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JPH0585819B2 - - Google Patents
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JPH0585819B2 - - Google Patents

Info

Publication number
JPH0585819B2
JPH0585819B2 JP59119101A JP11910184A JPH0585819B2 JP H0585819 B2 JPH0585819 B2 JP H0585819B2 JP 59119101 A JP59119101 A JP 59119101A JP 11910184 A JP11910184 A JP 11910184A JP H0585819 B2 JPH0585819 B2 JP H0585819B2
Authority
JP
Japan
Prior art keywords
liquid
liquid tank
spray chamber
spray
heat exchanger
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
Application number
JP59119101A
Other languages
Japanese (ja)
Other versions
JPS60263049A (en
Inventor
Osamu Sakuma
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.)
WAKO PURANTO KK
Original Assignee
WAKO PURANTO KK
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 WAKO PURANTO KK filed Critical WAKO PURANTO KK
Priority to JP59119101A priority Critical patent/JPS60263049A/en
Publication of JPS60263049A publication Critical patent/JPS60263049A/en
Publication of JPH0585819B2 publication Critical patent/JPH0585819B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H1/00Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
    • F24H1/18Water-storage heaters
    • F24H1/20Water-storage heaters with immersed heating elements, e.g. electric elements or furnace tubes

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
  • Heat-Pump Type And Storage Water Heaters (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〕 本発明は金属表面処理設備における液槽の加熱
装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a heating device for a liquid bath in metal surface treatment equipment.

〔従来の技術〕[Conventional technology]

金属の表面処理工程たとえば脱脂、皮膜化成、
湯洗、塗装、耐水処理などの工程においては、加
工液を貯えた槽を所定温度に加熱することが必要
となる。このような液槽を加熱する場合、従来で
は液槽内に加熱用コイルや加熱用パネルを配設し
て温水ボイラやスチームボイラから加熱媒体を供
給する手法や、液槽を外周から直接加熱する直火
方式が採用されていた。
Metal surface treatment processes such as degreasing, film formation,
In processes such as hot water washing, painting, and water resistance treatment, it is necessary to heat a tank containing processing liquid to a predetermined temperature. When heating such a liquid tank, conventional methods include placing a heating coil or heating panel inside the liquid tank and supplying the heating medium from a hot water boiler or steam boiler, or heating the liquid tank directly from the outer periphery. An open flame method was used.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら、上記のような加熱手段で液槽の
加熱を行つた場合、加熱用コイルや加熱用パネル
などの熱交換器や槽底などに水垢やスラツジが付
着するので、伝熱効果が短期間のうちに著しく低
下し、燃比が悪化する。また、付着した水垢やス
ラツジを頻繁に除去する必要があるためメンテナ
ンスが非常に面倒でコストがかかり、また水垢や
スラツジ除去により操業を中断する必要があるた
め、操業率が不必要に低下するという問題があつ
た。
However, when heating a liquid tank using the above-mentioned heating means, limescale and sludge adhere to the heat exchangers such as heating coils and heating panels, and the bottom of the tank, so that the heat transfer effect is limited for a short period of time. It will drop significantly over time, and the fuel ratio will deteriorate. In addition, maintenance is extremely troublesome and costly as it is necessary to frequently remove scale and sludge, and the operation rate must be interrupted due to the removal of scale and sludge, which unnecessarily reduces the operating rate. There was a problem.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は上記の問題点を解消し、ヒータや槽底
に水垢やスラツジを固着させず伝熱効率の低下を
確実に防止することができる液槽の加熱装置を提
供することを目的とする。
SUMMARY OF THE INVENTION An object of the present invention is to provide a heating device for a liquid tank that can solve the above-mentioned problems and can reliably prevent a decrease in heat transfer efficiency without causing lime scale or sludge to adhere to the heater or the bottom of the tank.

この目的を達成するため本発明は、従来の発想
を転換し、液槽中で液を直接加熱するのでなく、
液槽に通ずるスプレー室に加熱手段を配設し、液
槽から導いた液をスプレーし加熱手段と接触させ
たのち液槽に流入させる循環回路を採用すること
により水垢やスラツジの付着防止を図りつつ液の
加熱を行うようにしたものである。
In order to achieve this objective, the present invention changes the conventional idea, and instead of directly heating the liquid in a liquid tank,
A heating means is installed in the spray chamber leading to the liquid tank, and a circulation circuit is adopted in which the liquid led from the liquid tank is sprayed, brought into contact with the heating means, and then flows into the liquid tank to prevent limescale and sludge from adhering. The liquid is then heated.

すなわち本発明の特徴とするところは、液槽の
上部にスプレー室を設け、スプレー室の上部には
被処理物Wを移送するコンベアを設け、スプレー
室には被処理物に液を吹付けるスプレーノズル機
構を配設しこれを循環用配管で液槽に接続した形
式の金属表面処理設備において、液槽の液面より
上位レベルの前記スプレー室内に外部の熱媒体供
給手段から熱媒体の供給を受ける熱交換器を横設
し、スプレーノズル機構から被処理物に噴射され
た用液を該熱交換器に接触させ、液槽に流下させ
るように構成したことを特徴とする金属表面処理
設備における液槽の加熱装置。
In other words, the present invention is characterized in that a spray chamber is provided above the liquid tank, a conveyor for transporting the object W to be treated is provided above the spray chamber, and a sprayer for spraying the liquid onto the object W is provided in the spray chamber. In metal surface treatment equipment in which a nozzle mechanism is installed and connected to a liquid tank via circulation piping, a heat medium is supplied from an external heat medium supply means into the spray chamber at a level above the liquid level of the liquid tank. A metal surface treatment equipment characterized in that a receiving heat exchanger is installed horizontally, and the working liquid sprayed onto the workpiece from a spray nozzle mechanism is brought into contact with the heat exchanger and flows down into a liquid tank. Liquid tank heating device.

〔実施例〕〔Example〕

以下本発明の実施例を添付図面に基いて説明す
る。
Embodiments of the present invention will be described below with reference to the accompanying drawings.

第1図は本発明に係る液槽加熱装置の一実施例
を示すもので、被処理物に用液をスプレーする設
備に適用した場合を示している。図面において、
1は液槽であり、用液たとえば化成処理剤、脱脂
剤、湯洗用液、耐水処理剤などを収容するように
なつている。2は液槽1の上部に設けられたスプ
レー室であり、下部など少なくとも一部をもつて
液槽1と連通している。3は前記スプレー室2に
配設されたスプレーノズル機構である。
FIG. 1 shows an embodiment of the liquid tank heating device according to the present invention, and shows a case where the device is applied to equipment for spraying a treatment liquid onto an object to be treated. In the drawing,
Reference numeral 1 denotes a liquid tank, which accommodates cleaning liquids such as chemical conversion treatment agents, degreasing agents, hot water washing liquids, and water resistance treatment agents. A spray chamber 2 is provided at the upper part of the liquid tank 1, and communicates with the liquid tank 1 through at least a portion such as the lower part. 3 is a spray nozzle mechanism arranged in the spray chamber 2.

5は循環用配管で、一端をもつて液槽中に接続
されると共に、他端をもつて前記スプレーノズル
機構3に接続されており、中間にはポンプPが介
在接続されている。
Reference numeral 5 denotes a circulation pipe, which is connected at one end to the liquid tank and at the other end to the spray nozzle mechanism 3, with a pump P interposed and connected in the middle.

6は用液の加熱手段さらに詳細には熱交換部で
あり、内部に温水やスチームあるいは熱風などの
熱媒体が流通するようになつている。本発明にお
いて、前記熱交換器6は液槽1の用液レベルより
高いスプレー室内に配設され、スプレーノズル機
構3から噴射される用液が接触するようになつて
いる。熱交換器6は熱媒体供給手段7たとえばボ
イラーと接続されている。
Reference numeral 6 denotes a heating means for the liquid, more specifically a heat exchange section, through which a heat medium such as hot water, steam, or hot air flows. In the present invention, the heat exchanger 6 is disposed in a spray chamber whose level is higher than the liquid level in the liquid tank 1, so that the liquid sprayed from the spray nozzle mechanism 3 comes into contact with the heat exchanger 6. The heat exchanger 6 is connected to a heat medium supply means 7, such as a boiler.

熱交換器6は一般に反転屈曲パイプや格子状、
さん状など用液が通過し得る構造のものが適当で
ある。
The heat exchanger 6 is generally an inverted bent pipe, a lattice type,
It is suitable to have a structure that allows the liquid to pass through, such as a grating shape.

第2図ないし第4図は本発明を金属製品のスプ
レー式前処理設備に適用した一実施例を示すもの
で、薬液ゾーン4Aと、これに続く複数段の洗浄
ゾーン4B,4C,4D,4Eからなつている。
それら各ゾーンは下側に液槽1a,1b,1c,
1d,1eが設けられ、液槽の上部にはトンネル
状のスプレー室2が設けられている。そしてスプ
レー室2の上部にはコンベア8が架設され、被処
理物Wが所定の速度で移送されるようになつてい
る。
Figures 2 to 4 show an embodiment in which the present invention is applied to spray-type pretreatment equipment for metal products, which includes a chemical liquid zone 4A and a plurality of cleaning zones 4B, 4C, 4D, and 4E following this. It is made up of
Each of these zones has liquid tanks 1a, 1b, 1c,
1d and 1e are provided, and a tunnel-shaped spray chamber 2 is provided above the liquid tank. A conveyor 8 is installed above the spray chamber 2, and the workpiece W is transported at a predetermined speed.

各ゾーンの液槽1a〜1eには循環用配管5a
〜5eが設けられ、ポンプP1〜P5により用液を
スプレー室内のスプレーノズル機構3a〜3eに
供給するようになつている。
Circulation piping 5a is provided in the liquid tanks 1a to 1e of each zone.
5e are provided, and the pumps P 1 to P 5 supply the liquid to the spray nozzle mechanisms 3a to 3e in the spray chamber.

そして、薬液ゾーン4Aの液槽より上のスプレ
ー室下部域には熱交換器6が水平状に配設され、
一端は温水ボイラの如き熱媒体供給手段7に接続
されている。
A heat exchanger 6 is disposed horizontally in the lower area of the spray chamber above the liquid tank of the chemical liquid zone 4A.
One end is connected to a heat medium supply means 7 such as a hot water boiler.

第5図はさらに本発明の他の実施例を示すもの
で、洗浄ゾーン4B〜4Eの循環用配管5a〜5
eにバイパス管9b〜9eが設けられ、それらバ
イパス管はそれぞれ前段ゾーンの出口部(液切り
用の境界ゾーン)に延出され、先端にスプレーノ
ズル10b〜10eが設けられている。さらに最
終ゾーンの出口部には新水配管11が導かれ補給
スプレーノズル12により新水をスプレー供給す
るようになつている。
FIG. 5 further shows another embodiment of the present invention, in which circulation piping 5a to 5 of cleaning zones 4B to 4E are shown.
Bypass pipes 9b to 9e are provided in e, and each of these bypass pipes extends to the outlet of the front stage zone (boundary zone for liquid draining), and spray nozzles 10b to 10e are provided at the tip. Further, a fresh water pipe 11 is led to the outlet of the final zone, and a replenishment spray nozzle 12 sprays fresh water.

そして、各バイパス管9b〜9eにはそれぞれ
電磁バルブなどのコントロールバルブ13b〜1
3eが設けられ、第1洗浄ゾーン4Bにおけるコ
ントロールバルブ13bは薬液ゾーン4Aの液槽
1aに設けたレベルスイツチ14aにより作動す
るようになつており、第2洗浄ゾーン4Cのコン
トロールバルブ13cは第1洗浄ゾーン4Bの液
槽1bに設けたレベルスイツチ14bにより作動
するようになつており、以下同様にバイパス管9
dは前段の液槽1cのレベルスイツチ14cと、
バイパス管9eは前段の薬槽1dのレベルスイツ
チ14dと夫々接続されている。最終洗浄ゾーン
4Eの新水配管11には余剰水が生じないように
するため液槽1eに設けた高水位用を低水位用の
各レベルスイツチ14e,14e′により作動する
水位調整バルブ15,15′が設けられている。
前記構成により前記各洗浄ゾーンのスプレー室に
送る洗浄水の量と前段のスプレー室に送る洗浄水
の量は、100〜(1〜0.1)の範囲となるように自
動制御され、これにより水洗効率を高め、前段ゾ
ーンからの用液の持込み量を最小限にする。
Control valves 13b to 1, such as electromagnetic valves, are provided in each of the bypass pipes 9b to 9e, respectively.
3e, the control valve 13b in the first cleaning zone 4B is operated by a level switch 14a provided in the liquid tank 1a of the chemical zone 4A, and the control valve 13c in the second cleaning zone 4C is operated in the first cleaning zone 4B. It is operated by a level switch 14b provided in the liquid tank 1b of zone 4B, and the bypass pipe 9 is operated in the same manner.
d is the level switch 14c of the liquid tank 1c in the previous stage;
The bypass pipes 9e are respectively connected to the level switches 14d of the preceding medicine tank 1d. In order to prevent excess water from forming in the new water pipe 11 of the final cleaning zone 4E, water level adjustment valves 15, 15 are operated by the high water level and low water level level switches 14e, 14e' provided in the liquid tank 1e. ' is provided.
With the above configuration, the amount of washing water sent to the spray chamber of each washing zone and the amount of washing water sent to the preceding spray room are automatically controlled to be in the range of 100 to (1 to 0.1), thereby improving the water washing efficiency. and minimize the amount of liquid brought in from the front zone.

一方、前記薬液ゾーン4Aのスプレー室下部域
には熱交換器6が横設され、その一端は外部の熱
媒体供給手段7に導かれている。
On the other hand, a heat exchanger 6 is installed horizontally in the lower area of the spray chamber of the chemical zone 4A, and one end of the heat exchanger 6 is led to an external heat medium supply means 7.

そして、薬液ゾーン4Aの入口部にはスリツト
状など任意構造の熱風吹込み部16が設けられ高
温ガスカーテンが形成されるようになつており、
この熱風吹込み部16に焼付炉、乾燥炉などの他
の加熱設備17から導いた廃熱配管18が接続さ
れている。この廃熱配管18は必要に応じ、図示
するように熱媒体供給手段7の加熱源17′から
の廃熱が導入されてもよい。
A hot air blowing section 16 having an arbitrary structure such as a slit shape is provided at the entrance of the chemical liquid zone 4A, so that a high temperature gas curtain is formed.
A waste heat pipe 18 led from other heating equipment 17 such as a baking furnace and a drying furnace is connected to this hot air blowing section 16. If necessary, waste heat from a heating source 17' of the heat medium supply means 7 may be introduced into the waste heat pipe 18 as shown.

さらに、薬液ゾーン4Aの近傍好ましくは薬液
ゾーン4Aと第1洗浄ゾーン4Bの中間位置に吸
引排気部19が設けられ、該吸引排気部19は気
液分離器20とロードフアン21を備えた排気ダ
クト22に接続されている。
Further, a suction/exhaust section 19 is provided near the chemical zone 4A, preferably at an intermediate position between the chemical zone 4A and the first cleaning zone 4B, and the suction/exhaust section 19 is an exhaust duct equipped with a gas-liquid separator 20 and a load fan 21. 22.

なお、本発明はいわゆる単槽式の場合にも適用
されるのは勿論であり、また第1図の実施例にお
いて第5図の実施例と同様な熱風吹込み部16や
吸引排気構造を採用し得るのは勿論である。
It should be noted that the present invention is of course applicable to the so-called single-tank type, and in the embodiment shown in FIG. 1, the same hot air blowing section 16 and suction/exhaust structure as in the embodiment shown in FIG. Of course it is possible.

〔作用〕[Effect]

本発明は上記のような構成からなるので、操業
にあたつては、熱媒体供給手段7から熱交換器6
に熱媒体を供給しつつ、ポンプPを駆動して液槽
1から用液を取出し、これをスプレーノズル機構
3に供給する。
Since the present invention has the above-described configuration, during operation, the heat medium supply means 7 is connected to the heat exchanger 6.
While supplying a heat medium to the spray nozzle mechanism 3, the pump P is driven to take out the liquid from the liquid tank 1 and supply it to the spray nozzle mechanism 3.

スプレー室2は前記熱交換器6により雰囲気温
度が上昇しており、この状態で用液はスプレーノ
ズル機構3からスプレー室2に噴出され、シヤワ
ー状に落下する。第1図の実施例ではこの落下域
に熱交換器6が配設されているため、シヤワー状
に分散した用液は熱交換器6に接触して加熱さ
れ、液槽1に流入する。この動作が繰返されるこ
とにより液槽内の用液は加熱される。なお、スプ
レー室2に熱風吹込み部16を設けた場合には更
に急速に用液が加熱される。
The atmospheric temperature in the spray chamber 2 is raised by the heat exchanger 6, and in this state, the liquid is jetted from the spray nozzle mechanism 3 into the spray chamber 2 and falls in a shower shape. In the embodiment shown in FIG. 1, a heat exchanger 6 is disposed in this falling area, so that the shower-like dispersed liquid comes into contact with the heat exchanger 6, is heated, and flows into the liquid tank 1. By repeating this operation, the liquid in the liquid tank is heated. In addition, when the hot air blowing part 16 is provided in the spray chamber 2, the liquid is heated even more rapidly.

このようにして用液が一定温度まで上昇したな
らば、コンベア等の手段により被処理物Wを装入
するもので、該被処理物Wはスプレー室2を移送
されつつスプレーノズル機構3により用液が吹き
付けられる。
Once the temperature of the solution has risen to a certain level in this way, the object to be treated W is loaded by means such as a conveyor, and the object to be treated W is transported through the spray chamber 2 and used by the spray nozzle mechanism 3. Liquid is sprayed.

スプレーされた用液は液槽1に流下する前に必
ず熱交換器6に接触して加熱され、一方、熱交換
器6はまわりに静水がなく、スプレーされた用液
が接触することから、水垢やスラツジが常時物理
的に洗い落され、長期間の運転によつても水垢や
スラツジが付着しにくい。そのため安定した伝熱
効率に保たれ、省エネルギーになると共に、煩雑
なスラツジ類の除去作業が軽減され、作業性や運
転コストが大幅に改善される。
The sprayed liquid always comes into contact with the heat exchanger 6 and is heated before flowing down into the liquid tank 1. On the other hand, since there is no still water around the heat exchanger 6 and the sprayed liquid comes into contact with it, Limescale and sludge are constantly physically washed away, making it difficult for limescale and sludge to adhere even after long-term operation. As a result, stable heat transfer efficiency is maintained, energy is saved, and the complicated work of removing sludge is reduced, greatly improving workability and operating costs.

また、スプレー室2に熱交換器6を設けること
により、前記のようにスプレー室の雰囲気温度が
上昇するため、空気中の水分飽和量が増加する。
そのため用液がノズルによりミスト化されること
とあいまち蒸発速度が早くなる。このため、本発
明を蒸発手段に適用すれば、液槽の効率よい加熱
と余剰水分の効果的な蒸発があわせて達成され
る。
Further, by providing the heat exchanger 6 in the spray chamber 2, the atmospheric temperature of the spray chamber increases as described above, and therefore the amount of water saturation in the air increases.
Therefore, the liquid is turned into a mist by the nozzle, and the evaporation rate becomes faster. Therefore, if the present invention is applied to the evaporation means, efficient heating of the liquid tank and effective evaporation of excess water can be achieved at the same time.

第5図のような連続式表面処理設備に適用した
場合には、被処理物が常に出口側で次段からの洗
浄液により洗浄され、しかも、入口側からの熱風
導入と薬液ゾーン4Aのスプレー室への熱交換器
6の配設および薬液ゾーン出口側からの吸引排気
により、薬液ゾーンでの薬液温度低下が著減する
と共に、きわめて効果的な水分蒸発が行われ、そ
れらにより余剰水を生じさせなずしかも水洗効率
の高い表面処理を行える。
When applied to a continuous surface treatment equipment as shown in Fig. 5, the object to be treated is always cleaned by the cleaning liquid from the next stage on the outlet side, and hot air is introduced from the inlet side and the spray chamber of chemical zone 4A is used. The arrangement of the heat exchanger 6 in the chemical zone and the suction exhaust from the chemical zone outlet side significantly reduce the drop in chemical temperature in the chemical zone, and extremely effective water evaporation is carried out, thereby producing excess water. Surface treatment can be performed easily and with high water washing efficiency.

〔発明の効果〕〔Effect of the invention〕

以上説明した本発明によるときには、液槽1の
上部にスプレー室2を設け、スプレー室2の上部
には被処理物Wを移送するコンベア8を設け、ス
プレー室2には被処理物Wに液を吹付けるスプレ
ーノズル機構3を配設しこれを循環用配管5で液
槽1に接続した形式の金属表面処理設備におい
て、液槽1の液面より上位レベルの前記スプレー
室2内に外部の熱媒体供給手段7から熱媒体の供
給を受ける熱交換器6を横設し、スプレーノズル
機構3から被処理物Wに噴射された用液を該熱交
換器6に接触させ、液槽1に流下させるようにし
たので、被処理物Wを処理するための加工液がス
プレーノズル機構3から噴出すると、そのスプレ
ー液は液槽1に落ちる前に、外部の熱媒体供給手
段7から熱媒体の供給を受けている熱交換器6と
接触して加熱され、液槽1に戻される。したがつ
て加工液が付着スラツジが生じやすい性質であつ
ても熱交換器6は常時スラツジが洗い落される。
したがつて、簡単な構造により加熱手段や槽底に
水垢やスラツジを固着させず良好な伝熱効率を得
ることができ、またスラツジ類の固着に伴う煩雑
な作業を軽減し、メンテナンスを簡易化、低コス
ト化することができるなどのすぐれた効果が得ら
れる。
According to the present invention described above, the spray chamber 2 is provided above the liquid tank 1, the conveyor 8 for transporting the object W to be processed is provided above the spray chamber 2, and the spray chamber 2 is provided with a spray chamber 2 for transferring the object W to be processed. In a metal surface treatment equipment of the type in which a spray nozzle mechanism 3 for spraying is arranged and connected to a liquid tank 1 through a circulation piping 5, an external A heat exchanger 6 that receives the heat medium from the heat medium supply means 7 is installed horizontally, and the liquid sprayed onto the workpiece W from the spray nozzle mechanism 3 is brought into contact with the heat exchanger 6 and transferred to the liquid tank 1. Since the processing liquid is made to flow down, when the processing liquid for treating the workpiece W is ejected from the spray nozzle mechanism 3, the spray liquid is supplied with heat medium from the external heat medium supply means 7 before falling into the liquid tank 1. It comes into contact with the heat exchanger 6 receiving the supply, is heated, and is returned to the liquid tank 1. Therefore, even if the machining liquid has a property that sludge tends to form, the sludge is constantly washed off from the heat exchanger 6.
Therefore, due to its simple structure, it is possible to obtain good heat transfer efficiency without causing limescale or sludge to stick to the heating means or the bottom of the tank.It also reduces the complicated work associated with sticking of sludge, and simplifies maintenance. Excellent effects such as cost reduction can be obtained.

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

第1図は本発明に係る液槽の加熱装置の一実施
例を示す部分切欠斜視図、第2図は本発明を銀族
表面処理ラインに適用した実施例を示す平面図、
第3図は第2図−線に沿う断面図、第4図は
同じくその部分切欠側面図、第5図は本発明を適
用した金属表面処理ラインに適用した別の実施例
を示す断面図である。 1……液槽、2……スプレー室、3……スプレ
ーノズル機構、5……循環用配管、6……熱交換
器、7……熱媒体供給手段、W……被処理物。
FIG. 1 is a partially cutaway perspective view showing an embodiment of a liquid bath heating device according to the present invention, and FIG. 2 is a plan view showing an embodiment in which the present invention is applied to a silver group surface treatment line.
FIG. 3 is a sectional view taken along the line of FIG. 2, FIG. 4 is a partially cutaway side view thereof, and FIG. 5 is a sectional view showing another embodiment in which the present invention is applied to a metal surface treatment line. be. DESCRIPTION OF SYMBOLS 1... Liquid tank, 2... Spray room, 3... Spray nozzle mechanism, 5... Circulation piping, 6... Heat exchanger, 7... Heat medium supply means, W... Treated object.

Claims (1)

【特許請求の範囲】[Claims] 1 液槽1の上部にスプレー室2を設け、スプレ
ー室2の上部には被処理物Wを移送するコンベア
8を設け、スプレー室2には被処理物Wに液を吹
付けるスプレーノズル機構3を配設しこれを循環
用配管5で液槽1に接続した形式の金属表面処理
設備において、液槽1の液面より上位レベルの前
記スプレー室2内に外部の熱媒体供給手段7から
熱媒体の供給を受ける熱交換器6を横設し、スプ
レーノズル機構3から被処理物Wに噴射された用
液を該熱交換器6に接触させ、液槽1に流下させ
るように構成したことを特徴とする金属表面処理
設備における液槽の加熱装置。
1 A spray chamber 2 is provided in the upper part of the liquid tank 1, a conveyor 8 is provided in the upper part of the spray chamber 2 to transfer the object W to be processed, and a spray nozzle mechanism 3 is provided in the spray chamber 2 to spray the liquid onto the object W to be processed. In this metal surface treatment equipment, heat is supplied from an external heat medium supply means 7 to the spray chamber 2 at a level above the liquid level of the liquid tank 1. A heat exchanger 6 that receives a medium supply is installed horizontally, and the liquid sprayed from the spray nozzle mechanism 3 onto the object W to be treated is brought into contact with the heat exchanger 6 and flows down into the liquid tank 1. A heating device for a liquid tank in metal surface treatment equipment, characterized by:
JP59119101A 1984-06-12 1984-06-12 Heating device for liquid tank Granted JPS60263049A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59119101A JPS60263049A (en) 1984-06-12 1984-06-12 Heating device for liquid tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59119101A JPS60263049A (en) 1984-06-12 1984-06-12 Heating device for liquid tank

Publications (2)

Publication Number Publication Date
JPS60263049A JPS60263049A (en) 1985-12-26
JPH0585819B2 true JPH0585819B2 (en) 1993-12-08

Family

ID=14752928

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59119101A Granted JPS60263049A (en) 1984-06-12 1984-06-12 Heating device for liquid tank

Country Status (1)

Country Link
JP (1) JPS60263049A (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5343254U (en) * 1977-09-16 1978-04-13
JPS58167835U (en) * 1982-05-04 1983-11-09 大阪瓦斯株式会社 heat exchange equipment

Also Published As

Publication number Publication date
JPS60263049A (en) 1985-12-26

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