JPH0414196B2 - - Google Patents
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- Publication number
- JPH0414196B2 JPH0414196B2 JP59117862A JP11786284A JPH0414196B2 JP H0414196 B2 JPH0414196 B2 JP H0414196B2 JP 59117862 A JP59117862 A JP 59117862A JP 11786284 A JP11786284 A JP 11786284A JP H0414196 B2 JPH0414196 B2 JP H0414196B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- zone
- cleaning
- immersion
- hot air
- 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
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- Chemical Treatment Of Metals (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は金属表面の脱脂、酸洗、りん酸塩処理
などの目的に使用される浸漬式表面処理方法とり
わけ節水型の浸漬式表面処理方法に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to an immersion type surface treatment method used for degreasing, pickling, phosphate treatment, etc. of metal surfaces, particularly a water-saving type immersion type surface treatment method. Regarding.
金属製品の脱脂、酸洗、りん酸処理などを行う
前処理方法として、複数基の浸漬槽を並設し、被
処理物を薬液槽から順次次段以降の水洗槽に移送
浸漬させる方法が採用されている。
As a pre-treatment method for degreasing, pickling, phosphoric acid treatment, etc. of metal products, a method is adopted in which multiple immersion tanks are installed in parallel and the objects to be treated are sequentially transferred from the chemical bath to the next washing tank and immersed. has been done.
この浸漬式表面処理方法において、各水洗槽へ
の薬液の持ち込みが増加して洗滌効果が低下する
のを防止するため、各水洗槽の最終槽に新水を給
水し、順次前段の水洗槽にオーバーフロー式に前
送りし、薬液槽に続く最初の水洗槽から排水する
方法が採られていた。 In this immersion type surface treatment method, in order to prevent the cleaning effect from decreasing due to an increase in the amount of chemicals brought into each washing tank, fresh water is supplied to the final tank of each washing tank, and then water is added to the previous washing tank in sequence. A method was adopted in which the water was fed forward in an overflow manner and the water was drained from the first washing tank following the chemical tank.
しかしこの方法では、操業中、薬液を含む多量
のオーバーフロー水が常時発生するため、使用水
量が増加するだけでなく、排水により公害問題が
生じたり、排水処理に非常に負担がかかり、設備
費やランニングコストが高価になるという問題が
あつた。
However, with this method, a large amount of overflow water containing chemical solutions is constantly generated during operation, which not only increases the amount of water used, but also causes pollution problems due to the wastewater and places a heavy burden on wastewater treatment, which increases equipment costs. There was a problem that running costs were high.
本発明は前記のような従来の不具合を解消する
ために研究を重ねて創案されたもので、無排水あ
るいは少なくとも排水量を著しく低減しながら効
率よく浸漬式表面処理を行える方法を提供しよう
とするものである。 The present invention was devised through repeated research in order to solve the above-mentioned conventional problems, and aims to provide a method for efficiently performing immersion surface treatment without drainage or at least with a significant reduction in the amount of drainage. It is.
上記目的を達成するため本発明は従来のように
単純に洗浄ゾーンからオーバーフロー水を排水す
るのでなく、複数段の洗浄水を順次各ゾーンの前
段ゾーンへ送り、最終ゾーンで新水による付着水
置換を行うと共に、予め薬液ゾーン又は次段の洗
浄ゾーンに蒸発室を付設し、操業中、この蒸発室
に薬液または洗浄水をスプレーしつつ熱風を導入
し、この熱風で薬液または洗浄水を蒸発させ、熱
風と共に排出する方法としたものである。
In order to achieve the above object, the present invention does not simply drain overflow water from the cleaning zone as in the past, but instead sends multiple stages of cleaning water to the previous zone of each zone in order, and replaces the adhered water with fresh water in the final zone. At the same time, an evaporation chamber is attached in advance to the chemical solution zone or the next-stage cleaning zone, and during operation, hot air is introduced into this evaporation chamber while spraying the chemical solution or cleaning water, and the chemical solution or cleaning water is evaporated with this hot air. , the method is to discharge the hot air together with the hot air.
以下本発明を添付図面に基づいて説明する。 The present invention will be explained below based on the accompanying drawings.
第1図は本発明に係る浸漬式節水型表面処理方
法の概要を示すもので、少なくともひとつの薬液
ゾーン1とこれに続く複数の洗浄ゾーン(図示す
るものでは第1洗浄ゾーン〜第7洗浄ゾーン)2
A〜2Gを有している。3は前処理乾燥炉、4は
塗装部、5は塗装焼付炉で、薬液ゾーン1から塗
装焼付炉5にかけてはコンベアHが架設され、こ
のコンベアHにより金属製品などの被処理物Iが
移送され、薬液ゾーン1から洗浄ゾーン2A〜2
Gにおいて順次停止し、昇降されることで槽中に
浸漬されるようになつている。 FIG. 1 shows an overview of the immersion type water-saving surface treatment method according to the present invention, which includes at least one chemical solution zone 1 and a plurality of cleaning zones following this (in the illustrated example, the first cleaning zone to the seventh cleaning zone )2
It has A to 2G. 3 is a pre-treatment drying furnace, 4 is a painting section, and 5 is a paint baking furnace. A conveyor H is installed from the chemical zone 1 to the paint baking furnace 5, and the objects I to be treated such as metal products are transferred by this conveyor H. , chemical solution zone 1 to cleaning zones 2A to 2
They stop in sequence at G, and are immersed in the tank by being raised and lowered.
第2図ないし第4図は本発明の詳細を示すもの
で、薬液ゾーン1は、被処理物Iが浸漬されるタ
ンク6とタンク中の薬液(酸液、化成処理液、脱
脂液等)を加熱する手段7と、薬液をタンク6に
供給する手段とを備えている。 Figures 2 to 4 show details of the present invention, and the chemical liquid zone 1 includes a tank 6 in which the object to be treated I is immersed and a chemical liquid (acid liquid, chemical conversion liquid, degreasing liquid, etc.) in the tank. It includes means 7 for heating and means for supplying the chemical solution to the tank 6.
第1洗浄ゾーン2Aないし第7洗浄ゾーン2G
もそれぞれ洗浄液を収容し被処理物Iを浸漬する
浸漬タンク8a〜8gを有しており、図示するも
のでは、第1洗浄ゾーン2Aの浸漬タンク8aと
第7洗浄ゾーン2Gの浸漬タンク8gには加熱手
段9が設けられ、湯洗を行うようになつている。 1st cleaning zone 2A to 7th cleaning zone 2G
Each of these has immersion tanks 8a to 8g that contain a cleaning liquid and immerse the object to be treated I, and in the illustrated one, the immersion tank 8a of the first cleaning zone 2A and the immersion tank 8g of the seventh cleaning zone 2G are A heating means 9 is provided to perform hot water washing.
そして、前記各タンク8a〜8gには、それぞ
れ順次前段の浸漬タンク上方へと延出する導水配
管10a〜10gが設けられ、それら導水配管1
0a〜10gにはポンプP1〜P7が介在接続され
ると共に、それぞれタンク上方位置に相当する導
水配管先端にはスプレーノズル11a〜11gが
適宜フレキシブルホースを介して設けられてい
る。導水配管10a〜10gには制御バルブ12
a〜12gが設けられ、第2図の第2洗浄ゾーン
で代表的に示すようなリミツトスイツチ等の検出
器13と電気的に接続されており、制御バルブは
被処理物の昇降による検出器の作動信号により自
動的に開閉を行うようになつている。なお、必要
に応じ導水配管10a〜10gには前段の浸漬タ
ンクに臨むボールタツプ弁14を接続しておいて
もよい。 Each of the tanks 8a to 8g is provided with water guide pipes 10a to 10g that sequentially extend above the preceding immersion tank.
Pumps P 1 to P 7 are interposed and connected to 0a to 10g, and spray nozzles 11a to 11g are provided via appropriate flexible hoses at the tips of the water guide pipes corresponding to the upper positions of the tanks, respectively. A control valve 12 is installed in the water guide pipes 10a to 10g.
a to 12g are provided and are electrically connected to a detector 13 such as a limit switch as typically shown in the second cleaning zone in FIG. It is designed to open and close automatically based on signals. Note that, if necessary, a ball tap valve 14 facing the preceding immersion tank may be connected to the water guide pipes 10a to 10g.
最終洗浄ゾーンである第7洗浄ゾーン2Gに
は、これと別に貯槽8hが配され、これにたとえ
ば純水装置15を介して新水が貯えられるように
なつていると共に、ポンプP8を介して新水導管
10hが第7洗浄ゾーンの浸漬タンク8gまで延
出され、先端のスプレーノズル11hにより付着
水置換を行うようになつている。 In the seventh cleaning zone 2G, which is the final cleaning zone, a storage tank 8h is separately arranged, and fresh water is stored in this tank via, for example, a pure water device 15, and fresh water is also stored in this via a pump P8 . A new water conduit 10h is extended to the immersion tank 8g of the seventh cleaning zone, and a spray nozzle 11h at the tip replaces attached water.
さらに、本発明は各ゾーンの所望位置好ましく
は前記薬液ゾーン1又はこれに続く第1洗浄ゾー
ン2Aに所要容積の蒸発室16を設けると共に、
この蒸発室16内にスプレーノズル機構17を配
設し、該スプレーノズル機構17を洗浄ゾーンの
浸漬タンクと配管で接続し、さらに蒸発室16に
熱風吹込部19を設ける。 Furthermore, the present invention provides an evaporation chamber 16 of a required volume at a desired location in each zone, preferably in the chemical liquid zone 1 or the first cleaning zone 2A following it, and
A spray nozzle mechanism 17 is disposed within the evaporation chamber 16, and the spray nozzle mechanism 17 is connected to the immersion tank of the cleaning zone by piping, and a hot air blowing section 19 is further provided in the evaporation chamber 16.
蒸発室16は筒状あるいはボツクス状に構成さ
れる。設置位置は第1図のように薬液ゾーン又は
第1洗浄ゾーンの側部に併設してもよいし、第2
図のように前記ゾーンの直上域あるいは第3図の
ように上側域に設けてもよい。場合によつては別
個に独立した形態とし配置で結んでもよいが効率
などの面から上記実施例の方式が好ましい。 The evaporation chamber 16 has a cylindrical or box-like configuration. The installation location may be on the side of the chemical solution zone or the first cleaning zone as shown in Figure 1, or the second
It may be provided in the area immediately above the zone as shown in the figure or in the upper area as in FIG. Depending on the case, they may be connected in separate configurations, but from the viewpoint of efficiency and the like, the method of the above embodiment is preferable.
前記タンクからスプレーノズル機構17への配
管は任意であるが、一般には蒸発室を付設した当
該ゾーン(第2図の場合には第1洗浄ゾーン)2
Aの導水配管10aに分岐管18を設け、これを
スプレーノズル機構17と接続することが好まし
い。 Although the piping from the tank to the spray nozzle mechanism 17 is optional, it is generally connected to the zone (first cleaning zone in the case of FIG. 2) 2 equipped with an evaporation chamber.
It is preferable to provide a branch pipe 18 in the water guide pipe 10a of A and connect this to the spray nozzle mechanism 17.
前記熱風吹込部19は配管により供給源と接続
されるもので、具体的には乾燥炉、焼付炉、脱臭
装置あるいは薬液加温手段などの排気部と接続さ
れ、それらの廃熱を利用するのである。 The hot air blowing section 19 is connected to a supply source through piping, and specifically connected to an exhaust section of a drying oven, baking oven, deodorizing device, or chemical solution heating means, and utilizes the waste heat thereof. be.
前記蒸発室16には排気管20が設けられ、こ
の排気管20には気液分離器21とロードフアン
22が接続されており、気液分離器21は浸漬タ
ンクに液を戻すための戻し管23が設けられる。 The evaporation chamber 16 is provided with an exhaust pipe 20, a gas-liquid separator 21 and a load fan 22 are connected to the exhaust pipe 20, and the gas-liquid separator 21 is a return pipe for returning the liquid to the immersion tank. 23 are provided.
なお、必要に応じ、第2図で例示するように導
水配管10aの一部を前送りせずに自己の浸漬タ
ンク8aの上方に導いてスプレーノズル24と接
続し浸漬とスプレーとを選択的に行うようにして
もよい。 If necessary, as illustrated in FIG. 2, a part of the water conduit 10a may be guided above its own immersion tank 8a and connected to the spray nozzle 24, so that immersion and spraying can be selectively performed. You may also do so.
また、第4図のように蒸発室16に温水ボイ
ラ、スチームボイラなどの熱交換器25を配して
もよく、これを併用した場合には熱風吹込みと相
乗して雰囲気温度が上昇し、空気中への水分の飽
和量が増加するためより一層蒸発速度が早まる。 Further, as shown in FIG. 4, a heat exchanger 25 such as a hot water boiler or a steam boiler may be disposed in the evaporation chamber 16, and when this is used in combination with hot air blowing, the atmospheric temperature increases. As the amount of moisture saturated in the air increases, the rate of evaporation becomes even faster.
前記したところは本発明の一実施例であり、洗
浄ゾーン数に限定はない。また最終洗浄ゾーンの
次に別の薬液ゾーンとそれに続く複数段の洗浄ゾ
ーンがある場合も本発明に含まれる。蒸発室16
を薬液ゾーン1に設け、薬液を蒸発させるように
してもよいのは勿論である。 What has been described above is one embodiment of the present invention, and the number of cleaning zones is not limited. Further, the present invention also includes a case where there is another chemical liquid zone next to the final cleaning zone and a plurality of cleaning zones following the final cleaning zone. Evaporation chamber 16
Of course, it is also possible to provide a chemical liquid in the chemical liquid zone 1 to evaporate the chemical liquid.
その他図面において26はシヤワー用ブースで
ある。 In other drawings, 26 is a shower booth.
本発明による表面処理方法を上述した実施装置
に基づいて説明する。被処理物IはコンベアHに
より所定の間隔と速度で薬液ゾーン1およびこれ
に続く洗浄ゾーン2A〜2Gに搬送され、各ゾー
ンの浸漬タンク6,8a〜8gに順次浸漬され
る。 The surface treatment method according to the present invention will be explained based on the above-mentioned implementation apparatus. The object to be treated I is transported by a conveyor H at a predetermined interval and speed to the chemical solution zone 1 and the following cleaning zones 2A to 2G, and is sequentially immersed in the immersion tanks 6, 8a to 8g of each zone.
この工程において、本発明では予め貯槽8hに
新水を貯えておき、ポンプP8により新水導管1
0hを介して最終ゾーン2gの浸漬タンク上方の
スプレーノズル11hに新水を導く。また最終ゾ
ーン2gの浸漬タンク8gからポンプP7により
前段たる第6洗浄ゾーン2fの浸漬タンク上方の
スプレーノズル11gに洗浄水を導く。以下同様
に順次前段ゾーンのタンク上方のスプレーノズル
に洗浄水を前送りし、第1洗浄ゾーン2Aのポン
プP1から薬液ゾーン1Aの浸漬タンク6の上の
スプレーノズル7にも洗浄水を導く。 In this process, in the present invention, fresh water is stored in a storage tank 8h in advance, and the new water conduit 1 is pumped by pump P8.
0h to the spray nozzle 11h above the immersion tank in the final zone 2g. Further, cleaning water is guided from the immersion tank 8g in the final zone 2g to the spray nozzle 11g above the immersion tank in the sixth cleaning zone 2f, which is the first stage, by a pump P7 . Thereafter, the cleaning water is sequentially forwarded to the spray nozzles above the tank in the front zone in the same manner, and the cleaning water is also guided from the pump P1 of the first cleaning zone 2A to the spray nozzle 7 above the immersion tank 6 in the chemical zone 1A.
被処理物Iは、薬液ゾーン1の浸漬タンク6に
浸漬され、次いで引上げられるときにリミツトス
イツチ等の検出手段が作動し、その信号で制御パ
ルプ12aが開き、後段の第1洗浄ゾーン2Aか
ら導かれた洗浄液がスプレーノズル11aにより
被処理物にシヤワーされ、それから搬送が始ま
り、第1洗浄ゾーン2Aに到り、浸漬タンク8a
に浸漬されることで本洗浄が行われる。そして、
この浸漬タンクから引上げられたところで前述し
たように制御バルブ12bによりスプレーノズル
11bが作動し、次段の洗浄水により洗われる。
以下この過程が最終洗浄ゾーンまで繰返され、最
終洗浄ゾーン2Gでは貯槽8hからスプレーノズ
ル11gにより新水供給を兼ねたスプレー洗浄が
行われる。 The object to be treated I is immersed in the immersion tank 6 of the chemical zone 1, and then when it is pulled up, a detection means such as a limit switch is activated, and the control pulp 12a is opened in response to the signal, and the object is guided from the first washing zone 2A in the subsequent stage. The cleaning liquid is showered onto the workpiece by the spray nozzle 11a, and then conveyance begins, reaching the first cleaning zone 2A, and entering the immersion tank 8a.
The main cleaning is performed by immersing it in the water. and,
When the material is lifted out of the immersion tank, the control valve 12b operates the spray nozzle 11b as described above, and the material is washed with the next stage of washing water.
Thereafter, this process is repeated up to the final cleaning zone, and in the final cleaning zone 2G, the spray nozzle 11g performs spray cleaning that also serves as fresh water supply from the storage tank 8h.
そして、上記の操業を併行して蒸発室16には
第1洗浄ゾーン2Aの導水配管10aの分岐管1
8から洗浄水が送られ、スプレーノズル機構17
により噴霧されると共に、熱風吹込口19を通し
て蒸発室16に熱風が吹込まれる。 Concurrently with the above operation, the branch pipe 1 of the water guide pipe 10a of the first cleaning zone 2A is installed in the evaporation chamber 16.
Cleaning water is sent from 8 to the spray nozzle mechanism 17
At the same time, the hot air is blown into the evaporation chamber 16 through the hot air blowing port 19.
この熱風吹込みにより、蒸発室16の雰囲気温
度が高い温度に保持され、空気中への水分飽和量
が増加すると共に、洗浄水がミスト化されて室内
に供給されるので、それらの相乗作用できわめて
蒸発速度が早く、発生蒸気は熱風と共に排気管2
0から取出され、気液分離器21を通つたのち大
気に放出される。熱風は表面処理設備からの廃熱
を利用できるので経済的である。 By blowing hot air, the atmospheric temperature in the evaporation chamber 16 is maintained at a high temperature, the amount of water saturation in the air increases, and the cleaning water is turned into a mist and supplied into the room. The evaporation rate is extremely fast, and the generated steam is sent to the exhaust pipe 2 along with hot air.
0, passes through a gas-liquid separator 21, and then is released into the atmosphere. Hot air is economical because waste heat from surface treatment equipment can be used.
本発明は、上記のように付設した蒸発室16で
洗浄水を熱風により蒸発させることから排水量を
ゼロあるいは少なくとも排水量を著しく低減する
ことが可能となる。すなわち、蒸発室16が実施
例のように第1洗浄ゾーン2Aに設けられている
場合、前段の薬液ゾーン1から被処理物に付着し
て持込まれる水量と最終段の洗浄ゾーン2Gから
順次前送りされ、第1洗浄ゾーン2Aにスプレー
された洗浄水量との差(余剰量)に相当する水量
を分岐管18から蒸発室16に送り込むことによ
り排水量を皆無とすることができる。蒸発量のコ
ントロールはスプレーノズル機構17からのスプ
レー量や熱風吹込み量や熱風温度などで自在にコ
ントロールを行うことができる。 In the present invention, since the washing water is evaporated by hot air in the evaporation chamber 16 provided as described above, it is possible to eliminate the amount of drainage or at least significantly reduce the amount of drainage. That is, when the evaporation chamber 16 is provided in the first cleaning zone 2A as in the embodiment, the amount of water that adheres to the object to be treated and is brought in from the preceding chemical zone 1 and the amount of water that is sequentially forwarded from the final cleaning zone 2G. By sending an amount of water corresponding to the difference (surplus amount) from the amount of washing water sprayed into the first washing zone 2A from the branch pipe 18 to the evaporation chamber 16, the amount of water discharged can be completely eliminated. The amount of evaporation can be freely controlled by the amount of spray from the spray nozzle mechanism 17, the amount of hot air blown in, the temperature of the hot air, and the like.
実施例
本発明を用いて酸洗−第1水洗〜第7水洗の前
処理を行つた。被処理物はラジエータ幅530mm、
高さ350mm、厚さ16mm、放熱面積6m2で、これを
1時間あたり90台処理した。Example Using the present invention, pretreatments of pickling and first to seventh water washing were performed. The object to be treated is a radiator with a width of 530 mm.
It has a height of 350mm, a thickness of 16mm, and a heat dissipation area of 6m2 , and can process 90 units per hour.
給水量は320/hで、第7洗浄ゾーンから順
次薬液ゾーンまで4/hずつ前送りし、被処理
物が浸漬後引上げられたときにスプレーした。操
業中、蒸発室に直燃式脱臭付焼付乾燥炉から
70000Kcal/h、薬液加温用ボイラーから
40000Kcal/h、水切乾燥炉から23400Kcal/h
の熱風を110Nm3/min吹込みつつ、分岐管を通
してスプレーノズル機構により第1洗浄ゾーンの
洗浄液を230/hでスプレーした。 The water supply rate was 320/h, and the water was fed forward from the seventh cleaning zone to the chemical zone in 4/h increments, and sprayed when the object to be treated was pulled up after being immersed. During operation, a direct combustion type deodorizing baking drying oven is used in the evaporation chamber.
70000Kcal/h, from boiler for heating chemical solution
40000Kcal/h, 23400Kcal/h from drain drying oven
While blowing hot air at 110 Nm 3 /min, the cleaning solution in the first cleaning zone was sprayed at 230 Nm 3 /h through the branch pipe using a spray nozzle mechanism.
上記条件での操業により排水量はゼロとなつ
た。一方熱風供給を行わないで操業した場合に
は、自然蒸発量が約50/hで、180/hの排
水が生じた。 By operating under the above conditions, the amount of wastewater was reduced to zero. On the other hand, when the plant was operated without hot air supply, the natural evaporation rate was approximately 50/h, and 180/h of waste water was generated.
以上説明した本発明によるときには、複数段の
浸漬式洗浄を行う前処理において、比較的簡単に
無排水あるいは少なくとも排水量を低減すること
ができ、しかも廃熱を有効に利用するため経済的
に実施できるなどのすぐれた効果が得られる。
According to the present invention as described above, it is possible to relatively easily eliminate wastewater or at least reduce the amount of wastewater in the pretreatment that performs multi-stage immersion cleaning, and moreover, it can be carried out economically because waste heat is effectively used. Excellent effects such as
第1図は本発明に係る浸漬式節水型表面処理方
法の概要を示す平面図、第2図は本発明の実施装
置を示す回路図、第3図は本発明における蒸発室
の一例を示す断面図、第4図は別の実施例を示す
断面図である。
1……薬液ゾーン、2A〜2G……洗浄ゾー
ン、8a〜8g……浸漬タンク、10a〜10g
……導水配管、11a〜11g……スプレーノズ
ル、16……蒸発室、17……スプレーノズル機
構、19……熱風吹込部。
FIG. 1 is a plan view showing an overview of the immersion type water-saving surface treatment method according to the present invention, FIG. 2 is a circuit diagram showing an implementation apparatus of the present invention, and FIG. 3 is a cross-sectional view showing an example of the evaporation chamber in the present invention. 4 are sectional views showing another embodiment. 1...Chemical solution zone, 2A-2G...Cleaning zone, 8a-8g...Immersion tank, 10a-10g
. . . Water conveyance piping, 11a to 11g . . . Spray nozzle, 16 . . . Evaporation chamber, 17 . . . Spray nozzle mechanism, 19 .
Claims (1)
次いで洗浄水槽に浸漬して洗浄を行う表面処理方
法において、洗浄水を順次各ゾーンの前段ゾーン
へ送り、最終ゾーンで新水による付着水置換を行
うと共に、所望のゾーンに蒸発室を付設して該蒸
発室に操作中薬液または洗浄水をスプレーしつつ
熱風を導入し、薬液または洗浄水を蒸発して熱風
と共に排出することを特徴とする浸漬式節水型表
面処理方法。 2 複数段の洗浄水を前段ゾーンへ送る方法がス
プレーであり、被処理物が次段の洗浄水槽に浸漬
される前に洗浄水でスプレー洗浄される特許請求
の範囲第1項記載の浸漬式節水型表面処理方法。 3 蒸発室へ導入する熱風として、焼付炉、乾燥
炉、脱臭装置、薬液加温手段などからの廃熱を利
用するものを含む特許請求の範囲第1項記載の浸
漬式節水型表面処理方法。[Claims] 1. Treating a metal surface with an aqueous solution containing a chemical agent,
Next, in a surface treatment method in which cleaning is performed by immersion in a cleaning water tank, cleaning water is sequentially sent to the previous zone of each zone, and the adhered water is replaced with fresh water in the final zone, and an evaporation chamber is attached to the desired zone. An immersion water-saving surface treatment method characterized in that hot air is introduced into the evaporation chamber while spraying a chemical solution or cleaning water during operation, and the chemical solution or cleaning water is evaporated and discharged together with the hot air. 2. The immersion method according to claim 1, in which the method of sending multiple stages of washing water to the front zone is spraying, and the object to be treated is spray-washed with the washing water before being immersed in the next-stage washing water tank. Water-saving surface treatment method. 3. The immersion type water-saving surface treatment method according to claim 1, which includes a method that uses waste heat from a baking furnace, a drying furnace, a deodorizing device, a chemical solution heating means, etc. as the hot air introduced into the evaporation chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11786284A JPS60262983A (en) | 1984-06-08 | 1984-06-08 | Water saving type surface treatment by immersing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11786284A JPS60262983A (en) | 1984-06-08 | 1984-06-08 | Water saving type surface treatment by immersing |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60262983A JPS60262983A (en) | 1985-12-26 |
| JPH0414196B2 true JPH0414196B2 (en) | 1992-03-12 |
Family
ID=14722130
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11786284A Granted JPS60262983A (en) | 1984-06-08 | 1984-06-08 | Water saving type surface treatment by immersing |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60262983A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62247091A (en) * | 1986-04-17 | 1987-10-28 | Kemikooto:Kk | Apparatus and method for surface treatment of metal |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5229968A (en) * | 1975-09-03 | 1977-03-07 | Hitachi Ltd | Method of producing multiilayer printed circuit board |
| US4254362A (en) * | 1979-07-30 | 1981-03-03 | Midland-Ross Corporation | Power factor compensating electroluminescent lamp DC/AC inverter |
-
1984
- 1984-06-08 JP JP11786284A patent/JPS60262983A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60262983A (en) | 1985-12-26 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |