JPS60197889A - Method and device for adjusting liquid temperature - Google Patents

Method and device for adjusting liquid temperature

Info

Publication number
JPS60197889A
JPS60197889A JP5249384A JP5249384A JPS60197889A JP S60197889 A JPS60197889 A JP S60197889A JP 5249384 A JP5249384 A JP 5249384A JP 5249384 A JP5249384 A JP 5249384A JP S60197889 A JPS60197889 A JP S60197889A
Authority
JP
Japan
Prior art keywords
liquid
air
temperature
temp
heating
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
Application number
JP5249384A
Other languages
Japanese (ja)
Inventor
Sakae Nishiyama
榮 西山
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.)
Nishiyama Stainless Chemical Co Ltd
Original Assignee
Nishiyama Stainless Chemical 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 Nishiyama Stainless Chemical Co Ltd filed Critical Nishiyama Stainless Chemical Co Ltd
Priority to JP5249384A priority Critical patent/JPS60197889A/en
Publication of JPS60197889A publication Critical patent/JPS60197889A/en
Pending legal-status Critical Current

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  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)

Abstract

PURPOSE:To utilize the stirring effect of foam and to adjust exactly the liquid temp. by blowing the pressurized air as it is or after heating or cooling into the liquid in a vessel thereby heating or cooling the liquid. CONSTITUTION:The air compressed by a compressor 1 is passed through a flow rate regulating valve 2 to a selector valve 3. On the other hand a temp. sensor S detectes the temp. of the liquid W' in a vessel W and feeds the detection signal thereof to a control part 10. When the control part 10 makes judgement that it is necessary to increase the temp. of the liquid W', said part changes over the valve 3 to the heater 4 side to heat the pressurized air by the heater 4. The air is thereafter blown through a conduit 7 and the aperture 8a of a nozzle pipe 8 to the liquid W' in the vessel W. When the control part makes judgement that it is necessary to decrease the temp., the control part changes over the valve 3 to the cooler 5 side to cool the pressurized air by the cooler 5. The cooled air is then fed through conduits 5g, 7 to the nozzle pipe 8.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は主として酸洗浴、その他各種薬液の温度を調節
する方法及びその装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention mainly relates to a method and apparatus for adjusting the temperature of pickling baths and other various chemical solutions.

〔従来技術〕[Prior art]

例えば酸洗浴の温度調節は従来小型の鉄槽を用いる場合
には鉄をバーナ等にて直接加熱する方法が採られるが、
通窩は投込型の電熱ヒータ、或いは槽内に配したパイプ
に熱水を通流させ、或いは加熱蒸気を吹込む等の、所謂
内部加熱方式、又はメッキ浴をポンプで外部の熱交換器
に導き加熱する、所謂外部加熱方式等が採用されている
For example, when using a small iron tank, the temperature of a pickling bath is conventionally controlled by heating the iron directly with a burner, etc.
The through hole can be heated using an immersion type electric heater, a so-called internal heating method such as passing hot water through a pipe placed in the tank, or blowing heated steam, or using an external heat exchanger to pump the plating bath. The so-called external heating method, etc., which heats the material by guiding it to the outside, is used.

しかし前述した直接加熱方式は適用対象が狭く、また内
部加熱方式は浴液が、゛例えば強酸性2強アルカリ性で
ある場合、使用器具に耐薬品性が要求され、また槽内が
狭くなる問題があり、また水蒸気を用いる場合には薬液
が変化するという問題があり、さらに外部加熱方式は設
備が大型となり、しかも槽内には攪拌装置等をし必要と
する問題があった・ 〔目的〕 本発明は斯かる事情に鑑みなされたものであって、その
目的とするところは加熱又は冷却した空気を液中に吹き
込むことによって、気泡の撹拌効果を利用しして効率的
に液体の温度を正確、且つ迅速に加熱し得るようにした
液体温度調節方法及びその装置を提供するにある。
However, the above-mentioned direct heating method is applicable to a narrow range of applications, and the internal heating method requires chemical resistance for the equipment used when the bath liquid is, for example, strongly acidic or strongly alkaline, and there is also the problem that the inside of the bath becomes narrow. In addition, when using steam, there is a problem that the chemical solution changes, and in addition, the external heating method requires large equipment and requires a stirring device etc. inside the tank. [Purpose] This book The invention was made in view of the above circumstances, and its purpose is to efficiently and accurately control the temperature of a liquid by blowing heated or cooled air into the liquid, using the stirring effect of air bubbles. An object of the present invention is to provide a method and apparatus for controlling the temperature of a liquid that can be heated quickly.

〔構成〕〔composition〕

本発明に係る液体温度調節方法は加圧した空気をそのま
ま、又は加熱若しくは冷却した後槽内の液体中に吹き込
み、液を加熱若しくは冷却することを特徴とする。
The liquid temperature control method according to the present invention is characterized in that pressurized air is blown into the liquid in the tank either directly or after being heated or cooled to heat or cool the liquid.

また本発明に係る液体温度調節装置は空気を加圧する手
段と、加圧された空気を加熱及び/又は冷却する手段と
、加熱又は冷却された空気を槽内の液体中に噴射するノ
ズル部とを具イinすることを特徴とする。
Further, the liquid temperature control device according to the present invention includes means for pressurizing air, means for heating and/or cooling the pressurized air, and a nozzle section for injecting the heated or cooled air into the liquid in the tank. It is characterized by including the following.

〔実施例〕〔Example〕

以下本発明を酸洗液の温度調節に用いた場合につき具体
的に説明する。図面は本発明を酸洗液の温度調節に用い
た構成を示す模式図であり、図中Wは酸洗浴槽、W′は
洗浄液、1はコンプレッサを示している。コンプレッサ
lで圧縮された空気は流量調整弁2を経、分岐点に設け
た切換弁3により、加熱N4、又は冷却器5のいずれか
に選択的に導入される。加熱器4はハウジング4aの内
部下方にバーナ4bを備え、上方には空気通流用のパイ
プ4cが螺旋状に配設され”ζおり、このパイプ4b内
に導入された空気はパイプ4C内を通流する過程でバー
ナ4bの燃焼ガスとの熱交換により加熱される。加熱温
度はオイルタンク4dからバーナ4bへの燃料供給管4
eに介装した流量調節弁4fの調節により行なわれるよ
うになっている。この加熱器4自体の構成については特
に限定するものではな(、従来知られたものを適宜採用
してよい。
Hereinafter, the present invention will be explained in detail regarding the case where the present invention is used for controlling the temperature of a pickling solution. The drawing is a schematic diagram showing a configuration in which the present invention is used to adjust the temperature of a pickling solution. In the drawing, W indicates a pickling bath, W' indicates a cleaning solution, and 1 indicates a compressor. The air compressed by the compressor 1 passes through a flow rate regulating valve 2 and is selectively introduced into either the heating N4 or the cooler 5 by a switching valve 3 provided at a branch point. The heater 4 is equipped with a burner 4b inside the housing 4a, and a pipe 4c for air circulation is spirally arranged above the housing 4a, and the air introduced into the pipe 4b passes through the pipe 4C. During the flowing process, it is heated by heat exchange with the combustion gas of the burner 4b.The heating temperature is determined by the fuel supply pipe 4 from the oil tank 4d to the burner 4b.
This is done by adjusting the flow rate control valve 4f installed at e. The configuration of the heater 4 itself is not particularly limited (any conventionally known configuration may be used as appropriate).

一方冷却器5はハウジング5a内に図示しない冷媒通流
用のパイプを配設して構成されており、)\ウジング5
a内に導入された空気はパイプ内を通流する過程で冷却
される。冷却温度はハウジング5aに付設した温度制御
部5bの調節によって設定される。
On the other hand, the cooler 5 is configured by arranging a pipe for refrigerant flow (not shown) in the housing 5a.
The air introduced into a is cooled while flowing through the pipe. The cooling temperature is set by adjusting a temperature control section 5b attached to the housing 5a.

加熱器4で加熱された空気、冷却器5で冷却された空気
は配管4g、 5g、切換弁6にて選択的に給気管7に
導入される。給気管7は酸洗浴槽Wの一側壁に沿って配
設され、その先端にはノズル管8を備えている。ノズル
管8ばL形に屈曲せしめられ、酸洗浴槽Wの側壁下部か
ら低壁近くに延び、ここから低壁に沿って他側壁近傍に
延在され、その開口部8aから洗浄液の側方、又は−上
方に向けて空気を吹き出ずようにしである。
Air heated by the heater 4 and air cooled by the cooler 5 are selectively introduced into the air supply pipe 7 through the pipes 4g, 5g and the switching valve 6. The air supply pipe 7 is arranged along one side wall of the pickling bath W, and has a nozzle pipe 8 at its tip. The nozzle pipe 8 is bent into an L shape and extends from the lower part of the side wall of the pickling bath W to near the lower wall, and from there extends along the lower wall to near the other side wall, and from the opening 8a, the cleaning liquid is directed to the side, Or - without blowing air upwards.

ノズル管8の配設舷梯については特に限定するものでは
なく、途中で分岐して酸洗浴槽Wの底部に沿って平行、
或いは格子状に配設して酸洗浴槽Wの全体から均一に吹
き出されるようにしてもよい。
There are no particular limitations on the gangway on which the nozzle pipe 8 is arranged;
Alternatively, it may be arranged in a grid pattern so that the pickling bath W is blown out uniformly from the entire pickling bath W.

酸洗浴槽W内に加熱空気を吹き込んだ場合は空気洗浄液
中で細かい気泡となるため、洗浄液W′との熱交換が効
率よく行われ、また気泡による攪拌効果のため洗浄液W
′が局部的に加熱されることも防止され、所定温度への
加熱を迅速に行うことが出来、しかも水蒸気を吹き込む
場合に比較して薬液の希釈化等のおそれもない。洗浄液
中に冷却された空気を吹き込んだ場合も結果的には同し
である。
When heated air is blown into the pickling bath W, it forms fine bubbles in the air cleaning liquid, allowing efficient heat exchange with the cleaning liquid W'.
' is also prevented from being locally heated, heating to a predetermined temperature can be carried out quickly, and there is no risk of dilution of the chemical liquid compared to when steam is blown. The result is the same when cooled air is blown into the cleaning liquid.

洗浄液W′の温度はこの液中に挿入されている温度セン
サSによって検出され、その検出信号は指示計9に入力
される外、制御部10に人力される。
The temperature of the cleaning liquid W' is detected by a temperature sensor S inserted into this liquid, and the detection signal is inputted to the indicator 9 and also manually inputted to the control section 10.

制御部10には予め洗浄液温度としての設定値が入力さ
れており、温度センサSからの温度信号はこの設定値と
比較され、その差を解消すべく最適の制御パターンを決
定する。゛即ち、制御部10には洗浄液W′の量、比熱
、熱容量等のデータ、並びに洗浄液W′を成る温度にま
で加熱し、または冷却するうえでの空気圧、空気温度の
関係を示す式、或いは数値テーブルが入力されており、
上記に如く設定温度と測定温度との温度差がめられると
、加熱器4、冷却器5のいずれを駆動するかを判…iす
ると共に、温度差を解消するうえでの最も効率的な空気
量、空気温度を選定し、これを実現ずべくコンプレッサ
1並びに加熱器4における燃料流量調節弁4f、又は温
度制御部5bに所定の制御信号を出力するようになって
いる。
A set value for the temperature of the cleaning liquid is input into the control unit 10 in advance, and the temperature signal from the temperature sensor S is compared with this set value to determine an optimal control pattern to eliminate the difference.゛That is, the control unit 10 contains data such as the amount, specific heat, and heat capacity of the cleaning liquid W', as well as equations indicating the relationship between air pressure and air temperature when heating or cooling the cleaning liquid W' to a certain temperature, or A numerical table is entered,
When the temperature difference between the set temperature and the measured temperature is determined as described above, it is determined whether the heater 4 or the cooler 5 is to be driven, and the most efficient amount of air is determined to eliminate the temperature difference. , selects the air temperature, and outputs a predetermined control signal to the fuel flow control valve 4f in the compressor 1 and heater 4, or the temperature control section 5b in order to achieve this.

なお上記した制御部10は何ら自動制御式とする場合に
限るものではなく、作業者が指示計9を監視しつつ手動
的に制御JIする構成としても良いことは勿論である。
Note that the above-described control unit 10 is not limited to an automatic control type; it goes without saying that the control unit 10 may be configured to be manually controlled by an operator while monitoring the indicator 9.

以下本発明の実施例を数値を掲げて説明とする。Examples of the present invention will be described below with numerical values.

〔実施例1〕 幅2500++++、長さ5000mm、高さ2000
+uの浴槽に硝酸15%、弗化水素酸5%、水80%の
配合酸洗液201−ンを入れ、これを60℃に加熱ずべ
く 220’Cの熱風830r+?/時を吹き込んだと
ころ約30分で達成し得た。加熱過程では配合酸洗液の
攪拌効果が良好で、途中で温度を拡散的に測定したが平
均的な温度上昇がiMられ、格別の攪拌作業は全く不必
要であった。
[Example 1] Width 2500++++, length 5000mm, height 2000mm
Add 201-ton of pickling solution containing 15% nitric acid, 5% hydrofluoric acid, and 80% water to a +u bathtub and heat it to 60°C with 830r+ hot air at 220'C. / I was able to accomplish this in about 30 minutes. During the heating process, the mixed pickling solution had a good stirring effect, and although the temperature was measured diffusively during the heating process, an average temperature rise was observed, and no special stirring work was necessary.

また当初から焼鈍されたステンレス鋼を液中に浸漬して
おいたところ表面の酸化スケールが気泡の作業で完全に
剥離され、美しく仕上がり、従来脱スケールのためには
対象物を回転ブラシ等を用いて物理的なブラッシングを
必要としたがこの作業も全く不必要であった。
In addition, when stainless steel that has been annealed from the beginning is immersed in liquid, the oxidized scale on the surface is completely removed by the bubble process, resulting in a beautiful finish. This required physical brushing, but this work was also completely unnecessary.

〔実施例2〕 チタン合金成品を酸洗(ケミカルミーリング)するため
硝酸30%、弗化水素酸5%、水道水65%の酸洗液を
前記実施例1におけるのと同様の浴槽に入れ、加熱した
後、これに対象物を浸漬したところ、酸洗液とチタン合
金との急激な反応にょって60℃以上に昇温され水素ぜ
い性割れ発生のおそれが生じたため、加熱器4のバーナ
4cを停止し、切換弁3を操作し、冷却器5を作動する
ことにより容易に60°C以下に維持することができた
[Example 2] In order to pickle (chemical milling) a titanium alloy product, a pickling solution containing 30% nitric acid, 5% hydrofluoric acid, and 65% tap water was placed in the same bath as in Example 1, After heating, when the object was immersed in this, the temperature rose to over 60°C due to a rapid reaction between the pickling liquid and the titanium alloy, creating a risk of hydrogen brittle cracking. By stopping the burner 4c, operating the switching valve 3, and operating the cooler 5, the temperature could be easily maintained at 60°C or lower.

従来にあっては、酸洗液の急激な昇温に追随出来ず、酸
洗作業を一時中断し酸洗液の下降をまって再開するなど
作業の中断が多かったが、上記の実施例においては作業
の中断は全く不必要であった。また冷却空気は気泡とな
って酸洗浴中に吹き込まれるため、その攪拌効果によっ
て温度降下も均一に行い得、部分的な温度差も極めて小
さかった。
In the past, it was not possible to keep up with the rapid temperature rise of the pickling solution, and there were many interruptions in the pickling process, such as temporarily stopping the pickling process and restarting it after waiting for the pickling solution to descend.However, in the above example, The interruption of work was completely unnecessary. Furthermore, since the cooling air was blown into the pickling bath in the form of bubbles, the temperature could be lowered uniformly due to its stirring effect, and local temperature differences were also extremely small.

〔実施例3〕 耐酸性樹脂ポリプロピレンで製作された浴槽に塩素系又
はその他の溶剤からなる脱脂処理液を入れ、これに機械
部品等の対象物を浸漬し、120℃に加熱した圧縮空気
(3気圧)を吹き込んだところ、十分な脱脂処理を行い
得た。従来はこの種脱脂処理に際してはステンレス製の
超音波洗浄機を浴槽内に入れて超音波洗浄を行ってはい
るが、このような超音波洗浄には超音波が樹脂に吸収さ
れるために樹脂製浴槽を用いることが出来なかったが、
本実施例では何らの不都合も生しなかった。
[Example 3] A degreasing solution made of chlorine or other solvent was placed in a bathtub made of acid-resistant resin polypropylene, objects such as mechanical parts were immersed in this, and compressed air heated to 120°C (3 When air pressure) was blown into the tank, sufficient degreasing treatment was achieved. Conventionally, when performing this type of degreasing treatment, a stainless steel ultrasonic cleaner was placed in a bathtub to perform ultrasonic cleaning, but in this type of ultrasonic cleaning, the ultrasonic waves are absorbed by the resin, so the resin Although it was not possible to use a bathtub made of
This example did not cause any inconvenience.

〔実施例4〕 機械金属部品表面に付着している動植物油脂、鉱油類を
除去するため、これらを常温での使用が可能で、しかも
塩素系溶剤の如く人体への自重性(ハロゲンイオン)の
ないイソプロピルアルコールを用いて洗浄し、洗浄終了
の機械金属部品に加熱器4から供給される170℃、圧
力3気圧の熱風を適宜のノズルを用いて吹き(=lげた
ところ極めて効率よく乾燥せしめiM、火気が全くない
こともあって、燃焼、爆発等のおそれもなく、安全に作
業を行い得た。イソプロピルアルコールの引火点は21
.1℃であるが、これよりも引火点の低いメチルアルコ
ール: 15.6℃、エチルアルコール: 15.8℃
、nプロピルアルコール:15℃等のアルコール類、ベ
ンゼンニー11.1℃、トルエン:4.4℃、キシレン
: 34.4℃等の炭化水素等についても同様に動植物
油脂、鉱油類の除去に用い、対象機械金属部品を加熱器
4から供給される170℃の空気で乾燥させたが、燃焼
は全く生じなかった。
[Example 4] In order to remove animal and vegetable oils and mineral oils adhering to the surfaces of mechanical metal parts, these can be used at room temperature, and unlike chlorinated solvents, they do not have a negative impact on the human body (halogen ions). After cleaning, the machine metal parts are cleaned using isopropyl alcohol, and hot air of 170°C and 3 atmospheres is supplied from the heater 4 to the machine metal parts using an appropriate nozzle. Since there was no open flame, the work could be carried out safely without any fear of combustion or explosion.The flash point of isopropyl alcohol is 21.
.. 1℃, but lower flash point than this: Methyl alcohol: 15.6℃, Ethyl alcohol: 15.8℃
Alcohols such as , n-propyl alcohol: 15℃, benzene at 11.1℃, toluene: 4.4℃, xylene: 34.4℃, etc. are also used to remove animal and vegetable fats and mineral oils. , the target mechanical metal parts were dried with air at 170° C. supplied from the heater 4, but no combustion occurred.

〔実施例5〕 機械部品に有機溶剤(シンナー)を含む塗料を塗布し、
同様にして加熱器4から供給される170℃の熱風を吹
き付は乾燥したが、発火、燃焼させることなく効率的に
乾燥を行い得た。
[Example 5] Applying paint containing organic solvent (thinner) to mechanical parts,
Similarly, drying was carried out by blowing hot air at 170° C. supplied from the heater 4, but the drying could be carried out efficiently without ignition or combustion.

なお、上記実施例は常温の空気を加熱又は冷却して用い
る場合を説明したが、加熱又は冷却対象液体との関係で
は常温の空気をそのまま用いても対象液体の加熱又は冷
却を行い得ることは勿論である。
In addition, although the above embodiment describes the case where room temperature air is heated or cooled, in relation to the liquid to be heated or cooled, it is possible to heat or cool the target liquid even if room temperature air is used as it is. Of course.

〔効果〕〔effect〕

以上の如く本発明方法及び装置にあっては液体の温度調
節にそのまま、加熱、冷却した空気を用いることとして
いるから、対象液体の混合比率等を乱すことなく、また
燃焼、爆発等の危険性も泣く、しかも気泡による攪拌効
果によって液体温度を局部的にに変化させることなく均
一、且つ迅速に調節出来、しかも槽内に特別な装置を設
置しないから槽内を広く利用出来、更に洗浄液の温度調
節に用いた場合等には温度調節と同時に気泡によって対
象物にたいする洗浄効果も高め得るなど本発明は優れた
効果を奏する。
As described above, in the method and apparatus of the present invention, heated and cooled air is used to adjust the temperature of the liquid, so there is no need to disturb the mixing ratio of the target liquid, and there is no risk of combustion, explosion, etc. What's more, the agitation effect of air bubbles allows for uniform and quick adjustment of the liquid temperature without local changes.Furthermore, since no special equipment is installed inside the tank, the inside of the tank can be widely used, and the temperature of the cleaning liquid can be adjusted evenly. When used for temperature control, the present invention has excellent effects such as being able to improve the cleaning effect on objects by using air bubbles at the same time as temperature control.

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

図面は本発明を酸洗液の温度調節に適用した構成を示す
模式図である。 W・・・酸洗浴槽 Wl・・・洗浄液 S・・・温度セ
ンサト・・コンプレッサ 2・・・流量調整弁 3・・
・切換弁4・・・加熱器 5・・・冷却器 6・・・切
換弁 7・・・給気管 8・・・ノズル管 8a・・・
吹出口 9・・・指示計10・・・制御部 特許出願人 西山ステンレスケミカルカ株式会社代理人
 弁理士 河 野 登 夫
The drawing is a schematic diagram showing a configuration in which the present invention is applied to temperature control of a pickling solution. W... Pickling bath Wl... Cleaning liquid S... Temperature sensor... Compressor 2... Flow rate adjustment valve 3...
・Switching valve 4... Heater 5... Cooler 6... Switching valve 7... Air supply pipe 8... Nozzle pipe 8a...
Air outlet 9...Indicator 10...Control unit Patent applicant: Nishiyama Stainless Chemical Co., Ltd. Patent attorney: Noboru Kono

Claims (1)

【特許請求の範囲】 夏、加圧した空気をそのまま、又は加熱若しくは冷却し
た後、槽内め液体中に吹き込み、液体を加熱若しくは冷
却することを特徴とする液体温度調節方法。 2、 空気を加圧する手段と、加圧された空気を加熱及
び/又は冷却する手段と、加熱又は冷却された空気を槽
内の液体中に噴射するノズル部とを具備することを特徴
とする液体温度調節装置。
[Scope of Claims] A method for adjusting the temperature of a liquid in summer, which comprises blowing pressurized air directly or after heating or cooling into the liquid in a tank to heat or cool the liquid. 2. It is characterized by comprising means for pressurizing air, means for heating and/or cooling the pressurized air, and a nozzle section for injecting the heated or cooled air into the liquid in the tank. Liquid temperature control device.
JP5249384A 1984-03-19 1984-03-19 Method and device for adjusting liquid temperature Pending JPS60197889A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5249384A JPS60197889A (en) 1984-03-19 1984-03-19 Method and device for adjusting liquid temperature

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5249384A JPS60197889A (en) 1984-03-19 1984-03-19 Method and device for adjusting liquid temperature

Publications (1)

Publication Number Publication Date
JPS60197889A true JPS60197889A (en) 1985-10-07

Family

ID=12916233

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5249384A Pending JPS60197889A (en) 1984-03-19 1984-03-19 Method and device for adjusting liquid temperature

Country Status (1)

Country Link
JP (1) JPS60197889A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008285710A (en) * 2007-05-16 2008-11-27 Daido Steel Co Ltd Pickling method and pickling device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4952345A (en) * 1972-09-27 1974-05-21

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4952345A (en) * 1972-09-27 1974-05-21

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008285710A (en) * 2007-05-16 2008-11-27 Daido Steel Co Ltd Pickling method and pickling device

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