JPH0639960U - Pretreatment device - Google Patents

Pretreatment device

Info

Publication number
JPH0639960U
JPH0639960U JP7526492U JP7526492U JPH0639960U JP H0639960 U JPH0639960 U JP H0639960U JP 7526492 U JP7526492 U JP 7526492U JP 7526492 U JP7526492 U JP 7526492U JP H0639960 U JPH0639960 U JP H0639960U
Authority
JP
Japan
Prior art keywords
treatment liquid
sludge
heat exchanger
pipe
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
JP7526492U
Other languages
Japanese (ja)
Other versions
JP2560590Y2 (en
Inventor
野 忠 道 広
司 麟 庄
壁 哲 夫 明
井 禎 治 永
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
Toyota Motor Corp
Original Assignee
Trinity Industrial Corp
Toyota Motor 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, Toyota Motor Corp filed Critical Trinity Industrial Corp
Priority to JP7526492U priority Critical patent/JP2560590Y2/en
Publication of JPH0639960U publication Critical patent/JPH0639960U/en
Application granted granted Critical
Publication of JP2560590Y2 publication Critical patent/JP2560590Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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

Abstract

(57)【要約】 【目的】前処理タンク内の処理液を所定の管理温度に加
温する熱交換器の熱交換効率を高めると共に、その熱交
換器の内部に前処理タンクから循環供給される処理液中
に含まれたスラッジが付着して熱貫流効率が低下するこ
とを防止する。 【構成】前処理タンク1のV字底4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6が、前処
理タンク1内の処理液を熱交換器8に循環供給する処理
液循環配管7の往管9を成し、その往管9に、スラッジ
排出管6から排出された処理液中のスラッジを除去する
遠心分離機11が介装されて、当該遠心分離機11でス
ラッジを除去した清浄な処理液が熱交換器8に送液され
る。
(57) [Summary] [Purpose] The heat exchange efficiency of the heat exchanger that heats the treatment liquid in the pretreatment tank to a predetermined control temperature is improved, and the heat is circulated and supplied from the pretreatment tank to the inside of the heat exchanger. It prevents the sludge contained in the treatment liquid from adhering to lower the heat transmission efficiency. [Structure] A sludge discharge pipe 6 for sucking and discharging sludge settled on a V-shaped bottom 4 of a pretreatment tank 1 together with a treatment liquid, and a treatment liquid circulation pipe for supplying the treatment liquid in the pretreatment tank 1 to a heat exchanger 8 in a circulating manner. 7 is a forward pipe 9 and a centrifugal separator 11 for removing sludge in the treatment liquid discharged from the sludge discharge pipe 6 is interposed in the forward pipe 9 and the sludge is removed by the centrifugal separator 11. The clean processing liquid thus prepared is sent to the heat exchanger 8.

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留した 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ている(実公昭63−761号公 報)。 なお、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。 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 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 (Actual Publication No. Sho 63-761). The treated liquid discharged from the sludge discharge pipe is passed through a filter such as a settling tank to remove sludge and then returned to the main tank again.

【0003】 また、前処理タンクには、被処理物を浸漬するメインタンク内の処理液を所定 の管理温度に保つために、メインタンクからサブタンク内にオーバーフローした 処理液を熱交換器に送って加温すると共に、加温した処理液をメインタンク内に 戻す処理液循環配管が設けられている(実公昭60−31083号公報)。Further, in the pretreatment tank, in order to maintain the treatment liquid in the main tank in which the object to be treated is immersed at a predetermined control temperature, the treatment liquid overflowed from the main tank into the sub tank is sent to a heat exchanger. A processing solution circulation pipe is provided for heating and returning the heated processing solution into the main tank (Japanese Utility Model Publication No. 60-31083).

【0004】[0004]

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

上記の如く構成された従来の前処理装置は、例えば、処理液である被膜化成液 を加温する熱交換器の内部に化成スラッジが付着して熱貫流率が低下するため、 その内部を定期的に硝酸洗浄しているが、その洗浄頻度が少ないと、付着した化 成スラッジが石状に固まってこれを完全に除去することは極めて困難になる。 また、前処理タンクのメインタンク内に貯留された処理液を所定の管理温度に 保つために、そのメインタンクからサブタンク内にオーバーフローした処理液を 熱交換器に送って、蒸気で加熱された温水との熱交換によって加温しているが、 サブタンク内にオーバーフローする処理液は、メインタンクの液面に存する比較 的高温の処理液であり、サブタンクから熱交換器に送られる処理液の温度はその 熱交換器で加温されたメインタンク内の処理液の温度と大差がないので、熱交換 器の熱交換効率は決して良くない。 In the conventional pretreatment device configured as described above, for example, since the chemical conversion sludge adheres to the inside of the heat exchanger that heats the film forming liquid, which is the processing liquid, and the heat transmission coefficient decreases, the inside of the device is regularly However, if the cleaning frequency is low, it will be extremely difficult to completely remove the deposited chemical sludge as a stone. In addition, in order to keep the treatment liquid stored in the main tank of the pretreatment tank at a predetermined control temperature, the treatment liquid overflowing from the main tank into the sub tank is sent to a heat exchanger, where hot water heated by steam is used. Although it is heated by heat exchange with the sub-tank, the treatment liquid overflowing into the sub-tank is a comparatively high-temperature treatment liquid existing on the liquid surface of the main tank, and the temperature of the treatment liquid sent from the sub-tank to the heat exchanger is The heat exchange efficiency of the heat exchanger is never good because there is no big difference with the temperature of the treatment liquid in the main tank heated by the heat exchanger.

【0005】 そこで本考案は、前処理タンク内の処理液を所定の管理温度に加温する熱交換 器の熱交換効率を高めると共に、その熱交換器の内部に熱貫流率を低下させるス ラッジが付着しないようにすることを技術的課題としている。In view of this, the present invention improves the heat exchange efficiency of a heat exchanger that heats the treatment liquid in the pretreatment tank to a predetermined management temperature, and reduces the heat transmission coefficient inside the heat exchanger. It is a technical issue to prevent them from adhering.

【0006】[0006]

【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、前処理タンク内の処理液を熱交換器 に送る往管と、その熱交換器で加温された処理液を再び前処理タンクに戻す返管 とで成る処理液循環配管と、前処理タンクの槽底を成す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が前記処理液循環配管の往管を成すと共に、そ の往管に、前記スラッジ排出管から排出された処理液に含まれるスラッジを除去 する遠心分離機が介装されて、当該遠心分離機でスラッジを除去した清浄な処理 液が前記熱交換器に送液されるように成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 forward pipe for sending a treatment liquid in a pretreatment tank to a heat exchanger, and a return pipe for returning the treatment liquid heated by the heat exchanger to the pretreatment tank again. In the pretreatment equipment equipped with a treatment liquid circulation pipe consisting of and a sludge discharge pipe for sucking and discharging the sludge settled from the V-shaped bottom forming the bottom of the pretreatment tank to the bottom together with the treatment liquid, The pipe serves as a forward pipe of the treatment liquid circulation pipe, and a centrifugal separator for removing sludge contained in the treatment liquid discharged from the sludge discharge pipe is provided in the forward pipe, and the centrifugal separator concerned It is characterized in that a clean treatment liquid from which sludge has been removed by is sent to the heat exchanger.

【0007】[0007]

【作用】[Action]

本考案によれば、前処理タンクの槽底を成すV字底からスラッジ排出管で吸引 排出された処理液を熱交換器に送って加温するので、その熱交換器の熱交換効率 が非常に良い。 すなわち、前処理タンク内に貯留した処理液の温度は、槽底に近いほど低く、 特に、処理液が停滞しやすいV字底において最も低くなるので、そのV字底から 排出された処理液を加温する熱交換器は熱交換効率が著しく高まる。 According to the present invention, the treatment liquid sucked and discharged from the V-shaped bottom of the pretreatment tank through the sludge discharge pipe is sent to the heat exchanger for heating, so that the heat exchange efficiency of the heat exchanger is extremely high. Good for That is, the temperature of the treatment liquid stored in the pretreatment tank becomes lower as it gets closer to the bottom of the tank, especially at the V-shaped bottom where the treatment liquid tends to stagnant, so that the treatment liquid discharged from the V-shaped bottom is removed. The heat exchange efficiency of the heat exchanger for heating is significantly increased.

【0008】 また、前処理タンク内の処理液を熱交換器に送る処理液循環配管の往管は、従 来にも増して多量のスラッジを含んだ処理液を排出するスラッジ排出管で形成さ れているが、そのスラッジ排出管には処理液中からスラッジを除去する遠心分離 機が介装されているため、熱交換器には従来よりもスラッジ含有量の少ない清浄 な処理液が送られる。 したがって、熱交換器の内部にスラッジが付着することを確実に防止でき、熱 交換器の洗浄頻度も大幅に低減することができる。Further, the forward pipe of the treatment liquid circulation pipe for feeding the treatment liquid in the pretreatment tank to the heat exchanger is formed by a sludge discharge pipe for discharging the treatment liquid containing a large amount of sludge as compared with the conventional case. However, since the sludge discharge pipe is equipped with a centrifugal separator that removes sludge from the treatment liquid, a clean treatment liquid with a smaller sludge content than before is sent to the heat exchanger. . Therefore, it is possible to reliably prevent the sludge from adhering to the inside of the heat exchanger, and to significantly reduce the frequency of cleaning the heat exchanger.

【0009】[0009]

【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 apparatus according to the present invention.

【0010】 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留するサブタンク3とから成る前処理 槽であって、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4が形成されると共に、各V字底4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が接続されている。In the figure, reference numeral 1 denotes a pretreatment tank comprising 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 4 for accumulating sludge that settles on the tank bottom are formed on the bottom of No. 2, and a sludge discharge pipe for sucking and discharging the sludge settled and accumulated on each V-shaped bottom 4 with a pump 5. 6 is connected.

【0011】 7は、前処理タンク1内の処理液を熱交換器8に送る往管9と、熱交換器8で 加温された処理液を再び前処理タンク1に戻す返管10とで成る処理液循環配管 であって、往管9がスラッジ排出管6で形成されると共に、その往管9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 11が介装されて、当該遠心分離機11でスラッジを除去した清浄な処理液が熱 交換器8に送液されるようになっている。 なお、遠心分離機11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11に設けたドレン管12から系外に排出される。Reference numeral 7 denotes a forward pipe 9 that sends the treatment liquid in the pretreatment tank 1 to the heat exchanger 8, and a return pipe 10 that returns the treatment liquid heated in the heat exchanger 8 to the pretreatment tank 1 again. The forward pipe 9 is formed by the sludge discharge pipe 6, and the forward pipe 9 is a centrifugal device for removing sludge contained in the process liquid discharged from the sludge discharge pipe 6. A separator 11 is interposed so that the clean treatment liquid from which sludge has been removed by the centrifuge 11 is sent to the heat exchanger 8. The sludge separated from the treatment liquid by the centrifuge 11 is discharged out of the system through the drain pipe 12 provided in the centrifuge 11.

【0012】 また、熱交換器8に通して加温された処理液を前処理タンク1に戻す返管10 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4に落とし込むスプレーライザー管13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4に落とし込むスプレーライザー管14 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 15でメインタンク2に戻す循環配管16が接続されている。 17は、スチーム管18から液中噴射される蒸気で加温した温水タンク19内 の温水をポンプ20によって熱交換器8に送り込む温水循環配管である。Further, the return pipe 10 for returning the treatment liquid heated through the heat exchanger 8 to the pretreatment tank 1 blows a jet of the treatment liquid onto the sludge settling on the outlet side slope of the main tank 2. The spray riser pipe 14 that is connected to the spray riser pipe 13 that drops into the V-shaped bottom 4 and that drops the sludge that has settled on the inlet side slope of the main tank 2 into the V-shaped bottom 4 overflows from the main tank 2 into the sub-tank 3. A circulation pipe 16 for returning the treatment liquid to the main tank 2 with a pump 15 is connected. Reference numeral 17 denotes a hot water circulation pipe for sending hot water in the hot water tank 19 heated by the steam injected from the steam pipe 18 into the heat exchanger 8 by the pump 20.

【0013】 しかして、メインタンク2内からスラッジ排出管6を通じて熱交換器8に送ら れる処理液は、メインタンク2の槽底に形成したV字底4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19から温水循環配管17を通じて熱交換器 8に送り込まれる温水との熱交換効率が極めて良好となる。 また、スラッジ排出管6を通じて熱交換器8に送られる処理液は、その途中で 遠心分離機11によってスラッジが効果的に除去されるので、熱交換器8の内部 に付着するスラッジの量が大幅に減少する。Therefore, the treatment liquid sent from the inside of the main tank 2 to the heat exchanger 8 through the sludge discharge pipe 6 is the lowest temperature treatment liquid discharged from the V-shaped bottom 4 formed at the bottom of the main tank 2. Therefore, the heat exchange efficiency with the hot water sent from the hot water tank 19 to the heat exchanger 8 through the hot water circulation pipe 17 becomes extremely good. Further, since the sludge is effectively removed by the centrifuge 11 in the process liquid sent to the heat exchanger 8 through the sludge discharge pipe 6, the amount of sludge adhering to the inside of the heat exchanger 8 is greatly increased. Decrease to.

【0014】 実験によれば、V字底4から排出されるスラッジ含量450P.P.M の処理液を 従来から用いられているセットリングタンク等の濾過器に通したときは、そのス ラッジ含量が約250P.P.M までしか低下しないのに対し、遠心分離機11に通 したときは、約100P.P.M まで低下した。 そして、遠心分離機11でスラッジが除去された処理液を熱交換器8に通した 場合には、その熱交換器8の内部に付着するスラッジの量が従来の3分の1程度 まで減少したため、熱交換器8の洗浄頻度も大幅に低減された。According to the experiment, when the treatment liquid having a sludge content of 450 P.PM discharged from the V-shaped bottom 4 is passed through a filter such as a settling tank which has been conventionally used, the sludge content is about When it passed through the centrifuge 11, it decreased to about 100 P.PM while it decreased to only 250 P.PM. When the treatment liquid from which sludge was removed by the centrifuge 11 was passed through the heat exchanger 8, the amount of sludge adhering to the inside of the heat exchanger 8 was reduced to about one-third that of the conventional method. The cleaning frequency of the heat exchanger 8 was also greatly reduced.

【0015】[0015]

【考案の効果】[Effect of device]

本考案によれば、前処理タンク内の処理液を所定の管理温度に加温する熱交換 器の熱交換効率が良くなると同時に、熱交換器の内部に付着するスラッジの量が 大幅に減少して熱交換器の洗浄頻度が大幅に少なくなるという大変優れた効果が ある。 According to the present invention, the heat exchange efficiency of the heat exchanger for heating the treatment liquid in the pretreatment tank to a predetermined control temperature is improved, and at the same time, the amount of sludge adhering to the inside of the heat exchanger is significantly reduced. This has the excellent effect of significantly reducing the frequency of cleaning the heat exchanger.

【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.

【符号の説明】[Explanation of symbols]

1・・・前処理タンク 4・・・V字底 6・・・スラッジ排出管 7・・・処理液循環配管 8・・・熱交換器 9・・・往管 10・・・返管 11・・・遠心分離機 1 ... Pretreatment tank 4 ... V-shaped bottom 6 ... Sludge discharge pipe 7 ... Treatment liquid circulation pipe 8 ... Heat exchanger 9 ... Forward pipe 10 ... Return pipe 11 ... ··centrifuge

───────────────────────────────────────────────────── フロントページの続き (72)考案者 明 壁 哲 夫 愛知県豊田市柿本町一丁目9番地 トリニ ティ工業株式会社内 (72)考案者 永 井 禎 治 愛知県豊田市トヨタ町1番地 トヨタ自動 車株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Tetsuo Meikaka 1-9 Kakimoto-cho, Toyota City, Aichi Prefecture Trinity Industry Co., Ltd. (72) Sadaharu Nagai, 1 Toyota-cho, Toyota City, Aichi Prefecture Toyota Automobile Co., Ltd.

Claims (1)

【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(1)内の処理液を熱交換
器(8)に送る往管(9)と、その熱交換器(8)で加
温された処理液を再び前処理タンク(1)に戻す返管
(10)とで成る処理液循環配管(7)と、前処理タンク
(1)の槽底を成すV字底(4)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
(6)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)が前記処理液循環配管(7)の往管(9)
を成すと共に、その往管(9)に、前記スラッジ排出管
(6)から排出された処理液に含まれるスラッジを除去
する遠心分離機(11)が介装されて、当該遠心分離機
(11)でスラッジを除去した清浄な処理液が前記熱交換
器(8)に送液されるように成されていることを特徴と
する前処理装置。
1. A forward pipe (9) for sending the treatment liquid in the pretreatment tank (1) to a heat exchanger (8), and the treatment liquid heated by the heat exchanger (8) is again treated as a pretreatment tank. The treatment liquid circulation pipe (7) consisting of the return pipe (10) returning to (1) and the sludge settled from the V-shaped bottom (4) forming the bottom of the pretreatment tank (1) to the bottom together with the treatment liquid. In the pretreatment device provided with a sludge discharge pipe (6) for sucking and discharging, the sludge discharge pipe (6) is a forward pipe (9) of the treatment liquid circulation pipe (7).
And a centrifugal separator (11) for removing sludge contained in the treatment liquid discharged from the sludge discharge pipe (6) is interposed in the forward pipe (9), and the centrifugal separator (11) ), A clean treatment liquid from which sludge has been removed is sent to the heat exchanger (8).
JP7526492U 1992-10-29 1992-10-29 Pretreatment device Expired - Fee Related JP2560590Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7526492U JP2560590Y2 (en) 1992-10-29 1992-10-29 Pretreatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7526492U JP2560590Y2 (en) 1992-10-29 1992-10-29 Pretreatment device

Publications (2)

Publication Number Publication Date
JPH0639960U true JPH0639960U (en) 1994-05-27
JP2560590Y2 JP2560590Y2 (en) 1998-01-26

Family

ID=13571196

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7526492U Expired - Fee Related JP2560590Y2 (en) 1992-10-29 1992-10-29 Pretreatment device

Country Status (1)

Country Link
JP (1) JP2560590Y2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997012077A1 (en) * 1995-09-28 1997-04-03 Kawasaki Steel Corporation Method of discharging settling solid particles and apparatus therefor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997012077A1 (en) * 1995-09-28 1997-04-03 Kawasaki Steel Corporation Method of discharging settling solid particles and apparatus therefor

Also Published As

Publication number Publication date
JP2560590Y2 (en) 1998-01-26

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