JPH0642960U - Pretreatment device - Google Patents

Pretreatment device

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Publication number
JPH0642960U
JPH0642960U JP7998992U JP7998992U JPH0642960U JP H0642960 U JPH0642960 U JP H0642960U JP 7998992 U JP7998992 U JP 7998992U JP 7998992 U JP7998992 U JP 7998992U JP H0642960 U JPH0642960 U JP H0642960U
Authority
JP
Japan
Prior art keywords
sludge
discharge pipe
treatment liquid
sludge discharge
pretreatment tank
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.)
Granted
Application number
JP7998992U
Other languages
Japanese (ja)
Other versions
JP2594510Y2 (en
Inventor
野 仁 士 矢
口 徳 恭 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.)
Trinity Industrial Corp
Original Assignee
Trinity Industrial Corp
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 Trinity Industrial Corp filed Critical Trinity Industrial Corp
Priority to JP1992079989U priority Critical patent/JP2594510Y2/en
Publication of JPH0642960U publication Critical patent/JPH0642960U/en
Application granted granted Critical
Publication of JP2594510Y2 publication Critical patent/JP2594510Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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

Abstract

(57)【要約】 【目的】 前処理タンクの槽底を成す複数のV字底に沈
降したスラッジを前処理タンク内に舞い上がらせずにそ
のV字底に接続したスラッジ排出管から処理液と共に吸
引排出すると同時に、スラッジ排出管から吸引排出され
た処理液中のスラッジを効率良く除去する。 【構成】 前処理タンク1の各V字底4a〜4dとスラ
ッジ排出管6とを連結する各排水管7a〜7dに一定の
時間的間隔で順次開閉する自動バルブ8a〜8dを介装
することにより、各V字底4a〜4dからスラッジ排出
管6に吸引される処理液の流速を速めて前処理タンク1
内におけるスラッジの舞い上がりを防ぎ、スラッジ排出
管6に介装した遠心分離機13のスラッジ分離効率も高
める。
(57) [Summary] [Purpose] The sludge settling at the V-shaped bottoms of the pretreatment tank is not allowed to rise into the pretreatment tank, but is allowed to flow from the sludge discharge pipe connected to the V-bottom together with the treatment liquid. At the same time as suctioning and discharging, sludge in the processing liquid sucked and discharged from the sludge discharge pipe is efficiently removed. [Structure] Automatic valves 8a to 8d that sequentially open and close at regular time intervals are provided on the drainage pipes 7a to 7d connecting the V-shaped bottoms 4a to 4d of the pretreatment tank 1 and the sludge discharge pipes 6, respectively. Thus, the flow velocity of the treatment liquid sucked from the V-shaped bottoms 4a to 4d to the sludge discharge pipe 6 is increased, and the pretreatment tank 1
The sludge is prevented from soaring inside, and the sludge separation efficiency of the centrifugal separator 13 provided in the sludge discharge pipe 6 is also increased.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】[Industrial applications]

本考案は、塗装やメッキの前処理を行う前処理装置に関する。 The present invention relates to a pretreatment device for performing a pretreatment for painting or plating.

【0002】[0002]

【従来の技術】[Prior art]

自動車塗装の前処理を行う前処理装置は、コンベアのハンガに載せて移送され る自動車ボディ等の大型の被処理物を前処理タンクのメインタンク内に貯溜した 脱脂液や被膜化成液等の処理液中に浸漬するようになっている。 メインタンクの槽底には、その槽底に沈降するスラッジを集積させる複数のV 字底が形成され、各V字底には、その底に集積したスラッジを処理液と共にタン ク外に吸引排出するスラッジ排出管が接続され、スラッジ排出管から排出された 処理液は、セットリングタンク等の濾過器に通してスラッジを除去した後、再び メインタンク内に戻されるようになっている(実公昭63−761号公報)。 The pre-treatment device for pre-treatment of automobile coating is the treatment of degreasing liquid and film forming liquid etc. stored in the main tank of the pre-treatment tank for large objects such as automobile bodies that are transferred on the hanger of the conveyor. It is designed to be immersed in liquid. A plurality of V-shaped bottoms for accumulating sludge that settles on the tank bottom are formed on the bottom of the main tank, and the sludge accumulated on the bottom is sucked out of the tank together with the treatment liquid at each V-shaped bottom. The sludge discharge pipe is connected, and the treated liquid discharged from the sludge discharge pipe is passed through a filter such as a settling tank to remove the sludge, and then returned to the main tank again. 63-761).

【0003】[0003]

【考案が解決しようとする課題】[Problems to be solved by the device]

しかし、セットリングタンク等の濾過器はスラッジの除去効率があまり良くな いし、前処理タンクの各V字底に沈降集積したスラッジをスラッジ排出管で一斉 に吸引しているので、各V字底からスラッジ排出管に吸引される処理液の流速が 遅く、各V字底に一旦沈降したスラッジが再び舞い上がるという不具合を生じて いた。 However, filters such as settling tanks do not have very good sludge removal efficiency, and sludge that has settled and accumulated at each V-shaped bottom of the pretreatment tank is sucked all at once by the sludge discharge pipes. There was a problem that the flow rate of the processing liquid sucked from the sludge to the sludge discharge pipe was slow and sludge once settled at each V-bottom rose again.

【0004】 そこで本考案は、前処理タンクの各V字底に沈降したスラッジを舞い上がらせ ずにスラッジ排出管から吸引排出させると同時に、そのスラッジ排出管から吸引 排出されたスラッジを効率良く除去できるようにすることを技術的課題としてい る。Therefore, the present invention allows the sludge settling at each V-shaped bottom of the pretreatment tank to be sucked and discharged from the sludge discharge pipe without rising, and at the same time, the sludge sucked and discharged from the sludge discharge pipe can be efficiently removed. This is a technical issue.

【0005】[0005]

【課題を解決するための手段】[Means for Solving the Problems]

上記の課題を解決するために、本考案は、前処理タンクの槽底を成す複数のV 字底からその底に沈降したスラッジを処理液と共に吸引排出するスラッジ排出管 が設けられた前処理装置において、前記スラッジ排出管に処理液中のスラッジを 除去する遠心分離機が介装されると共に、前記スラッジ排出管と前記各V字底と を連結する各排水管に、一定の時間的間隔で順次開閉する自動バルブが介装され ていることを特徴とする。 In order to solve the above problems, the present invention provides a pretreatment device provided with a sludge discharge pipe for sucking and discharging sludge settled from a plurality of V-shaped bottoms forming the bottom of the pretreatment tank together with the treatment liquid. In the above, the sludge discharge pipe is provided with a centrifuge for removing sludge in the treatment liquid, and the drain pipes connecting the sludge discharge pipe and the V-shaped bottoms are arranged at regular time intervals. It is characterized by an automatic valve that opens and closes in sequence.

【0006】[0006]

【作用】[Action]

本考案によれば、前処理タンクの槽底を成す各V字底からスラッジ排出管を通 じて吸引排出される処理液中に含まれたスラッジが遠心分離機によって効率良く 除去される。 特に、本考案においては、前処理タンク内のスラッジを沈降集積させる各V字 底とそれらV字底からスラッジを吸引排出するスラッジ排出管とを連結する各排 水管に介装された自動バルブが、一定の時間的間隔で順次開閉して、スラッジ排 出管に介装された遠心分離機に送られる処理液中のスラッジ濃度が常に一定以上 に維持されるので、遠心分離機のスラッジ分離効率が著しく良い。 According to the present invention, the sludge contained in the treatment liquid sucked and discharged from each V-shaped bottom forming the bottom of the pretreatment tank through the sludge discharge pipe is efficiently removed by the centrifuge. In particular, in the present invention, there is an automatic valve provided in each drainage pipe that connects each V-shaped bottom for accumulating sludge in the pretreatment tank and a sludge discharge pipe for sucking and discharging the sludge from the V-shaped bottom. The sludge concentration in the centrifuge is kept constant because the sludge concentration in the treatment liquid sent to the centrifuge installed in the sludge discharge pipe is constantly maintained at a certain level by opening and closing the sludge at regular intervals. Is remarkably good.

【0007】 すなわち、前処理タンクの各V字底から間断なく一斉に処理液を吸引排出する と、その処理液中に含まれるスラッジの濃度が低いので遠心分離機のスラッジ分 離効率は低下するが、本考案のように前処理タンクの各V字底にある程度の量の スラッジが沈降集積するまで待って、スラッジが沈降集積したV字底から順に処 理液を吸引排出すれば、その処理液中のスラッジ濃度が高まって遠心分離機のス ラッジ分離効率も良好となる。 また、各V字底から処理液を一斉に吸引せずに、順次吸引すれば、その処理液 の流速が高まってV字底に沈降したスラッジの舞い上がりも防止される。That is, when the treatment liquid is sucked and discharged all at once from each V-shaped bottom of the pretreatment tank, the sludge separation efficiency of the centrifuge decreases because the concentration of sludge contained in the treatment liquid is low. However, as in the present invention, wait until a certain amount of sludge settles and accumulates at each V-shaped bottom of the pretreatment tank, and then suction and discharge the treatment liquid in order from the V-shaped bottom where the sludge settles and accumulates, the treatment. The sludge concentration in the liquid is increased and the sludge separation efficiency of the centrifuge is improved. Further, if the treatment liquid is not sucked simultaneously from the respective V-shaped bottoms but is sequentially sucked, the flow velocity of the treatment liquid is increased and the sludge settling at the V-shaped bottoms is prevented from rising.

【0008】[0008]

【実施例】【Example】

以下、本考案の実施例を図面によって説明する。 図1は本考案による前処理装置の一例を示すフローシート図、図2は本考案に 係る自動バルブの開閉動作を示すタイムチャートである。 Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a flow sheet diagram showing an example of a pretreatment device according to the present invention, and FIG. 2 is a time chart showing an opening / closing operation of an automatic valve according to the present invention.

【0009】 図中、1は、被処理物を処理液中に浸漬するメインタンク2と、そのメインタ ンク2からオーバーフローした処理液を貯溜するサブタンク3とから成る前処理 タンクであって、メインタンク2の槽底には、その槽底に沈降するスラッジを集 積させる複数のV字底4a,4b,4c及び4dが形成されると共に、これら各 V字底4a〜4dに沈降集積したスラッジをポンプ5で吸引排出するスラッジ排 出管6が、各V字底4a〜4dごとに設けた各排水管7a〜7dを介して接続さ れている。 また、スラッジ排出管6と各V字底4a〜4dとを連結する各排水管7a〜7 dには、一定の時間的間隔で順次開閉する電磁バルブ等の自動バルブ8a〜8d が夫々介装されている。In the figure, reference numeral 1 is a pretreatment tank consisting of a main tank 2 for immersing an object to be treated in a treatment liquid, and a sub-tank 3 for storing the treatment liquid overflowing from the main tank 2. A plurality of V-shaped bottoms 4a, 4b, 4c and 4d for accumulating sludge settling on the tank bottom are formed on the bottom of No. 2 and the sludge settled and accumulated on each of these V-shaped bottoms 4a to 4d is formed. A sludge discharge pipe 6 sucked and discharged by the pump 5 is connected via drainage pipes 7a to 7d provided for the respective V-shaped bottoms 4a to 4d. Further, automatic valves 8a to 8d such as electromagnetic valves that are sequentially opened and closed at fixed time intervals are installed in the drainage pipes 7a to 7d that connect the sludge discharge pipe 6 and the V-shaped bottoms 4a to 4d, respectively. Has been done.

【0010】 次に、9は、前処理タンク1内の処理液を熱交換器10に送る往管11と、熱 交換器10で加温された処理液を再び前処理タンク1に戻す返管12とで成る処 理液循環配管であって、往管11がスラッジ排出管6で形成されると共に、その 往管11には、スラッジ排出管6から排出される処理液に含まれたスラッジを除 去する遠心分離機13が介装されて、当該遠心分離機13でスラッジを除去した 清浄な処理液が熱交換器10に送液されるようになっており、それにより熱交換 器10の内部に熱貫流率を低下させるスラッジが付着することを防止している。 なお、遠心分離機13によって処理液中から分離したスラッジは、その遠心分 離機13に設けたドレン管14から系外に排出される。Next, 9 is a forward pipe 11 for sending the treatment liquid in the pretreatment tank 1 to the heat exchanger 10, and a return pipe for returning the treatment liquid heated in the heat exchanger 10 to the pretreatment tank 1 again. The sludge discharge pipe 6 is formed on the forward pipe 11 and the sludge contained in the treatment liquid discharged from the sludge discharge pipe 6 is supplied to the forward pipe 11. A centrifuge 13 for removal is interposed, and a clean treatment liquid from which sludge has been removed by the centrifuge 13 is sent to the heat exchanger 10, whereby the heat exchanger 10 It prevents sludge from adhering to the inside, which lowers the heat transmission coefficient. The sludge separated from the treatment liquid by the centrifugal separator 13 is discharged to the outside of the system from the drain pipe 14 provided in the centrifugal separator 13.

【0011】 また、熱交換器10を通じて加温された処理液を再び前処理タンク1に戻す返 管12は、メインタンク2の出槽側斜面に沈降したスラッジに処理液の噴流を吹 き付けてV字底4a〜4dに落とし込むスプレーライザー管15に接続され、メ インタンク2の入槽側斜面に沈降したスラッジをV字底4a〜4dに落とし込む スプレーライザー管16には、メインタンク2からサブタンク3内にオーバーフ ローした処理液をポンプ17でメインタンク2内に戻す循環配管18が接続され ている。 19は、スチーム管20から液中噴射される蒸気で加温した温水タンク21内 の温水をポンプ22によって熱交換器10に送り込む温水循環配管である。The return pipe 12 for returning the treatment liquid heated by the heat exchanger 10 to the pretreatment tank 1 again blows a jet of the treatment liquid onto the sludge settling on the outlet side slope of the main tank 2. Is connected to the spray riser pipe 15 that drops into the V-shaped bottoms 4a to 4d, and the sludge that settles on the inlet side slope of the main tank 2 drops into the V-shaped bottoms 4a to 4d. A circulation pipe 18 is connected to the processing liquid that has flowed into the sub tank 3 and returns it to the main tank 2 by a pump 17. Reference numeral 19 denotes a hot water circulation pipe for sending hot water in the hot water tank 21 heated by the steam injected from the steam pipe 20 into the heat exchanger 10 by the pump 22.

【0012】 しかして、前処理装置の稼働中は、自動バルブ8a〜8dが例えば図2のタイ ムチャートに示すようなローテーションに従って一定の時間的間隔で順次開閉さ れるようになされており、まず、V字底4aの排水管7aに介装した自動バルブ 8aが、V字底4a内に沈降堆積したスラッジを排出するために必要な一定時間 だけ開放され、その自動バルブ8aの開放中に、V字底4bの排水管7bに介装 した次なる自動バルブ8bが自動バルブ8aと同様の一定時間だけ開放される。 また、このようなタイミングで、自動バルブ8bの開放中に、V字底4cの排 水管7cに介装した自動バルブ8cが開放され、更に、その自動バルブ8cの開 放中に、V字底4dの排水管7dに介装した自動バルブ8dが開放される。However, during operation of the pretreatment apparatus, the automatic valves 8a to 8d are designed to be sequentially opened and closed at fixed time intervals in accordance with, for example, the rotation shown in the timing chart of FIG. The automatic valve 8a interposed in the drainage pipe 7a of the V-shaped bottom 4a is opened for a fixed time necessary for discharging the sludge settled and accumulated in the V-shaped bottom 4a. The next automatic valve 8b interposed in the drainage pipe 7b of the letter bottom 4b is opened for a fixed time similar to the automatic valve 8a. Further, at such a timing, the automatic valve 8c interposed in the drainage pipe 7c of the V-shaped bottom 4c is opened during the opening of the automatic valve 8b, and further, the V-shaped bottom is opened during the opening of the automatic valve 8c. The automatic valve 8d provided in the 4d drain pipe 7d is opened.

【0013】 これにより、前処理タンク1の各V字底4a〜4dにはある程度まとまった量 のスラッジが沈降堆積し、そのまとまった量のスラッジが各V字底4a〜4dか ら代わる代わる吸引排出されるので、スラッジ排出管6に介装された遠心分離機 13にはスラッジ濃度の高い処理液が間断なく定常的に送液される。 殊に、各自動バルブ8a〜8dが、先に開放した自動バルブを閉鎖する前に次 の自動バルブを開放する時間差で順次開閉されて、常に二つの自動バルブがオー バーラップして開放されるようになっていれば、遠心分離機13に送液される処 理液の流れに全く途切れが生じないので、その処理中に含まれたスラッジの分離 効率がより一層高まって、熱交換器10の内部に付着するスラッジの量が大幅に 減少する。As a result, a certain amount of sludge is settled and deposited on the V-shaped bottoms 4a to 4d of the pretreatment tank 1, and the collected sludge is sucked from the V-shaped bottoms 4a to 4d instead. Since it is discharged, the treatment liquid having a high sludge concentration is constantly fed to the centrifuge 13 provided in the sludge discharge pipe 6 without interruption. In particular, the automatic valves 8a to 8d are sequentially opened and closed with a time difference of opening the next automatic valve before closing the previously opened automatic valve so that the two automatic valves are always opened in an overlapping manner. If so, the flow of the treatment liquid sent to the centrifuge 13 will not be interrupted at all, and the separation efficiency of the sludge contained in the treatment will be further enhanced, and the heat exchanger 10 The amount of sludge adhering to the inside is greatly reduced.

【0014】 また、自動バルブ8a〜8dが順次開閉すれば、各V字底4a〜4dからスラ ッジ排出管6に吸引排出される処理液の流速も高まるので、各V字底4a〜4d に一旦沈降したスラッジが前処理タンク1内に舞い上がるという不具合も防止で きる。Further, if the automatic valves 8a to 8d are sequentially opened and closed, the flow velocity of the processing liquid sucked and discharged from the respective V-shaped bottoms 4a to 4d to the sludge discharge pipe 6 is increased, so that the respective V-shaped bottoms 4a to 4d are increased. It is also possible to prevent the problem that sludge once settled up rises into the pretreatment tank 1.

【0015】 そして、遠心分離機13を介して熱交換器10に送られる処理液は、前処理タ ンク1の槽底を成す各V字底4a〜4dから排出される最も低温の処理液である から、温水タンク21から温水循環配管19を通じて熱交換器10に送り込まれ る温水との熱交換効率も極めて良好となる。 なお、実施例では、スラッジ排出管6が熱交換器10を介装した処理液循環配 管9の往管11を成しているが、本考案はこれに限るものではない。The treatment liquid sent to the heat exchanger 10 via the centrifugal separator 13 is the lowest temperature treatment liquid discharged from the V-shaped bottoms 4 a to 4 d forming the tank bottom of the pretreatment tank 1. Therefore, the efficiency of heat exchange with the warm water sent from the warm water tank 21 to the heat exchanger 10 through the warm water circulation pipe 19 is also very good. In addition, in the embodiment, the sludge discharge pipe 6 constitutes the forward pipe 11 of the treatment liquid circulation pipe 9 in which the heat exchanger 10 is interposed, but the present invention is not limited to this.

【0016】[0016]

【考案の効果】[Effect of device]

本考案によれば、前処理タンクの槽底を成す複数のV字底からスラッジ排出管 を通じて吸引排出される処理液中に含まれたスラッジを非常に効率良く除去する ことができると同時に、各V字底から吸引排出される処理液の流速が高まるので 各V字底に一旦沈降したスラッジが前処理タンク内で舞い上がることも防止され るという大変優れた効果がある。 According to the present invention, sludge contained in the treatment liquid sucked and discharged through the sludge discharge pipe from the plurality of V-shaped bottoms of the pretreatment tank can be removed very efficiently and at the same time, Since the flow velocity of the treatment liquid sucked and discharged from the V-shaped bottom is increased, the sludge once settled on each V-shaped bottom is prevented from soaring in the pretreatment tank, which is a very excellent effect.

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

【図1】本考案による前処理装置の一例を示すフローシ
ート図。
FIG. 1 is a flow chart showing an example of a pretreatment device according to the present invention.

【図2】本考案に係る自動バルブの開閉動作を示すタイ
ムチャート。
FIG. 2 is a time chart showing an opening / closing operation of an automatic valve according to the present invention.

【符号の説明】[Explanation of symbols]

1・・・・・・・前処理タンク 4a〜4d・・・V字底 6・・・・・・・スラッジ排出管 7a〜7d・・・排水管 8a〜8d・・・自動バルブ 13・・・・・・・遠心分離機 1 ... Pretreatment tank 4a-4d ... V-shaped bottom 6 ... Sludge discharge pipe 7a-7d ... Drainage pipe 8a-8d ... Automatic valve 13 ... ·····centrifuge

Claims (2)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 前処理タンクの槽底を成す複数のV字底
からその底に沈降したスラッジを処理液と共に吸引排出
するスラッジ排出管が設けられた前処理装置において、
前記スラッジ排出管(6)に処理液中のスラッジを除去
する遠心分離機(13)が介装されると共に、前記スラッ
ジ排出管(6)と前記各V字底(4a〜4d)とを連結する
各排水管(7a〜7d)に、一定の時間的間隔で順次開閉す
る自動バルブ(8a〜8d)が介装されていることを特徴と
する前処理装置。
1. A pretreatment apparatus provided with a sludge discharge pipe for sucking and discharging sludge settled from a plurality of V-shaped bottoms forming the bottom of the pretreatment tank to the bottom together with a treatment liquid.
A centrifuge (13) for removing sludge in the treatment liquid is interposed in the sludge discharge pipe (6), and the sludge discharge pipe (6) is connected to each of the V-shaped bottoms (4a to 4d). A pretreatment device characterized in that each drainage pipe (7a to 7d) is provided with an automatic valve (8a to 8d) which is sequentially opened and closed at regular time intervals.
【請求項2】 前記各自動バルブ(8a〜8d)が、先に開
放した自動バルブを閉鎖する前に次の自動バルブを開放
する時間差で順次開閉される請求項1記載の前処理装
置。
2. The pretreatment device according to claim 1, wherein each of the automatic valves (8a to 8d) is sequentially opened and closed with a time difference of opening the next automatic valve before closing the previously opened automatic valve.
JP1992079989U 1992-11-19 1992-11-19 Pretreatment device Expired - Fee Related JP2594510Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1992079989U JP2594510Y2 (en) 1992-11-19 1992-11-19 Pretreatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1992079989U JP2594510Y2 (en) 1992-11-19 1992-11-19 Pretreatment device

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JPH0642960U true JPH0642960U (en) 1994-06-07
JP2594510Y2 JP2594510Y2 (en) 1999-04-26

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013112868A (en) * 2011-11-30 2013-06-10 Fuji Heavy Ind Ltd Electrodeposition coating apparatus

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56158896A (en) * 1980-05-12 1981-12-07 Toyota Motor Corp Surface treating device
JPS5827985A (en) * 1981-08-12 1983-02-18 Nippon Paint Co Ltd Controlling method for dip coating type phosphating

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56158896A (en) * 1980-05-12 1981-12-07 Toyota Motor Corp Surface treating device
JPS5827985A (en) * 1981-08-12 1983-02-18 Nippon Paint Co Ltd Controlling method for dip coating type phosphating

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013112868A (en) * 2011-11-30 2013-06-10 Fuji Heavy Ind Ltd Electrodeposition coating apparatus

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