℃/秒(ガスジエツト)であり、第4表
における一次冷却速度は約200℃/秒(ミスト)
であり、第5表における一次冷却速度は約200
℃/秒(ミスト)である。又、第2〜5表におけ
る引張り試験値はJISNo.5試験片によつている。
第2〜5表から明らかなように、いずれの表に
おいても本発明で規定するTs、T1、T2、t、を
すべて満足したときにのみ低い時効指数と優れた
材質が得られたことがわかる。
The present invention relates to a continuous annealing method for cold-rolled steel strip for drawing, and aims to produce a steel sheet with excellent aging resistance through short-time overaging treatment by optimizing the thermal cycle. It is well known that the conventional continuous annealing method for cold-rolled steel strip for drawing consists of three successive steps: a short-time heating/soaking step, a rapid cooling step, and an overaging step. In the process of developing this continuous annealing method,
Although various proposals have been made for each process, the process that can demonstrate the most distinctive characteristics is the treatment process from the rapid cooling process to the overaging process, which is both hard (equipment) and soft (thermal cycle). Many proposals have been made regarding this process. The two basic methods are listed below. (i) In the method proposed in Japanese Patent Publication No. 49-1969, after annealing, the steel strip is quenched in flowing water at an appropriate temperature to bring the solid solute C in the steel into a highly supersaturated state, and then heated to a predetermined temperature ( By reheating and soaking to the temperature (overaging treatment temperature), solid solute C is precipitated in a short time using the supersaturation degree of solid solute C as a basis (starting source). (ii) The method proposed in Japanese Patent Publication No. 51-5335 attempts to precipitate solid solution C by cooling to a predetermined overaging temperature by gas jet cooling after annealing and then soaking at that temperature. . In this method, cooling from the annealing temperature is slower than in (i) above, so the degree of supersaturation of solid solute C at the start of overaging treatment is low, making it difficult to use as a starting point for C precipitation. Since it is too low, it is necessary to take a longer overaging treatment time than in the method (i) above. In addition to the two conventional basic methods mentioned above, a method using hot water as the cooling medium, a method using alcohol, a method of cooling by contacting with a water-cooled roll, and a method using mist, which is a mixture of gas and water, as the refrigerant. Although various cooling methods such as The problem is whether to continue the aging process and to precipitate solid solution C through short-term over-aging treatment.The heat cycles and heat treatment patterns in the two basic conventional methods mentioned above are ultimately based on the same idea. . Conventionally, techniques for improving the above two basic thermal cycles have been proposed from the viewpoints of material, steel composition, process, and energy. Although most of these have been made for the purpose of optimizing overaging treatment, no attempt has been made to optimize them in a unified manner based on the technical idea of precipitation of solid solution C from a supersaturated solid solution C state. The current situation is that nothing has been done. In view of the above-mentioned problems of the prior art, the present invention has been developed in which the precipitation site of solid solution C changes during the overaging process depending on the cooling rate from the annealing soaking temperature. There is a lot of solid solution C)
Now, we will consider the fundamental difference that carbides precipitate within ferrite grains as fine carbides, and precipitate at ferrite grain boundaries under slow cooling rates such as gas jet cooling (where the amount of supersaturated solid solute C is small). This article specifies the optimum overaging cycle for the fastest precipitation of solid solution C under these conditions. The present invention relates to a continuous annealing method for cold-rolled steel strip for drawing, and in particular to a method for continuously annealing a cold-rolled steel strip for drawing, and in particular to a method for continuously annealing cold-rolled steel strip for drawing, and in particular to a method for continuously annealing a cold-rolled steel strip for drawing.
The main objective is to sufficiently precipitate the In the present invention, after heating and annealing, the cooling end point temperature T s is determined at the primary average cooling rate v (°C/sec) after the soaking zone.
After cooling to (℃), the time t (minutes) from the overaging start temperature T 1 (℃) to the overaging end temperature T 2 (℃) is shown below in the thermal cycle of the cold rolled steel strip that is overaged. This is a continuous annealing method for a steel strip that is continuously annealed under one condition selected from conditions 1) to (3), and the conditions are: (1) v300°C/sec T s < T 1 ; T 1 500°C; T 2 200℃T 1 −T 2
50℃; 1 minute t5 minutes; -0.5T 2 +500℃T 1
−0.5T 2 +650℃ (2) v<300℃/sec 0T 1 −T s <50℃; T 1 450℃; T 2 320
℃; 0T 1 -T 2 50℃; 2 minutes t5 minutes; (3) 50℃/sec v<300℃/sec T 1 -T s 50℃; T 1 450℃; T 2 300℃; 0
T 1 −T 2 70°C; 1 minute t5 minutes; Next, the requirements constituting the present invention will be explained in detail based on examples. As already explained, the present invention provides an overaging start temperature, an overaging end temperature, and an overaging time under a combination of a predetermined cooling rate and cooling end point temperature before overaging treatment in a continuous annealing thermal cycle. The heating and soaking conditions before heating and soaking conditions do not essentially impair the effects of the present invention, and the normal continuous annealing thermal cycle, that is, heating and annealing at a temperature higher than the recrystallization temperature. There is no difference from the conventional method in that respect. Now, in continuous annealing, it is well known that there is a close relationship between the cooling rate after annealing soaking and the overaging effect. In other words, increasing the cooling rate prevents the precipitation of solid solute C in ferrite during cooling and increases the degree of supersaturation of solid solute C before overaging. Solid solution C precipitates in a short time. Figure 1 shows the above relationship using Steel 1 in Table 1, which will be shown later, as a raw material.The steel strip was hot-rolled at 200°C and then cold-pressed to 0.8 mm, and then rapidly rolled. In a heating annealing furnace
After heating and annealing to 700℃, the average cooling rate is about 20 to about 1500
After cooling to room temperature at ℃/sec cooling condition, 350℃
In the case of overaging treatment by reheating and holding until
The primary cooling rate when cooling to 350℃ and soaking overaging treatment, and the aging index obtained when soaking and air cooling at 350℃ (100℃ x 1 after 8% tensile deformation)
Relationship between the soaking time required for the stress increase (evaluated by the amount of stress increase when tensile deformation is applied again after time aging) to be less than 4 Kgf/mm 2 and the number of fine precipitated carbides observed in the ferrite grains at the end of over-aging. This is what is shown. As is clear from FIG. 1, the precipitation rate of solid solution C during the overaging treatment process largely depends on the primary cooling rate and the supercooling before overaging. This is nothing but the fact that the average precipitation path of solid solute C became shorter due to the precipitation of carbides within the ferrite grains as the amount of supersaturated solid solute C increased. Based on the findings of the above experiments, the present invention is based on the findings of the present invention that, when the primary cooling rate is slow such that no fine carbides are observed and solute C is mainly precipitated at grain boundaries, most of the solute C is finely precipitated within the grain boundaries. When the primary cooling rate is high, and when the primary cooling rate is intermediate between the two, 3.
The purpose of this study is to optimize the overaging thermal cycle for two conditions. Figures 2 to 5 are diagrams for determining the optimal combination of overaging start temperature T1 and overaging end temperature T2 . These figures all show equal aging index curves when steel 1 hot- and cold-rolled under the same conditions as in FIG. 1 is annealed in the thermal cycles shown in FIGS. 11A to 11D, respectively. From the results in Figures 2 to 5, it is clear that when there are intragranular precipitated carbides, it is better to have a temperature gradient from T 1 to T 2 (Figure 2), and when there are no intragranular precipitated carbides (T 3 (Fig. 4) and when there are few intragranular precipitated carbides (Fig. 4), it is preferable to overage in the state of T 1 T 2 . Furthermore, under the conditions shown in Figure 4, T s before T 1
When supercooling is performed to (250℃) (Figure 5), a decrease in the aging index is observed. The main point of the present invention is basically to define the optimum combination of T 1 and T 2 in addition to the overaging time and supercooling conditions described later. Figure 6 shows T 1 where the above-mentioned aging index is the lowest.
This figure shows the aging index change when changing the time from T 1 to T 2 under the combination of and T 2 . Originally, it is preferable that the aging index is low, and from that point of view, it is preferable to carry out the aging treatment for as long as possible. However, for a continuous annealing line, excessive aging treatment is not preferable because it increases the length of the line. On the other hand, in continuous annealing, it is impossible to reduce the aging index to 0 just by thermal cycling, so it is necessary to divide the aging index below the level at which strain aging is considered not to be a problem in practice. In the present invention, from the above point of view, the aging index is 4Kgf/mm 2
From Figure 6, assuming that the primary cooling rate is less than 300
If the primary cooling rate is 300°C/sec or more, set the overaging time t to 1 to 5 minutes, and if the primary cooling rate is less than 300°C/sec, set the overaging time t to 2 to 5 minutes.
In the case of less than 50° C./second and more than 50° C./second, one condition is selected from among the respective prescribed conditions, with the overaging time t being 1 minute to 5 minutes. The effect of supercooling on the aging index reduction shown in FIGS. 1, 5, and 6 is as shown in FIG. 7. This figure shows the same pretreatment conditions as in Figure 1, with cooling rates before overaging of 50°C/sec and 200°C/sec.
This graph shows the relationship between the degree of supercooling (the difference ΔT between the primary cooling end point temperature T s and T 1 when T 1 = 350 to 400°C) and the number of precipitated carbides in the grains. It can be seen that the number of intragranular precipitated carbides increases when This is due to the increase in the number of precipitation sites for solute C due to supercooling, and with supercooling of 50°C/sec or more, it is possible to accelerate the precipitation rate of solute C even if the primary cooling rate is slow. It is shown that. Therefore, in the present invention, the conditions for thermal cycling of cold rolled steel strip are: when the average primary cooling rate is 300°C/second or more, when the average primary cooling rate is less than 300°C/second and the degree of subcooling is less than 50°C, Average cooling rate is 50℃/
For the three cases in which the degree of supercooling is 50°C or more at a rate of 300°C/second or more and less than 300°C/second, the combination areas of T 1 and T 2 shown in Figures 8 to 10 are defined, and the combinations of T 1 and T 2 are determined from among these thermal cycle conditions. One condition is selected. Table 1 shows the chemical compositions of the steels used in the examples of the present invention, and Tables 2 to 5 show the chemical compositions of steels 1 and 2 in Table 1, with respect to T s , T 1 , T 2 , t specified in the present invention. What kind of material can be obtained by continuous annealing through thermal cycles of , is shown in comparison with the conventional method. C is obtained by the method of the present invention, and C is obtained by the conventional method.
The primary cooling rate in Table 2 is approximately 1500°C/sec (560°C water cooling), the primary cooling rate in Table 3 is approximately 30°C/sec (gas jet), and the primary cooling rate in Table 4 is Approx. 200℃/sec (mist)
The primary cooling rate in Table 5 is approximately 200
°C/sec (mist). Moreover, the tensile test values in Tables 2 to 5 are based on JIS No. 5 test pieces. As is clear from Tables 2 to 5, in all tables, a low aging index and excellent material quality were obtained only when all of T s , T 1 , T 2 , and t specified by the present invention were satisfied. I understand that.
【表】【table】
【表】【table】
【表】【table】
【表】【table】
第1図は過時効前冷却速度と、時効指数<4Kg
f/mm2となる350℃での過時効時間及びそのとき
認められる粒内析出炭化物数の関係を示すグラフ
であり、第2図〜第5図はそれぞれ熱処理A−D
において得られる鋼板の等時効指数を示すグラフ
であり、第6図は本発明に基づくT1とT2の組合
せによる過時効時間と時効指数の関係を示すグラ
フであり、第7図は一次冷却速度が200℃/秒と
50℃/秒のときの過時効前過冷度(ΔT)と過時
効後の粒内析出炭化物数の関係を示すグラフであ
り、第8図〜第10図は本発明におけるT1とT2
の組合せ範囲を示すグラフであり、第11図A−
Dは夫々前記第2図〜第5図の熱サイクルを示す
グラフである。
Figure 1 shows the cooling rate before overaging and the aging index <4Kg
This is a graph showing the relationship between the overaging time at 350°C resulting in f/mm 2 and the number of intragranular precipitated carbides observed at that time.
FIG. 6 is a graph showing the relationship between overaging time and aging index for the combination of T 1 and T 2 based on the present invention, and FIG. Speed is 200℃/sec
It is a graph showing the relationship between the degree of supercooling before overaging (ΔT) and the number of intragranular precipitated carbides after overaging at 50°C/sec, and FIGS. 8 to 10 are graphs showing the relationship between T 1 and T 2 in the present invention.
11 is a graph showing the combination range of FIG.
D is a graph showing the thermal cycles of FIGS. 2 to 5, respectively.
Claims (1)
v(℃/秒)にて冷却終点温度Ts(℃)迄冷却
後、過時効開始温度T1(℃)より過時効終了温
度T2(℃)に至る時間t(分)過時効処理する
冷延鋼帯の熱サイクルにおいて、下記に示す(1)〜
(3)条件の中から選ばれた1条件で連続焼鈍するこ
とを特徴とする鋼帯の連続焼鈍方法。 (1) v300℃/秒 Ts<T1;T1500℃;T2200℃T1−T2
50℃;1分t5分;−0.5T2+500℃T1
−0.5T2+650℃ (2) v<300℃/秒 0T1−Ts<50℃;T1450℃;T2320
℃;0T1−T250℃;2分t5分; (3) 50℃/秒v<300℃/秒 T1−Ts50℃;T1450℃;T2300℃;0
T1−T270℃;1分t5分;[Claims] 1. After heating and annealing, after cooling to the cooling end point temperature T s (°C) at the primary average cooling rate v (°C/sec) after the soaking zone, the temperature is increased from the overaging start temperature T 1 (°C). Time t (minutes) to reach the aging end temperature T 2 (°C) In the thermal cycle of a cold rolled steel strip to be overaged, the following (1) to
(3) A continuous annealing method for steel strip, characterized by continuous annealing under one condition selected from conditions. (1) v300℃/sec T s <T 1 ; T 1 500℃; T 2 200℃T 1 −T 2
50℃; 1 minute t5 minutes; -0.5T 2 +500℃T 1
−0.5T 2 +650℃ (2) v<300℃/sec 0T 1 −T s <50℃; T 1 450℃; T 2 320
℃; 0T 1 -T 2 50℃; 2 minutes t5 minutes; (3) 50℃/sec v<300℃/sec T 1 -T s 50℃; T 1 450℃; T 2 300℃; 0
T 1 −T 2 70℃; 1 minute t5 minutes;
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11406982A JPS596329A (en) | 1982-07-02 | 1982-07-02 | Continuous annealing method for steel strip |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11406982A JPS596329A (en) | 1982-07-02 | 1982-07-02 | Continuous annealing method for steel strip |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS596329A JPS596329A (en) | 1984-01-13 |
| JPS6254375B2 true JPS6254375B2 (en) | 1987-11-14 |
Family
ID=14628252
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11406982A Granted JPS596329A (en) | 1982-07-02 | 1982-07-02 | Continuous annealing method for steel strip |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS596329A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62104083U (en) * | 1985-12-20 | 1987-07-02 |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA1259197A (en) * | 1985-02-13 | 1989-09-12 | Alan D. Bennett | High reliability fuel oil nozzle for a gas turbine |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5316465B2 (en) * | 1972-04-24 | 1978-06-01 | ||
| JPS5413403A (en) * | 1977-07-04 | 1979-01-31 | Kawasaki Steel Co | Batch furnace apparatus |
| JPS5534852A (en) * | 1978-09-04 | 1980-03-11 | Hitachi Ltd | Speed controller of motor |
-
1982
- 1982-07-02 JP JP11406982A patent/JPS596329A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62104083U (en) * | 1985-12-20 | 1987-07-02 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS596329A (en) | 1984-01-13 |
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