JP2702523B2 - Processing solution thermostat - Google Patents

Processing solution thermostat

Info

Publication number
JP2702523B2
JP2702523B2 JP63264759A JP26475988A JP2702523B2 JP 2702523 B2 JP2702523 B2 JP 2702523B2 JP 63264759 A JP63264759 A JP 63264759A JP 26475988 A JP26475988 A JP 26475988A JP 2702523 B2 JP2702523 B2 JP 2702523B2
Authority
JP
Japan
Prior art keywords
water
processing liquid
pipe
liquid
circuit
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 - Fee Related
Application number
JP63264759A
Other languages
Japanese (ja)
Other versions
JPH02111471A (en
Inventor
正利 宮崎
勇 松岡
明彦 鈴木
増利 竿尾
進 吉田
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.)
Honda Motor Co Ltd
Original Assignee
Honda Motor 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 Honda Motor Co Ltd filed Critical Honda Motor Co Ltd
Priority to JP63264759A priority Critical patent/JP2702523B2/en
Publication of JPH02111471A publication Critical patent/JPH02111471A/en
Application granted granted Critical
Publication of JP2702523B2 publication Critical patent/JP2702523B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、例えば自動車の車体等表面への塗装前に行
なわれる浸漬法による化成処理に際し、前処理液の恒温
を保持する恒温装置の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to an improvement of a thermostatic apparatus for maintaining a thermostat of a pretreatment liquid in a chemical conversion treatment by a dipping method performed before painting a surface of an automobile body or the like. About.

(従来の技術) 従来例えば自動車の車体等の鋼板に防錆性を与え、塗
膜被着性を高めるため、電着塗装等の前には鋼板の化成
処理を行なっている。この化成処理はリン酸塩を主成分
とする前処理液を用い、第2図に示すように本槽101の
中に前処理液102を満たし、この本槽101の上方に設けた
搬送路103をハンガー104に載せられた被処理物105が通
過すると、途中で本槽処理液102中に浸漬し処理される
方法が一般的である。この際、表面処理を効率的にしか
も表面を均一に仕上げるため、この処理液を加熱して使
用している。すなわち、本槽101に並設されたオーバー
フロー槽106の導出管107から処理液を熱交換器108の通
路に導き、他方の通路に構成される高温流体回路109に
よって加熱して導入管110を経て本槽101に戻し、これを
循環せしめている。
(Prior Art) Conventionally, for example, in order to impart rust resistance to a steel plate of an automobile body or the like and enhance coating film adhesion, a chemical conversion treatment of the steel plate is performed before electrodeposition coating or the like. This chemical conversion treatment uses a pretreatment liquid containing phosphate as a main component, and as shown in FIG. 2, a main tank 101 is filled with a pretreatment liquid 102, and a transport path 103 provided above the main tank 101 is provided. When the object 105 placed on the hanger 104 passes through the container, the substrate is generally immersed in the main bath processing liquid 102 to be processed. At this time, this treatment liquid is heated and used in order to efficiently and uniformly finish the surface treatment. That is, the processing liquid is led from the outlet pipe 107 of the overflow tank 106 arranged in parallel to the main tank 101 to the passage of the heat exchanger 108, heated by the high-temperature fluid circuit 109 formed in the other passage, and passed through the inlet pipe 110. It is returned to the main tank 101 and circulated.

一方この表面処理の際、処理液中にはリン酸塩化合物
等のスラッジが発生し、このスラッジがオーバーフロー
槽106に混入して導出管107に入り込み、熱交換器108の
通路内壁に付着するという問題があった。このため熱交
換の効率を低下せしめないため、定期的にラインを停止
して硝酸等の酸で洗浄しスラッジを溶かしていた。
On the other hand, at the time of this surface treatment, sludge such as a phosphate compound is generated in the treatment liquid, and the sludge is mixed into the overflow tank 106, enters the outlet pipe 107, and adheres to the inner wall of the passage of the heat exchanger 108. There was a problem. For this reason, in order not to lower the efficiency of heat exchange, the line was periodically stopped and washed with an acid such as nitric acid to dissolve the sludge.

又、このような浸漬処理液の熱交換器ではないが、他
の装置の熱交換器単体の洗浄装置としては、例えば特開
昭61-122497号のような装置も知られる。この場合、熱
交換器を通過する高温のガスが熱交換により急冷されて
水蒸気化し、有害成分を含有する腐食性の凝縮水が通路
管に溜まり、有害成分が内壁に付着して悪影響を及ぼす
のを除去するためのものであり、内部に溜まる凝縮水を
集め、この中の特定成分の濃度を検出して、一定値以上
になると自動的に洗浄液を流し洗浄するというものであ
る。
Although not a heat exchanger for such an immersion treatment liquid, an apparatus as disclosed in, for example, JP-A-61-122497 is also known as a cleaning apparatus for a single heat exchanger of another apparatus. In this case, the high-temperature gas passing through the heat exchanger is rapidly cooled by heat exchange and turned into steam, and corrosive condensed water containing harmful components accumulates in the passage pipe, and the harmful components adhere to the inner wall and have an adverse effect. Is to collect the condensed water accumulated in the inside, detect the concentration of a specific component in the collected water, and when the concentration exceeds a certain value, automatically wash the washing by flowing a washing liquid.

(発明が解決しようとする課題) しかし、従来の塗装前処理液の恒温装置の場合、熱交
換器を洗浄するためラインを非稼動にする必要があり又
分解して硝酸等の酸で洗浄する作業を手動で行なう必要
から、工数がかかるとともに危険を伴っていた。更に酸
洗いした後拭取りを忘れたりすると腐食等の原因ともな
っていた。又特開昭61-122497号のような装置にあって
も洗浄中に装置を非稼動にしなければならない点につい
ては従来の前処理液の恒温装置と同様であった。
(Problems to be Solved by the Invention) However, in the case of the conventional thermostat of the coating pretreatment liquid, it is necessary to deactivate the line in order to clean the heat exchanger, and to disassemble and clean with an acid such as nitric acid. Since the work has to be performed manually, it takes a lot of man-hours and involves risks. Furthermore, forgetting to wipe off after pickling has caused corrosion and the like. Further, even in the apparatus as disclosed in JP-A-61-122497, the point that the apparatus must be deactivated during cleaning is the same as the conventional pretreatment liquid constant temperature apparatus.

(課題を解決するための手段) かかる課題を解決するため本発明は、化成処理液に満
たした液槽から処理液を導出し、再び液槽へ処理液を戻
す循環管路の途中に、並列的に且つ流路切換可能に複数
配置された熱交換器を有する処理液循環管路と、該処理
液循環管路に連結する洗浄回路路と、通気、通水回路と
を設けた処理液の恒温装置において、処理液循環管路に
エア、及び水を選択的に供給する通気、通水管を設け、
且つ該通気、通水管へのエア、水の供給で、該エア、水
と一緒にスラッジ等を排出する排出管を、通気、通水管
と接続するように設けた。
(Means for Solving the Problems) In order to solve the above problems, the present invention provides a method in which a processing liquid is derived from a liquid tank filled with a chemical conversion processing liquid and is returned to the liquid tank again. Liquid circulation line having a plurality of heat exchangers arranged in a manner capable of switching the flow paths, a cleaning circuit connected to the processing liquid circulation line, and a ventilation and water passage circuit. In the constant temperature device, air and water are selectively supplied to the treatment liquid circulation pipe, and a water supply pipe is provided,
In addition, a discharge pipe for discharging sludge and the like together with the air and water by supplying air and water to the ventilation and water pipe is provided so as to be connected to the ventilation and water pipe.

(作用) 一つの熱交換器に洗浄の必要が生じた時には、他の熱
交換器を使用して化成処理を行なうことが出来、ライン
を停止させる必要がない。又洗浄作業も洗浄液、エア
ー、水を順次流通させることにより確実な洗浄が出来、
最後にエアーを流せば洗浄液の拭き残しもなくなる。更
に気液二相流のような掻き取り効果の高い組合せも可能
となる。
(Operation) When it is necessary to wash one heat exchanger, a chemical conversion treatment can be performed using another heat exchanger, and there is no need to stop the line. In addition, the washing work can be surely washed by sequentially passing the washing liquid, air and water,
If air is flowed at the end, there is no need to wipe off the cleaning liquid. Further, a combination having a high scraping effect such as a gas-liquid two-phase flow is also possible.

(実施例) 本発明の処理液の恒温装置の実施例について添付した
図面に基づき説明する。
(Example) An example of the processing liquid constant temperature apparatus of the present invention will be described with reference to the attached drawings.

第1図は本発明の恒温装置を用いた塗装前処理装置の
系統図を示し、(A)図が恒温装置の管路図、(B)図
が管路に設けられた電磁弁等を制御する制御回路で、一
方の熱交換器側のみの接続を示す説明図である。
FIG. 1 shows a system diagram of a coating pretreatment apparatus using a constant temperature apparatus of the present invention. FIG. 1 (A) shows a pipe diagram of the constant temperature apparatus, and FIG. 1 (B) shows a solenoid valve provided in the pipe. FIG. 5 is an explanatory diagram showing connection of only one heat exchanger side in a control circuit to be performed.

被処理物1は搬送路2を移動するハンガー3上に載置
され、本槽4上で処理液5中を通過し表面処理される。
この処理液5は昇温して用いられており、このため本槽
4とこの本槽4に隣接して設けられたオーバーフロー槽
6には恒温装置7が接続している。
The workpiece 1 is placed on a hanger 3 moving on a transport path 2, passes through a processing solution 5 on a main tank 4, and is subjected to surface treatment.
The processing liquid 5 is used at an elevated temperature. For this reason, a constant temperature device 7 is connected to the main tank 4 and an overflow tank 6 provided adjacent to the main tank 4.

この恒温装置7は、処理液5が循環する処理液循環回
路10と、洗浄液として硝酸を供給するための洗浄液回路
20と、圧縮エアー及び工業用水が選択的に供給できる通
気・通水回路40を備え、これら各回路10,20,40に設けた
電磁弁、ポンプ等を(B)図に示す制御回路50により自
動的に制御している。
The constant temperature device 7 includes a processing liquid circulation circuit 10 for circulating the processing liquid 5 and a cleaning liquid circuit for supplying nitric acid as a cleaning liquid.
20 and a ventilation / water passage circuit 40 capable of selectively supplying compressed air and industrial water. The solenoid valves, pumps, etc. provided in these circuits 10, 20, 40 are controlled by a control circuit 50 shown in FIG. Automatically controlling.

処理液循環回路10はオーバーフロー槽6と本槽4を結
んで構成され、オーバーフロー槽に接続する導出管11の
途中には導出ポンプ12が配設され、その後この導出管11
は2本の入口接続管13a,13bに分岐し、夫々の電磁弁14
a,14bを経て夫々の熱交換器15a,15bの入口Aに連結して
いる。すなわちこの処理液循環回路10には2個の熱交換
器15a,15bが並列的に設けられ、お互いの流路が切換可
能となっている。この熱交換器15a,15bは温水通路16a,1
6baを有し、この温水によって入口Aから出口Bまでの
処理液を加熱可能としている。又、出口Bには夫々の出
口接続管17a,17bが接続し、電磁弁18a,18bを経た後1本
の導入管19に纏まり、この導入管19は本槽4と連結して
処理液が循環するよう構成されている。
The processing liquid circulation circuit 10 is configured by connecting the overflow tank 6 and the main tank 4, and a discharge pump 12 is provided in the middle of a discharge pipe 11 connected to the overflow tank.
Branches into two inlet connection pipes 13a and 13b, and each solenoid valve 14
a and 14b are connected to the inlets A of the respective heat exchangers 15a and 15b. That is, the processing liquid circulation circuit 10 is provided with two heat exchangers 15a and 15b in parallel, and their flow paths can be switched. The heat exchangers 15a, 15b are connected to hot water passages 16a, 1
The treatment water from the inlet A to the outlet B can be heated by the hot water. Further, the outlet B is connected to respective outlet connection pipes 17a and 17b, and after passing through the solenoid valves 18a and 18b, is combined into one introduction pipe 19. The introduction pipe 19 is connected to the main tank 4, and the processing liquid is connected thereto. It is configured to circulate.

洗浄液回路20は洗浄液として用いられる硝酸を溜めた
洗浄槽21を備え、この洗浄槽21にはポンプ22及び電磁弁
23を配した洗浄液の供給管24が接続し、この供給管24は
2本の分岐供給管25a,25bに分岐した後、夫々の電磁弁2
6a,26bを経て前述の処理液循環管路10のうち熱交換器15
a,15bの出口Bと電磁弁18a,18bの間の出口接続管17a,17
bに夫々接続している。一方処理液循環回路10の入口接
続管13a,13b側には、電磁弁14a,14bと熱交換器の入口A
の間に電磁弁27a,27bを配した分岐排出管28a,28bを接続
し、これを1本の排出管29に連結して洗浄槽21に戻して
いる。又このように洗浄液を循環させるよう構成した回
路の途中すなわちポンプ22と電磁弁23の間の供給管24に
は電磁弁30を備えた配管31を接続し、攪拌装置32を有す
る中和槽33に導き、一方この中和槽33には中和剤槽34の
苛性ソーダ等からなる中和剤をポンプ35で送り込めるよ
う構成している。
The cleaning liquid circuit 20 includes a cleaning tank 21 for storing nitric acid used as a cleaning liquid. The cleaning tank 21 includes a pump 22 and an electromagnetic valve.
The supply pipe 24 of the cleaning liquid provided with 23 is connected to the supply pipe 24. The supply pipe 24 branches into two branch supply pipes 25a and 25b.
6a and 26b, the heat exchanger 15
Outlet connection pipes 17a, 17 between the outlet B of the a, 15b and the solenoid valves 18a, 18b
Each is connected to b. On the other hand, on the inlet connection pipes 13a and 13b side of the processing liquid circulation circuit 10, the solenoid valves 14a and 14b and the inlet A of the heat exchanger are connected.
Between them, branch discharge pipes 28a and 28b provided with solenoid valves 27a and 27b are connected, connected to one discharge pipe 29 and returned to the washing tank 21. Further, a pipe 31 provided with an electromagnetic valve 30 is connected to the supply pipe 24 between the pump 22 and the electromagnetic valve 23 in the circuit configured to circulate the cleaning liquid in this way, and a neutralization tank 33 having a stirring device 32 is provided. On the other hand, a neutralizing agent composed of caustic soda in a neutralizing agent tank 34 can be fed into the neutralizing tank 33 by a pump 35.

一方、通気・通水回路40は電磁弁41を備える通水管42
と、電磁弁43を備える通気管44を1本とした後分岐通気
・通水管45a,45bに分岐させ、夫々に電磁弁46a,46bを設
けて前記出口接続管17a,17bに接続している。この接続
箇所は電磁弁18a,18bと前述の洗浄液回路20の分岐供給
管25a,25bの接続箇所の間に選定している。又入口接続
管13a,13bにも電磁弁48a,48bを設けた通気・通水管47a,
47bを接続し、この接続箇所は電磁弁14a,14bと前述の洗
浄液回路20の分岐排出管28a,28bの間に選定するととも
に、この夫々の通気・通水管47a,47bは1本の排出管49
に接続している。
On the other hand, the ventilation / water passage circuit 40 is provided with a water passage pipe 42 having an electromagnetic valve 41.
Then, a single vent pipe 44 having an electromagnetic valve 43 is provided, and then branched into branch vent / water pipes 45a and 45b, and electromagnetic valves 46a and 46b are provided respectively and connected to the outlet connection pipes 17a and 17b. . This connection point is selected between the connection points between the solenoid valves 18a and 18b and the branch supply pipes 25a and 25b of the cleaning liquid circuit 20 described above. In addition, ventilation / flow pipes 47a, provided with solenoid valves 48a, 48b also at the inlet connection pipes 13a, 13b,
47b is connected between the solenoid valves 14a and 14b and the branch discharge pipes 28a and 28b of the washing liquid circuit 20. Each of the ventilation / water pipes 47a and 47b is connected to a single discharge pipe. 49
Connected to

制御回路50は、以上のような処理液循環回路10、洗浄
回路20及び通気・通水回路40を自動的に制御し、熱交換
器を自動洗浄するため設けられ、夫々の熱交換器15a,15
bの入口Aと出口B近傍の処理液循環回路に取り付けた
圧力計51と、この入口側の圧力P1と出口側の圧力P2の差
で電磁弁等を制御するコントローラー52を備え、このコ
ントローラー52は(B)図に示すような各電磁弁と接続
している。尚この(B)図は、一方の熱交換器15a側の
みの接続を示している。
The control circuit 50 is provided for automatically controlling the treatment liquid circulation circuit 10, the cleaning circuit 20, and the ventilation / water passage circuit 40 as described above, and for automatically cleaning the heat exchangers. Fifteen
b) a pressure gauge 51 attached to the processing liquid circulation circuit near the inlet A and the outlet B, and a controller 52 for controlling an electromagnetic valve or the like based on a difference between the pressure P1 on the inlet side and the pressure P2 on the outlet side. Are connected to the respective solenoid valves as shown in FIG. FIG. 2B shows the connection on only one heat exchanger 15a side.

このように構成した処理液の恒温装置の作動概要の一
例は次のとおりである。
An example of an outline of the operation of the processing liquid constant temperature apparatus configured as described above is as follows.

熱交換器15a側の通路にスラッジが凝着し内径が縮小
すると、A,B間に圧力差が生じ、圧力計51によって検出
された信号がコントローラー52に送られ自動洗浄が開始
される。まず当該熱交換器15a側の処理液循環回路を閉
鎖せしめるため、入口接続管13aの電磁弁14aと出口接続
管17aの電磁弁18aを閉じる。次いで通気・通水回路40の
電磁弁43,46a,48aを開き、エアーによって管路に残留す
る処理液を排出管49から排出する。次いで以上の電磁弁
43,46a,48aを閉じると洗浄液回路20の電磁弁23,26a,27a
を開き、ポンプ22を作動させて洗浄槽21内の硝酸を循環
させ、凝着するスラッジの溶解洗浄を行なう。所定時間
の酸洗いが終了すると電磁弁27aを残して残りの電磁弁2
3,26aを閉じ、電磁弁43,46aを開いて通気し残った酸を
洗浄槽21に圧送する。その後電磁弁43を閉じて通気を終
了すると通水管42の電磁弁41を開いて水で洗浄し、これ
も洗浄槽21に送り込む。最後に電磁弁46aを残して電磁
弁41及び27aを閉じ、通気管44の電磁弁43,48aを開いて
エアですべての残留物を排出管49から排出する。
When the sludge adheres to the passage on the side of the heat exchanger 15a and the inner diameter is reduced, a pressure difference is generated between A and B, a signal detected by the pressure gauge 51 is sent to the controller 52, and automatic cleaning is started. First, in order to close the processing liquid circulation circuit on the heat exchanger 15a side, the solenoid valve 14a of the inlet connection pipe 13a and the solenoid valve 18a of the outlet connection pipe 17a are closed. Next, the electromagnetic valves 43, 46a, 48a of the ventilation / water passage circuit 40 are opened, and the processing liquid remaining in the pipeline is discharged from the discharge pipe 49 by air. Then the above solenoid valve
When closing 43, 46a, 48a, the solenoid valves 23, 26a, 27a of the cleaning liquid circuit 20
Is opened, and the pump 22 is operated to circulate the nitric acid in the washing tank 21 to dissolve and wash the sludge that adheres. When the pickling for a predetermined time is completed, the remaining solenoid valve 2 is left, leaving the solenoid valve 27a.
The solenoid valves 43 and 46a are opened by closing the valves 3 and 26a, and the remaining acid is pumped to the washing tank 21 by ventilation. After that, when the solenoid valve 43 is closed to terminate the ventilation, the solenoid valve 41 of the water pipe 42 is opened to wash with water, and this is also sent to the washing tank 21. Finally, the solenoid valves 41 and 27a are closed except for the solenoid valve 46a, and the solenoid valves 43 and 48a of the ventilation pipe 44 are opened to discharge all the residue from the discharge pipe 49 by air.

一方、洗浄槽21の中のスラッジを溶かした硝酸は中和
槽33に送られ、中和剤槽34から送られる苛性ソーダと一
緒に攪拌中和され、系外に排出される。
On the other hand, the nitric acid in which the sludge in the cleaning tank 21 is dissolved is sent to the neutralization tank 33, neutralized by stirring together with the caustic soda sent from the neutralizing agent tank 34, and discharged out of the system.

尚、この通気・通水回路の通気と通水を同時に行な
い、気液2相流として掻き取り効果の高い洗浄方法も採
用可能である。
It should be noted that it is also possible to adopt a cleaning method that simultaneously performs ventilation and water passage in the ventilation / water passage circuit and has a high scraping effect as a gas-liquid two-phase flow.

又この間他方の熱交換器15bは正常運転しており、本
槽処理液の恒温維持は継続している。
During this time, the other heat exchanger 15b is operating normally, and the constant temperature of the processing solution in the main tank is maintained.

(発明の効果) 本発明は以上のように並列となった複数の熱交換器の
通路に洗浄液、エア、水が選択的に供給可能となるよう
構成したため、スラッジが溜まってこれを洗浄する時も
従来のようにラインを停止させることなく行なうことが
出来るようになった。又自動的にしかも簡易に洗浄でき
るため工数削減が可能となったばかりでなく硝酸等の危
険な薬品を直接取扱う必要がなくなり、災害防止上から
も有効なものである。
(Effects of the Invention) The present invention is configured such that the cleaning liquid, air, and water can be selectively supplied to the passages of the plurality of heat exchangers arranged in parallel as described above. Can be performed without stopping the line as in the prior art. In addition, since the washing can be performed automatically and easily, the number of man-hours can be reduced, and it is not necessary to directly handle dangerous chemicals such as nitric acid, which is effective for disaster prevention.

又本発明は、処理液循環管路にエア、及び水を選択的
に供給する通気、通水管を設け、且つ該通気、通水管へ
のエア、水の供給で、該エア、水と一緒にスラッジ等を
排出する排出管を、通気、通水管と接続するように設け
たので、処理液循環管路にエアと水とを通気、通水管に
供給することで、エア、水と一緒にスラッジ等を排出管
から排出させることができ、処理液の加熱作業を停止す
ることなく、安定して処理液の温度を保持しながら熱交
換器内部を洗浄することができる。
Also, the present invention provides a ventilation and water supply pipe for selectively supplying air and water to the treatment liquid circulation pipe, and supplies the air and water to the ventilation and water supply pipe together with the air and water. The exhaust pipe for discharging sludge etc. is provided so as to be connected to the ventilation and water passage pipes, so that air and water are ventilated to the treatment liquid circulation pipe and supplied to the water pipe, so that sludge is mixed with air and water. Can be discharged from the discharge pipe, and the inside of the heat exchanger can be washed while maintaining the temperature of the processing liquid stably without stopping the work of heating the processing liquid.

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

第1図は本発明の恒温装置を用いた塗装前処理装置の系
統図を示し、(A)図が恒温装置の管路図、(B)図が
管路に設けられた電磁弁等を制御する制御回路で、一方
の熱交換器側の接続を示す説明図、第2図が従来例を示
す系統図である。 尚同図中、1は被処理物、4は本槽、5は処理液、7は
恒温装置、10は処理液循環回路、15a,15bは熱交換器、2
0は洗浄液回路、21は洗浄槽、40は通気・通水回路、42
は通水管、44は通気管、49は排出管、50は制御回路、10
1は本槽、108は熱交換器、109は高温流体回路を示す。
FIG. 1 shows a system diagram of a coating pretreatment apparatus using a constant temperature apparatus of the present invention. FIG. 1 (A) shows a pipe diagram of the constant temperature apparatus, and FIG. 1 (B) shows a solenoid valve provided in the pipe. FIG. 2 is an explanatory diagram showing a connection on one heat exchanger side in a control circuit to be performed, and FIG. 2 is a system diagram showing a conventional example. In the figure, 1 is an object to be processed, 4 is a main tank, 5 is a processing liquid, 7 is a thermostat, 10 is a processing liquid circulation circuit, 15a and 15b are heat exchangers, 2
0 is a washing liquid circuit, 21 is a washing tank, 40 is a ventilation / water passage circuit, 42
Is a water pipe, 44 is a vent pipe, 49 is a drain pipe, 50 is a control circuit, 10
1 is a main tank, 108 is a heat exchanger, and 109 is a high-temperature fluid circuit.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 竿尾 増利 東京都新宿区西新宿2丁目6番1号 株 式会社大氣社内 (72)発明者 吉田 進 東京都新宿区西新宿2丁目6番1号 株 式会社大氣社内 (56)参考文献 特開 昭60−194083(JP,A) ────────────────────────────────────────────────── ─── Continued on the front page (72) Inventor Masuri Masao 2-6-1 Nishi-Shinjuku, Shinjuku-ku, Tokyo In-house Daiki Co., Ltd. (72) Inventor Susumu Yoshida 2-6-Nishishinjuku, Shinjuku-ku, Tokyo No. 1 Daiki Co., Ltd. (56) References JP-A-60-194083 (JP, A)

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】化成処理液を満たした液槽から処理液を導
出し、再び液槽へ処理液を戻す循環管路の途中に、並列
的に且つ流路切換可能に複数配置された熱交換器を有す
る処理液循環管路と、該処理液循環管路に連結する洗浄
回路路と、通気、通水回路とを設けた処理液の恒温装置
において、 前記処理液循環管路にエア、及び水を選択的に供給する
通気、通水管を設け、且つ該通気、通水管へのエア、水
の供給で、該エア、水と一緒にスラッジ等を排出する排
出管を、通気、通水管と接続するように設けた、 ことを特徴とする処理液の恒温装置。
1. A heat exchanger comprising a plurality of heat exchangers disposed in parallel and switchable in the middle of a circulation pipe for drawing out a processing liquid from a liquid tank filled with a chemical conversion processing liquid and returning the processing liquid to the liquid tank again. A processing liquid circulation line having a vessel, a cleaning circuit connected to the processing liquid circulation line, and a ventilating, a constant temperature apparatus for processing liquid provided with a water passage circuit, wherein the processing liquid circulation line has air, and A vent and a water pipe are provided for selectively supplying water, and a discharge pipe for discharging sludge and the like together with the air and the water by supplying the air and water to the water and the water pipe is provided with a vent and a water pipe. A constant temperature device for a processing liquid, which is provided so as to be connected.
JP63264759A 1988-10-20 1988-10-20 Processing solution thermostat Expired - Fee Related JP2702523B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63264759A JP2702523B2 (en) 1988-10-20 1988-10-20 Processing solution thermostat

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63264759A JP2702523B2 (en) 1988-10-20 1988-10-20 Processing solution thermostat

Publications (2)

Publication Number Publication Date
JPH02111471A JPH02111471A (en) 1990-04-24
JP2702523B2 true JP2702523B2 (en) 1998-01-21

Family

ID=17407792

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63264759A Expired - Fee Related JP2702523B2 (en) 1988-10-20 1988-10-20 Processing solution thermostat

Country Status (1)

Country Link
JP (1) JP2702523B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5421022B2 (en) * 2009-08-06 2014-02-19 日本ペイント工業用コ−ティング株式会社 Chemical liquid warming system and method for stopping the same

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60194083A (en) * 1984-03-14 1985-10-02 Kawatetsu Kohan Kk Automatic change-over device of heat exchanger for heating chemical converting liquid for pretreatment prior to painting

Also Published As

Publication number Publication date
JPH02111471A (en) 1990-04-24

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