JPS5946314B2 - Metal strip continuous annealing pickling equipment - Google Patents

Metal strip continuous annealing pickling equipment

Info

Publication number
JPS5946314B2
JPS5946314B2 JP10690277A JP10690277A JPS5946314B2 JP S5946314 B2 JPS5946314 B2 JP S5946314B2 JP 10690277 A JP10690277 A JP 10690277A JP 10690277 A JP10690277 A JP 10690277A JP S5946314 B2 JPS5946314 B2 JP S5946314B2
Authority
JP
Japan
Prior art keywords
equipment
pickling
heat exchanger
metal strip
continuous annealing
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
Application number
JP10690277A
Other languages
Japanese (ja)
Other versions
JPS5440235A (en
Inventor
道利 奥村
浩 伊藤
賢治 川手
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Daido Steel Co Ltd
Original Assignee
Daido Steel Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP10690277A priority Critical patent/JPS5946314B2/en
Publication of JPS5440235A publication Critical patent/JPS5440235A/en
Publication of JPS5946314B2 publication Critical patent/JPS5946314B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 この発明は金属ストリップ連続焼鈍酸洗装置の改良に関
する。
DETAILED DESCRIPTION OF THE INVENTION This invention relates to improvements in continuous annealing and pickling equipment for metal strip.

一般に鋼や銅合金などの金属ストリップのAPラインに
用いられる金属ストリップ連続焼鈍酸洗装置は、第1図
に示すように、焼鈍炉1と、その前後装置として脱脂装
置2、脱脂後の乾燥用の乾燥装置3、水冷槽4、水冷後
の乾燥用の乾燥装置5、酸洗装置6、湯洗装置7、湯洗
後の乾燥用の乾燥装置8などをそなえている。
The continuous annealing and pickling equipment for metal strips, which is generally used in AP lines for metal strips such as steel and copper alloys, consists of an annealing furnace 1, a degreasing device 2 as equipment before and after the annealing furnace, and a drying device for drying after degreasing, as shown in Fig. 1. A drying device 3, a water cooling tank 4, a drying device 5 for drying after water cooling, a pickling device 6, a hot water washing device 7, a drying device 8 for drying after hot water washing, etc. are provided.

そして従来は乾燥装置3、5、8への温風の供給、酸洗
装置6の酸洗液の加熱、および湯洗装置7への温水の供
給のため、ボイラ9を設けてこのボイラで発生した蒸気
を各熱交換器10、11、12、13、14に流通させ
て、空気酸洗液、水などの加熱をおこなつていた。従つ
て従来のこの装置においては焼鈍炉の前後装置用加熱源
としてボイラを必要とし、しかもこのボイラや各熱交換
器における熱損失が大きく、加熱のための熱効率も低か
つた。一方、焼鈍炉の冷却帯1aの各ゾーンには水冷式
の熱交換器15を設け、第2図に示すようにこの熱交換
器により冷却した雰囲気ガスを循環ファン216により
循環させてストリップITに吹付けて、対流熱伝達によ
るストリップの間接冷却をおこなつている。このように
してストリップITから熱交換器15の冷却水に伝達さ
れた熱(以下冷却熱という。)は相当な熱量に及ぷもの
であるが、従来この冷却熱はなんら利用することなく棄
てられていた。この発明は上記の点にかんがみてなされ
たもので、焼鈍炉におけるストリップの冷却熱を焼鈍炉
の前後装置用の加熱源として用いることにより、3、設
備費および運転費が大巾に節約される金属ストリップ連
続焼鈍酸洗装置を提供しようとするものである。
Conventionally, a boiler 9 is provided to supply hot air to the drying devices 3, 5, and 8, heat the pickling liquid in the pickling device 6, and supply hot water to the hot water washing device 7. The steam was passed through each heat exchanger 10, 11, 12, 13, and 14 to heat the air pickling liquid, water, and the like. Therefore, in this conventional apparatus, a boiler is required as a heating source for the equipment before and after the annealing furnace, and heat loss in the boiler and each heat exchanger is large, and the thermal efficiency for heating is also low. On the other hand, a water-cooled heat exchanger 15 is provided in each zone of the cooling zone 1a of the annealing furnace, and as shown in FIG. 2, the atmospheric gas cooled by the heat exchanger is circulated by a circulation fan 216 to the strip IT. The strip is sprayed to provide indirect cooling of the strip through convective heat transfer. The heat transferred from the strip IT to the cooling water of the heat exchanger 15 in this way (hereinafter referred to as cooling heat) amounts to a considerable amount of heat, but conventionally, this cooling heat is discarded without any use. was. This invention was made in view of the above points, and by using the cooling heat of the strip in the annealing furnace as a heating source for the front and rear devices of the annealing furnace, 3. Equipment costs and operating costs can be significantly reduced. It is an object of the present invention to provide a continuous annealing and pickling apparatus for metal strips.

以下第3図および第4図によりこの発明の一実施例を説
明する。
An embodiment of the present invention will be described below with reference to FIGS. 3 and 4.

図中、焼鈍炉1など第1図と同一符号を付した部分は第
1図と同一部分を示す。
In the figure, parts such as the annealing furnace 1 denoted by the same reference numerals as in FIG. 1 indicate the same parts as in FIG. 1.

21は焼鈍炉の冷却帯1aの第1ゾーンに設けた空冷式
熱交換器で、第2図における熱交換器15と同様に配設
され、冷風をこの熱交換器内に流通させてストリツプ1
7を間接冷却するものである。
Reference numeral 21 denotes an air-cooled heat exchanger provided in the first zone of the cooling zone 1a of the annealing furnace, which is arranged in the same manner as the heat exchanger 15 in FIG.
7 is indirectly cooled.

22は送風機(図示しない)などの冷風供給源に接続さ
れた冷風流路、23は冷風流量調節弁、24は熱交換器
流通後の温風の流路で乾燥装置3,5,8に接続されて
いる。
22 is a cold air flow path connected to a cold air supply source such as a blower (not shown), 23 is a cold air flow rate control valve, and 24 is a hot air flow path after flowing through the heat exchanger, which is connected to the drying devices 3, 5, and 8. has been done.

25は温風温度検出器、26は温度発信器、27は温度
調節計である。
25 is a hot air temperature detector, 26 is a temperature transmitter, and 27 is a temperature controller.

また28は温風の流路24内の圧力を検出して圧力信号
を発する圧力発信器、29は圧力調節計、30は温風放
出弁である。一方31は焼鈍炉の冷却帯1aの第2ゾー
ンに設けた第2図における熱交換器15と同様な水冷式
熱交換器である。32は冷水供給源(図示しない)に接
続された冷水流路、33は冷水流量調節弁、34は熱交
換器流通後の温水の流路で、湯洗装置7、および酸洗装
置S用の熱交換器35に接続されている。
Further, 28 is a pressure transmitter that detects the pressure in the hot air flow path 24 and issues a pressure signal, 29 is a pressure regulator, and 30 is a hot air release valve. On the other hand, 31 is a water-cooled heat exchanger similar to the heat exchanger 15 in FIG. 2 provided in the second zone of the cooling zone 1a of the annealing furnace. 32 is a cold water flow path connected to a cold water supply source (not shown), 33 is a cold water flow rate control valve, and 34 is a flow path for hot water after flowing through the heat exchanger, which is used for the hot water washing device 7 and the pickling device S. It is connected to a heat exchanger 35.

36は温水温度検出器、37は温度発信器、38は温度
調節計である。
36 is a hot water temperature detector, 37 is a temperature transmitter, and 38 is a temperature controller.

また39は差圧検出弁、40はこの差圧検出弁の前後の
圧力差が一定になるよう作動するダイヤフラム式の定流
量調整弁、41はブリードオフ用の絞り弁である。すな
わち、空冷式熱交換器21によつて得られた温風は乾燥
装置3,5,8にその乾燥用温風として供給され、その
際ストリツプ処理量などが変化しても一定温度の温風が
供給されるように、温風の温度を検出し温度調節計27
により冷風流量調節弁27の開度を調節する。
Further, 39 is a differential pressure detection valve, 40 is a diaphragm type constant flow regulating valve that operates so that the pressure difference before and after the differential pressure detection valve is constant, and 41 is a bleed-off throttle valve. That is, the hot air obtained by the air-cooled heat exchanger 21 is supplied to the drying devices 3, 5, and 8 as drying hot air, and at this time, even if the strip processing amount changes, the hot air remains at a constant temperature. The temperature controller 27 detects the temperature of the hot air so that
The opening degree of the cold air flow rate control valve 27 is adjusted by.

また各乾燥装置には一定流量の温風を供給する必要があ
るので、供給ヘツダ圧を検出して圧力調節計29により
温風放出弁30の開度を調節して温風供給圧力を一定に
保持するのである。一方、水冷式熱交換器31によつて
得られた温水は、その一部は酸洗装置6の酸洗液加熱用
の熱交換器35に供給され、他は湯洗装置rに直接供給
されて洗浄用温水として用いられる。この際ストリツプ
処理量などが変化しても一定温度の温水が供給されるよ
うに、温水温度を検出して温度調節計38により冷水流
量調節弁33の開度を調節し、また一定流量の温水が供
ノ給されるように定流量調整弁40を作動させて必要量
以上の温水は絞り弁41よりブリードオフさせるのであ
る。
In addition, since it is necessary to supply a constant flow rate of hot air to each drying device, the supply header pressure is detected and the opening degree of the hot air release valve 30 is adjusted using the pressure regulator 29 to keep the hot air supply pressure constant. hold it. On the other hand, part of the hot water obtained by the water-cooled heat exchanger 31 is supplied to the heat exchanger 35 for heating the pickling liquid of the pickling device 6, and the other part is directly supplied to the hot water washing device r. It is used as hot water for washing. At this time, the hot water temperature is detected and the opening degree of the cold water flow rate control valve 33 is adjusted by the temperature controller 38, so that hot water at a constant temperature is supplied even if the strip processing amount changes, etc. The constant flow regulating valve 40 is operated so that hot water is supplied, and hot water in excess of the required amount is bled off by the throttle valve 41.

このように焼鈍炉1の冷却帯1aにおいてストリツプか
ら得た冷却熱を焼鈍炉1の前後装置用の加熱源として用
いるので、特別のボイラなどを用いる必要がなくなり、
設備費とともに燃料消費量が減つて運転費も大巾に節約
される。
In this way, since the cooling heat obtained from the strip in the cooling zone 1a of the annealing furnace 1 is used as a heating source for the front and rear devices of the annealing furnace 1, there is no need to use a special boiler, etc.
Fuel consumption is reduced as well as equipment costs, resulting in significant savings in operating costs.

なお本実施例においては温風および温水の温度、前後装
置への供給流量などを一定に維持する調節装置を設けた
ので、ストリツプ処理量などAPラインの負荷が変動す
る場合に好都合であるが、ストリツプ処理量が一定の場
合にはこれらの調節装置は省略することができる。
In this embodiment, a regulating device is provided to maintain constant the temperature of hot air and hot water, the flow rate of supply to the front and rear devices, etc., which is convenient when the load on the AP line, such as the amount of strip processed, fluctuates. If the strip throughput is constant, these regulating devices can be omitted.

次にこの発明の効果のうち運転費節約の具体例をあげる
Next, we will give a specific example of the effect of this invention, which is the reduction in operating costs.

銅および銅合金ストリツプを毎時8乃至11.5トン処
理する連続焼鈍酸洗装置において、乾燥用温風の必要総
量は65℃の温風300TrI/紬でありこれを20℃
の空気を加熱して得るには毎時250500Kca1の
熱量が必要である。
In a continuous annealing and pickling equipment that processes 8 to 11.5 tons of copper and copper alloy strips per hour, the total amount of hot air required for drying is 300 TrI/pongee of hot air at 65°C, which is
It takes 250,500 Kcal of heat per hour to heat the air.

一方温水の所要量は65℃の温水601/〒であり、こ
れを20℃の水を加熱して得るには毎時162000K
ca1の熱量が必要である。ところがストリツプからの
冷却熱は、最小処理量毎時8トンの場合の冷却曲線が第
4図に示す通りなので、この冷却曲線から第1ゾーンに
おいて毎時294000Kca1、第2ゾーンにおいて
毎時201000Kca1の冷却熱が得られることが判
り、配管その他の熱損失を考慮しても前記温風および温
水を得るための十分な熱量が得られることが判る。従つ
て本発明を適用すれば前記所要熱量の合計毎時4125
00Kca1の熱量をボイラで得るための燃料がすべて
不要となるので、ボイラおよび各前後装置用の熱交換器
などの総熱効率を0.72とすると毎時約48.5kg
のLPGが節約されることになり、APラインの稼動時
間は年間7200時間に及ぶので、年間350トンとい
う大巾な燃料節約が達成される。なお本発明は横形の焼
鈍炉を用いた金属ストリップ連続焼鈍酸洗装置にも適用
できることは明らかである。
On the other hand, the required amount of hot water is 601/〒 of hot water at 65℃, and to obtain this by heating water at 20℃, 162,000 K/hour is required.
The amount of heat of ca1 is required. However, since the cooling curve for the minimum throughput of 8 tons/hour is as shown in Figure 4, the cooling heat from the strip is 294,000 Kca1/hour in the first zone and 201,000 Kca1/hour in the second zone. It can be seen that a sufficient amount of heat can be obtained to obtain the hot air and hot water even if heat loss from piping and other sources is considered. Therefore, if the present invention is applied, the total required amount of heat will be 4125 per hour.
Since all the fuel needed to obtain 00Kca1 of heat in the boiler is no longer required, assuming the total thermal efficiency of the boiler and heat exchangers for each front and rear device to be 0.72, it will generate approximately 48.5 kg per hour.
of LPG will be saved and the AP line will run for 7200 hours per year, resulting in a massive fuel savings of 350 tons per year. It is clear that the present invention can also be applied to a continuous annealing and pickling apparatus for metal strips using a horizontal annealing furnace.

また本発明において、焼鈍炉の冷却帯に設ける熱交換器
は、焼鈍炉や前後装置の規模や種類などに応じて、温水
だけあるいは温風だけを得て前後装置のうちの所定の装
置に供給するようにしてもよい。
In addition, in the present invention, the heat exchanger installed in the cooling zone of the annealing furnace obtains only hot water or only hot air and supplies it to a predetermined device among the annealing furnace and the front and rear devices, depending on the scale and type of the annealing furnace and the front and rear devices. You may also do so.

また熱交換器は上記実施例に示す対流熱伝達によるもの
のほか、水冷または空冷のチユープあるいはチヤンバに
よりストリツブからの放射熱を吸収する放射冷却による
形式のものなどとしてもよい。以上説明したように、こ
の発明によると焼鈍炉の前後装置用の加熱源としてのボ
イラが不要となるので、設備費および運転費が大巾に節
約され、メンテナンスの手間も減る。
Further, the heat exchanger may be of the type using convection heat transfer as shown in the above embodiments, or may be of the type using radiant cooling in which radiant heat from the strip is absorbed by a water-cooled or air-cooled tube or chamber. As explained above, according to the present invention, there is no need for a boiler as a heating source for the upstream and downstream devices of the annealing furnace, so equipment costs and operating costs are greatly reduced, and maintenance effort is also reduced.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は従来の金属ストリツプ連続焼鈍酸洗装置を示す
系統図、第2図は第1図の焼鈍炉の冷却帯の水平断面図
、第3図はこの発明に係る金属ストリツプ連続焼鈍酸洗
装置の一実施例を示す系統図、第4図は焼鈍炉の冷却帯
におけるストリツプの冷却曲線の一例である。 1・・・・・・焼鈍炉、1a・・・・・・冷却帯、2・
・・・・・脱脂装置、3・・・・・・乾燥装置、4・・
・・・・水冷槽、5・・・・・・乾燥装置、6・・・・
・・酸洗装置、7・・・・・・湯洗装置、8・・・・・
・乾燥装置、17・・・・・・ストリツプ、21・・・
・・・空冷式熱交換器、23・・・・・・冷風流量調節
弁、24・・・・・・温風の流路、27・・・―温度調
節計、29・・・・・・圧力調節計、30・・・・・・
温風放出弁、31・・・・・・水冷式熱交換器、33・
・・・・・冷水流量調節弁、34・・・・・・温水の流
路、38・・・・・・温度調節計、40・・・・・・定
流量調整弁。
Fig. 1 is a system diagram showing a conventional continuous annealing and pickling apparatus for metal strips, Fig. 2 is a horizontal sectional view of the cooling zone of the annealing furnace shown in Fig. 1, and Fig. 3 is a continuous annealing and pickling apparatus for metal strips according to the present invention. FIG. 4, a system diagram showing one embodiment of the apparatus, is an example of a cooling curve of a strip in a cooling zone of an annealing furnace. 1... Annealing furnace, 1a... Cooling zone, 2.
...Degreasing device, 3...Drying device, 4...
...Water cooling tank, 5...Drying device, 6...
... Pickling equipment, 7...Hot water washing equipment, 8...
・Drying device, 17... Strip, 21...
...Air-cooled heat exchanger, 23...Cold air flow rate control valve, 24...Hot air flow path, 27...Temperature controller, 29... Pressure regulator, 30...
Hot air release valve, 31...Water-cooled heat exchanger, 33.
...Cold water flow rate control valve, 34...Hot water flow path, 38...Temperature controller, 40...Constant flow rate control valve.

Claims (1)

【特許請求の範囲】 1 焼鈍炉と、その前後装置である脱脂装置、酸洗装置
、湯洗装置、乾燥装置などをそなえてなる金属ストリッ
プ連続焼鈍酸洗装置において、上記焼鈍炉の冷却帯に設
けられ水や空気などの流体を冷却媒体としてストリップ
を間接冷却する熱交換器と、上記流体を上記熱交換器に
流通させて得られる加熱流体を上記前後装置のうちの所
定の装置に供給する供給系路とをそなえたことを特徴と
する金属ストリップ連続焼鈍酸洗装置。 2 焼鈍炉と、その前後装置である脱脂装置、酸洗装置
、湯洗装置、乾燥装置などをそなえてなる金属ストリッ
プ連続焼鈍酸洗装置において、上記焼鈍炉の冷却帯に設
けられ水や空気などの流体を冷却帯に設けられ水や空気
などの流体を冷却媒体としてストリップを間接冷却する
熱交換器と、上記流体を上記熱交換器に流通させて得ら
れる加熱流体を上記前後装置のうちの所定の装置に供給
する供給系路と、上記加熱流体の温度を調節する温度調
節装置と、上記加熱流体の上記前後装置への供給流量を
調節する流量調節装置とをそなえたことを特徴とする金
属ストリップ連続焼鈍酸洗装置。
[Scope of Claims] 1. A metal strip continuous annealing and pickling apparatus comprising an annealing furnace and equipment before and after the same, such as a degreasing device, a pickling device, a hot water washing device, a drying device, etc., in which a cooling zone of the annealing furnace is provided. A heat exchanger is provided to indirectly cool the strip using a fluid such as water or air as a cooling medium, and a heated fluid obtained by circulating the fluid through the heat exchanger is supplied to a predetermined device among the front and rear devices. 1. A continuous annealing and pickling apparatus for metal strip, characterized by comprising a supply line. 2. In a metal strip continuous annealing and pickling equipment which is equipped with an annealing furnace and equipment before and after the degreasing equipment, a pickling equipment, a hot water washing equipment, a drying equipment, etc., a metal strip continuous annealing and pickling equipment is provided in the cooling zone of the annealing furnace and is equipped with water, air, etc. A heat exchanger is installed in the cooling zone and indirectly cools the strip using a fluid such as water or air as a cooling medium, and a heated fluid obtained by circulating the fluid through the heat exchanger is used in the front and rear devices. The heating fluid is characterized by comprising a supply line for supplying to a predetermined device, a temperature adjustment device for adjusting the temperature of the heating fluid, and a flow rate adjustment device for adjusting the flow rate of the heating fluid supplied to the front and rear devices. Metal strip continuous annealing and pickling equipment.
JP10690277A 1977-09-06 1977-09-06 Metal strip continuous annealing pickling equipment Expired JPS5946314B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10690277A JPS5946314B2 (en) 1977-09-06 1977-09-06 Metal strip continuous annealing pickling equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10690277A JPS5946314B2 (en) 1977-09-06 1977-09-06 Metal strip continuous annealing pickling equipment

Publications (2)

Publication Number Publication Date
JPS5440235A JPS5440235A (en) 1979-03-29
JPS5946314B2 true JPS5946314B2 (en) 1984-11-12

Family

ID=14445378

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10690277A Expired JPS5946314B2 (en) 1977-09-06 1977-09-06 Metal strip continuous annealing pickling equipment

Country Status (1)

Country Link
JP (1) JPS5946314B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT410804B (en) * 2000-06-30 2003-08-25 Koerner Chemieanlagen pickling

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0293065A (en) * 1988-09-29 1990-04-03 Tonen Corp Formation of thin film
JP5625419B2 (en) * 2010-03-19 2014-11-19 Jfeスチール株式会社 Washing water heating device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT410804B (en) * 2000-06-30 2003-08-25 Koerner Chemieanlagen pickling

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JPS5440235A (en) 1979-03-29

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