JPH0583617B2 - - Google Patents
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- Publication number
- JPH0583617B2 JPH0583617B2 JP63181756A JP18175688A JPH0583617B2 JP H0583617 B2 JPH0583617 B2 JP H0583617B2 JP 63181756 A JP63181756 A JP 63181756A JP 18175688 A JP18175688 A JP 18175688A JP H0583617 B2 JPH0583617 B2 JP H0583617B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- amount
- tank
- hot water
- cooling
- 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 - Lifetime
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 119
- 238000001816 cooling Methods 0.000 claims description 49
- 239000000498 cooling water Substances 0.000 claims description 23
- 238000007654 immersion Methods 0.000 claims description 22
- 238000002347 injection Methods 0.000 claims description 14
- 239000007924 injection Substances 0.000 claims description 14
- 238000000137 annealing Methods 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 11
- 239000002184 metal Substances 0.000 claims description 5
- 239000002351 wastewater Substances 0.000 claims description 4
- 238000004140 cleaning Methods 0.000 description 10
- 239000007788 liquid Substances 0.000 description 7
- 238000001704 evaporation Methods 0.000 description 5
- 230000008020 evaporation Effects 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 3
- 238000002791 soaking Methods 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000007689 inspection Methods 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 239000010960 cold rolled steel Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
Landscapes
- Control Of Heat Treatment Processes (AREA)
- Heat Treatment Of Strip Materials And Filament Materials (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は金属ストリツプの連続焼鈍炉における
浸漬冷却装置の注水制御方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for controlling water injection in an immersion cooling device in a continuous annealing furnace for metal strip.
金属ストリツプの連続焼鈍炉の一例を第３図に
示す。ストリツプ１はペイオフリール２を払い出
され、溶接機３にて先行のストリツプの尾端に溶
接された後、クリーニング装置４、入側ルーパ５
を通過して焼鈍炉に入る。焼鈍炉は金属ストリツ
プの熱処理を行うために加熱冷却を行うものであ
り、均熱または過時効処理が含まれる場合もあ
る。
An example of a continuous annealing furnace for metal strip is shown in FIG. The strip 1 is discharged from the payoff reel 2, and is welded to the tail end of the preceding strip by a welding machine 3.
It passes through and enters the annealing furnace. An annealing furnace performs heating and cooling to heat treat the metal strip, and may also include soaking or overaging treatment.
第３図では入側から加熱帯６、均熱帯７、冷却
帯８，９、最終冷却帯１０と順次ならんでいる。
焼鈍炉を出たストリツプ１は出側ルーパ１１、ス
キンパス装置１２、検査装置１３を通過し、テン
シヨンリール１５に巻き取られる。 In FIG. 3, the heating zone 6, the soaking zone 7, the cooling zones 8 and 9, and the final cooling zone 10 are arranged in this order from the entrance side.
The strip 1 leaving the annealing furnace passes through an exit looper 11, a skin pass device 12, an inspection device 13, and is wound onto a tension reel 15.
本発明は金属ストリツプの浸漬冷却に関するも
のである。浸漬冷却はその冷却能力が大きいとこ
ろから、ストリツプの焼き入れまたは最終冷却に
多く用いられている。第３図の例では、最終冷却
帯１０が浸漬冷却である。 The present invention relates to immersion cooling of metal strips. Immersion cooling is often used for quenching or final cooling of strips because of its large cooling capacity. In the example of FIG. 3, the final cooling zone 10 is immersion cooling.
浸漬冷却ではストリツプを冷却する時の熱によ
り、温排水が発生する。近年この温排水は省エネ
ルギーの観点から、工場用水として利用されてき
ている。第３図ではその一例を示しているが、最
終冷却帯１０で発生した温水１８は温水タンク１
６に貯溜され、移送ポンプ１９によつて入側温水
タンク１７に移送される。この移送された温水
は、クリーニング装置４で用いられる温水２０と
して利用されている。 In immersion cooling, the heat generated when the strip is cooled generates hot water. In recent years, this heated wastewater has been used as factory water from the perspective of energy conservation. FIG. 3 shows an example of this, and the hot water 18 generated in the final cooling zone 10 is
6 and transferred to the inlet hot water tank 17 by a transfer pump 19. This transferred hot water is used as hot water 20 used in the cleaning device 4.
従来の浸漬冷却における注水制御は大別して次
のａ），ｂ）の２つの方法が採られている。 Water injection control in conventional immersion cooling can be broadly classified into the following two methods a) and b).
ａ 冷却槽内液温制御
この方法では冷却槽内の液温を一定に保つため
に、冷却水の注水量を制御する（特公昭57−
11931）。第４図にその一例を示す。a Liquid temperature control in the cooling tank In this method, the amount of cooling water injected is controlled in order to keep the liquid temperature in the cooling tank constant.
11931). An example is shown in FIG.
ストリツプ１は冷却水槽２２内に貯溜された冷
却水２３に浸漬することにより冷却される。この
時、冷却水２３の温度はストリツプ１を所定の温
度に冷却するために一定温度にコントロールする
必要がある。この際、冷却水温を制御するために
補給水２４が流調弁２６によつて注水制御され
る。補給水２４はストリツプ１の持ち出しおよび
蒸発によつても消費されるが、その殆どは温水１
８として、温水タンク１６に排水される。温水タ
ンク中の温水は移送ポンプ１９により各使用先へ
移送される。 The strip 1 is cooled by being immersed in cooling water 23 stored in a cooling water tank 22. At this time, the temperature of the cooling water 23 must be controlled to a constant temperature in order to cool the strip 1 to a predetermined temperature. At this time, the supply of makeup water 24 is controlled by the flow control valve 26 in order to control the cooling water temperature. Make-up water 24 is also consumed by strip 1 removal and evaporation, but most of it is consumed by hot water 1.
8, the water is drained into the hot water tank 16. The hot water in the hot water tank is transferred to each place of use by a transfer pump 19.
ｂ 一定量注水
第５図に一例を示すように、冷却槽内の液温に
無関係に一定量の水を補給水２４として注水す
る。b Constant amount of water injection As shown in an example in FIG. 5, a constant amount of water is injected as make-up water 24 regardless of the liquid temperature in the cooling tank.
上記ａ）方式と異なり、冷却水槽２２の液温コ
ントロールは補給水の注水制御によるものではな
く、他の方式による。第３図に示した例では、冷
却水２３を循環し、この循環系に熱交換器３０を
設け、循環水温あるいは循環水量で冷却水２３の
液温をコントロールするものである。 Unlike the method a) above, the liquid temperature of the cooling water tank 22 is not controlled by injection of makeup water, but by another method. In the example shown in FIG. 3, the cooling water 23 is circulated, a heat exchanger 30 is provided in this circulation system, and the temperature of the cooling water 23 is controlled by the circulating water temperature or the amount of circulating water.
このような液温コントロールを行つた場合、補
給水はストリツプが持ち出す量および蒸発によつ
て減少する量を補給すればよく、一定量を補給す
べく注水バルブの開度を一定としており、余分な
補給水が温水１８として温水タンク１６に排出さ
れている。 When controlling the liquid temperature in this way, it is only necessary to replenish the amount of make-up water taken out by the strip and the amount that decreases due to evaporation.The opening of the water injection valve is kept constant to replenish a constant amount, and excess water is Make-up water is discharged into the hot water tank 16 as hot water 18.
以上の従来の方式では、浸漬冷却装置からの温
水の発生量とクリーニング装置用温水等の工場用
水の使用量とのバランスがとれず、発生量が多い
場合には余分な温水はドレンとして排水し、また
使用量が多い場合には、純水などの水を補給し、
さらに温度を上げるために蒸気などの熱が必要で
あつた。
In the conventional method described above, it is difficult to maintain a balance between the amount of hot water generated from the immersion cooling equipment and the amount of factory water used such as hot water for cleaning equipment, and when the amount of hot water generated is large, excess hot water is drained as a drain. , If the amount used is large, replenish water such as pure water,
Heat such as steam was required to further raise the temperature.
このアンバランスは従来の浸漬冷却装置におけ
る温排水の発生量は冷却装置のみを考慮した冷却
水の注水制御を行つていたためであり、本発明は
冷却水の注水量を工場使用量に合わせることによ
り、前記の不具合を解消しようとするものであ
る。 This imbalance is due to the fact that the amount of heated waste water generated in conventional immersion cooling equipment is controlled by cooling water injection taking only the cooling device into consideration.The present invention is designed to adjust the amount of cooling water injection to match the amount used in the factory. This is an attempt to solve the above-mentioned problems.
温水の使用量と補給水の注水量のバランスが崩
れると、冷却槽から排出された温水の温水タンク
レベルが変化する。すなわち、温水の使用量が多
いとタンクレベルが低下し、また少ないとタンク
レベルが上昇する。
If the balance between the amount of hot water used and the amount of make-up water injected is disrupted, the level of hot water discharged from the cooling tank in the hot water tank changes. That is, if the amount of hot water used is large, the tank level will decrease, and if the amount of hot water used is small, the tank level will increase.
本発明は、ストリツプの連続焼鈍炉における浸
漬冷却槽へ浸漬冷却に用いる冷却水を補給し、そ
のオーバーフロー温排水を工場用水として利用す
るにあたり、前記浸漬冷却槽からのオーバーフロ
ー温排水を受ける温水タンクを設け、該タンクか
ら使用先に供給する温水の流量を測定し、前記流
量の測定値から補給水量を演算し、該演算値に基
いて前記浸漬冷却槽への補給水の注水量を制御す
る一方、前記浸漬冷却槽の水温が所定値となるよ
うに温度制御を行うことを特徴とする連続焼鈍炉
における浸漬冷却装置の注水制御方法である。な
お、温水タンクの水面レベルと使用先に供給する
温水の流量とをカスケードして補給水量を演算す
れば一層好適である。 The present invention provides a hot water tank that receives overflow hot water from the immersion cooling tank when replenishing cooling water used for immersion cooling to the immersion cooling tank in a continuous strip annealing furnace and using the overflow hot water as water for factory use. and measuring the flow rate of hot water supplied from the tank to the user, calculating the amount of make-up water from the measured value of the flow rate, and controlling the amount of make-up water injected into the immersion cooling tank based on the calculated value. , a water injection control method for an immersion cooling device in a continuous annealing furnace, characterized in that temperature control is performed so that the water temperature of the immersion cooling tank becomes a predetermined value. Note that it is more preferable to calculate the amount of replenishment water by cascading the water level of the hot water tank and the flow rate of hot water supplied to the destination.
第１図に本発明の実施例を示す。 FIG. 1 shows an embodiment of the present invention.
ストリツプ１は冷却槽２２に溜められた冷却水
２３に浸漬することにより冷却される。冷却水２
３はストリツプの熱を奪うことにより温度上昇す
るが、本例に示す如く、冷却水の循環系を設けて
槽内の冷却水温をコントロールすればよい。２５
は液温計、２８は循環ポンプ、２９はコントロー
ルバルブ、３０は熱交換器である。 The strip 1 is cooled by immersing it in cooling water 23 stored in a cooling tank 22. cooling water 2
3, the temperature rises by removing heat from the strip, but as shown in this example, a cooling water circulation system may be provided to control the temperature of the cooling water in the tank. 25
28 is a circulation pump, 29 is a control valve, and 30 is a heat exchanger.
この例に示した水温制御方法は一例であつて、
本発明を何ら限定するものではなく、例えば循環
水を温水タンク１６から取り出し熱交換器を通し
て冷却水槽２２に供給してもよい。 The water temperature control method shown in this example is just an example.
For example, the circulating water may be taken out from the hot water tank 16 and supplied to the cooling water tank 22 through a heat exchanger, without limiting the present invention in any way.
冷却槽への補給水２４はコントロールバルブ３
２を介して冷却槽２２へ注水されるが、ストリツ
プの持ち出しおよび蒸発によつて消費された残り
の冷却水は温水１８として温水タンク１６に排出
される。この時温水の排出は冷却槽からのオーバ
ーフローによつて行うのが好ましい。これは冷却
槽内の冷却液面レベルを一定に保つためであり、
ストリツプの浸漬長を一定にすることで、冷却能
力を確保することができる。 Supply water 24 to the cooling tank is provided by control valve 3
The remaining cooling water consumed by strip removal and evaporation is discharged into the hot water tank 16 as hot water 18. At this time, hot water is preferably discharged by overflow from the cooling tank. This is to keep the coolant level in the cooling tank constant.
By keeping the immersion length of the strip constant, cooling capacity can be ensured.
温水タンク１６に溜められた温水１８は移送ポ
ンプ１９によつて工場用水として、例えばクリー
ニング装置などに移送される。この時、移送ポン
プ１９による移送量と、補給水の注水量およびス
トリツプの持ち出し量、蒸発量の差が温水タンク
１６のレベル変化として現れる。そこで工場の温
水使用量を流量計３７で測定し、補給量演算装置
３８によつて、補給水の注水量の設定を行う。こ
のようにすれば使用量と供給量との差は小さくな
り、温水タンク１６のレベル変化はほとんどなく
なる。しかしながら、工場使用量をそのまま補給
水量の設定とすると、ストリツプが持ち出す水量
および蒸発によつて消費される水量が不足するた
め、補給水の設定水量には、これらの水量を考慮
して、多めの設定を行う。この時、一定量を加算
して補給水量を設定してもよいが、ストリツプの
サイズラインスピード、冷却槽入口板温により、
ストリツプの持ち出す水量および蒸発水量が異な
るため、一定量の加算ではこれらの水量を補正す
ることができない。 The hot water 18 stored in the hot water tank 16 is transferred by a transfer pump 19 to, for example, a cleaning device as factory water. At this time, the difference between the amount transferred by the transfer pump 19, the amount of makeup water injected, the amount taken out of the strip, and the amount of evaporation appears as a change in the level of the hot water tank 16. Therefore, the amount of hot water used in the factory is measured by the flow meter 37, and the amount of replenishment water to be injected is set by the replenishment amount calculating device 38. In this way, the difference between the amount used and the amount supplied becomes small, and there is almost no change in the level of the hot water tank 16. However, if the amount of make-up water is set based on the amount used in the factory, the amount of water taken out by the strip and the amount of water consumed by evaporation will be insufficient. Make settings. At this time, the make-up water amount may be set by adding a certain amount, but depending on the strip size, line speed, and cooling tank inlet plate temperature,
Since the amount of water carried out by the strip and the amount of evaporated water are different, it is not possible to correct these amounts of water by adding a fixed amount.
そこでレベル計３６を温水タンク１６に設置
し、温水タンク１６のレベルが一定となるように
補給量演算装置３８に信号を送り補給水２４の補
給量制御器３９を作動させる。このようにすれば
温水の消費量と同量を確実に補給水量として設定
することができる。 Therefore, a level meter 36 is installed in the hot water tank 16, and a signal is sent to the replenishment amount calculation device 38 to operate the replenishment amount controller 39 of the makeup water 24 so that the level of the hot water tank 16 becomes constant. In this way, it is possible to reliably set the amount of make-up water equal to the consumption amount of hot water.
本発明による注水制御を実施した結果を以下に
示す。冷延鋼板の連続焼鈍炉の最終冷却帯におけ
る注水制御に本発明方法を適応した。本方法によ
る効果を確認するために、従来方法との比較テス
トを実施した。
The results of water injection control according to the present invention are shown below. The method of the present invention was applied to water injection control in the final cooling zone of a continuous annealing furnace for cold-rolled steel sheets. In order to confirm the effectiveness of this method, we conducted a comparative test with conventional methods.
テスト条件としてはストリツプ0.8mmｔ×1150
mmＷを400mpmで通板した。最終冷却帯は第１図
と同型式のものを設置した。 The test conditions are strip 0.8mmt x 1150
mmW was threaded at 400mpm. The final cooling zone was of the same type as shown in Figure 1.
ストリツプは250℃で浸漬冷却を開始し、80℃
まで冷却される。この時、冷却槽の水温は65℃で
あつた。また温水はクリーニング装置で利用さ
れ、その使用量は18m3／ｈであつた。 The strips start immersion cooling at 250°C and then 80°C.
cooled down to. At this time, the water temperature in the cooling tank was 65°C. Hot water was also used in the cleaning equipment, and the amount used was 18 m 3 /h.
この冷却装置を用いて第４図に示すような注水
による液温制御を実施したところ、補給水として
127m3／ｈもの多量の冷却水を必要とし、この殆
ど全量が温水タンクへ排出された。温水タンクか
らはクリーニング装置へ18m3／ｈ移送されている
が、残りの109m3／ｈの温水はドレンとして温水
タンクより排水された。また同様に第５図に示す
ような一定流量の補給水として５m3／ｈを冷却槽
へ注水した。本方式では移送ポンプは温水タンク
のレベルにより間欠運転を行つている。この場
合、クリーニング装置の温水消費量に対して移送
量が少ないため、クリーニング装置において温水
を造る必要が生じる。 When this cooling device was used to control the liquid temperature by injecting water as shown in Figure 4, it was found that the water was used as make-up water.
A large amount of cooling water of 127 m 3 /h was required, and almost the entire amount was discharged into the hot water tank. Although 18 m 3 /h of hot water was transferred from the hot water tank to the cleaning device, the remaining 109 m 3 /h of hot water was drained from the hot water tank as drain. Similarly, water was poured into the cooling tank at a constant flow rate of 5 m 3 /h as makeup water as shown in FIG. In this system, the transfer pump operates intermittently depending on the level of the hot water tank. In this case, since the amount of transferred water is small compared to the amount of hot water consumed by the cleaning device, it is necessary to produce hot water in the cleaning device.
この時クリーニング装置では13m3／ｈの純水お
よびこの純水を65℃まで昇温するために約1t／ｈ
の蒸気を消費した。 At this time, the cleaning equipment uses 13 m 3 /h of pure water and approximately 1 t/h to raise the temperature of this pure water to 65℃.
of steam was consumed.
これに対し第１図に示した本発明による注水制
御を実施した結果、クリーニング装置への温水移
送量は18m3／ｈと安定し、また注水量は温水レベ
ルに応じて約18m3／ｈと安定した注水制御ができ
た。 On the other hand, as a result of implementing the water injection control according to the present invention shown in Fig. 1, the amount of hot water transferred to the cleaning device was stable at 18 m 3 /h, and the amount of water injected was approximately 18 m 3 /h depending on the hot water level. Stable water injection control was achieved.
なお、第１図は冷却水槽が一槽タイプの実施例
であるが、連続焼鈍炉出側にスキンパスが設置さ
れている場合、冷却水槽出口板温は50℃以下が良
いとされている。一槽タイプではストリツプのサ
イズ変化、ラインスピード変化に対して出口板温
50℃を制御できない場合がある。 Although FIG. 1 shows an embodiment in which the cooling water tank is a single tank type, when a skin pass is installed on the exit side of the continuous annealing furnace, it is said that the plate temperature at the exit of the cooling water tank is preferably 50° C. or less. In the single-tank type, the outlet plate temperature varies depending on changes in strip size and line speed.
It may not be possible to control 50℃.
そこで冷却水槽を複数槽設けて段階的に板温を
下げる方式が考えられる。第２図は２槽タイプの
冷却装置に本発明を適用した例である。 Therefore, a method can be considered in which multiple cooling water tanks are provided to lower the board temperature in stages. FIG. 2 shows an example in which the present invention is applied to a two-tank type cooling device.
以上述べた如く、本発明による注水制御を行う
ことにより、ストリツプの冷却時に発生する温水
を効率よく利用することができる。
As described above, by performing the water injection control according to the present invention, it is possible to efficiently utilize the hot water generated when cooling the strip.
第１図、第２図は本発明の実施例のフローシー
ト、第３図は連続焼鈍装置の全体模式図、第４
図、第５図は従来例のフローシートである。
１……ストリツプ、２……ペイオフリール、３
……溶接機、４……クリーニング装置、５……入
口ルーパ、６……加熱帯、７……均熱帯、８，９
……冷却帯、１０……最終冷却帯、１１……出側
ルーパ、１２……スキンパス装置、１３……検査
装置、１５……テンシヨンリール、１６……温水
タンク、１７……入側温水タンク、１８……温
水、１９……移送ポンプ、２０……温水、２２…
…冷却槽、２３……冷却水、２４……補給水、２
５……液温計、２８……循環ポンプ、２９，３２
……コントロールバルブ、３０……熱交換器、３
６……レベル計、３７……流量計、３８……補給
量演算装置、３９……補給量制御器。
FIGS. 1 and 2 are flow sheets of embodiments of the present invention, FIG. 3 is an overall schematic diagram of a continuous annealing apparatus, and FIG.
FIG. 5 is a flow sheet of a conventional example. 1...Strip, 2...Payoff reel, 3
... Welding machine, 4 ... Cleaning device, 5 ... Inlet looper, 6 ... Heating zone, 7 ... Soaking zone, 8,9
... Cooling zone, 10 ... Final cooling zone, 11 ... Outlet side looper, 12 ... Skin pass device, 13 ... Inspection device, 15 ... Tension reel, 16 ... Hot water tank, 17 ... Inlet side hot water Tank, 18...Hot water, 19...Transfer pump, 20...Hot water, 22...
...Cooling tank, 23...Cooling water, 24...Supplementary water, 2
5... Liquid thermometer, 28... Circulation pump, 29, 32
...Control valve, 30 ...Heat exchanger, 3
6...Level meter, 37...Flow meter, 38...Replenishment amount calculation device, 39...Replenishment amount controller.
Claims (1)
却槽へ浸漬冷却に用いる冷却水を補給し、そのオ
ーバーフロー温排水を工場用水として利用するに
あたり、 前記浸漬冷却槽からのオーバーフロー温排水を
受ける温水タンクを設け、該タンクから使用先に
供給する温水の流量を測定し、 前記流量の測定値から補給水量を演算し、該演
算値に基いて前記浸漬冷却槽への補給水の注水量
を制御する一方、 前記浸漬冷却槽の水温が所定値となるように温
度制御を行うことを特徴とする連続焼鈍炉におけ
る浸漬冷却装置の注水制御方法。[Scope of Claims] 1. When replenishing cooling water used for immersion cooling to an immersion cooling tank in a continuous annealing furnace for metal strips and using the overflow warm waste water as factory water, the overflow warm waste water from the immersion cooling tank is A hot water tank is provided to receive hot water, the flow rate of hot water supplied from the tank to the user is measured, the amount of make-up water is calculated from the measured value of the flow rate, and the amount of make-up water to be injected into the immersion cooling tank is calculated based on the calculated value. 1. A water injection control method for an immersion cooling device in a continuous annealing furnace, characterized in that the temperature is controlled so that the water temperature of the immersion cooling tank becomes a predetermined value.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18175688A JPH0234728A (en) | 1988-07-22 | 1988-07-22 | Method for controlling injection of water into dip cooler in continuous annealing furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18175688A JPH0234728A (en) | 1988-07-22 | 1988-07-22 | Method for controlling injection of water into dip cooler in continuous annealing furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0234728A JPH0234728A (en) | 1990-02-05 |
| JPH0583617B2 true JPH0583617B2 (en) | 1993-11-26 |
Family
ID=16106338
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18175688A Granted JPH0234728A (en) | 1988-07-22 | 1988-07-22 | Method for controlling injection of water into dip cooler in continuous annealing furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0234728A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5289813A (en) * | 1991-08-28 | 1994-03-01 | Aisin Seiki Kabushiki Kaisha | Two speed mechanical supercharger |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5711931A (en) * | 1980-06-25 | 1982-01-21 | Sumitomo Chem Co Ltd | Production of allyl alcohol |
| JPS5756532A (en) * | 1980-09-16 | 1982-04-05 | Unitika Ltd | Production of wavy flat low crimped yarn |
| JPS6347341A (en) * | 1986-08-18 | 1988-02-29 | Mitsubishi Heavy Ind Ltd | Method for recovering heat of metallic strip |
-
1988
- 1988-07-22 JP JP18175688A patent/JPH0234728A/en active Granted
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5711931A (en) * | 1980-06-25 | 1982-01-21 | Sumitomo Chem Co Ltd | Production of allyl alcohol |
| JPS5756532A (en) * | 1980-09-16 | 1982-04-05 | Unitika Ltd | Production of wavy flat low crimped yarn |
| JPS6347341A (en) * | 1986-08-18 | 1988-02-29 | Mitsubishi Heavy Ind Ltd | Method for recovering heat of metallic strip |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0234728A (en) | 1990-02-05 |
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