JP2560590Y2 - Pretreatment device - Google Patents

Pretreatment device

Info

Publication number
JP2560590Y2
JP2560590Y2 JP7526492U JP7526492U JP2560590Y2 JP 2560590 Y2 JP2560590 Y2 JP 2560590Y2 JP 7526492 U JP7526492 U JP 7526492U JP 7526492 U JP7526492 U JP 7526492U JP 2560590 Y2 JP2560590 Y2 JP 2560590Y2
Authority
JP
Japan
Prior art keywords
processing liquid
sludge
heat exchanger
tank
pipe
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
JP7526492U
Other languages
Japanese (ja)
Other versions
JPH0639960U (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
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 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)

Description

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

【0001】[0001]

【産業上の利用分野】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。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pretreatment device for pretreatment of painting and plating.

【0002】[0002]

【従来の技術】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。
2. Description of the Related Art A pre-treatment apparatus for pre-treatment of automobile painting is a degreasing liquid or a coating film in which a large object to be treated such as an automobile body transferred on a hanger of a conveyor is stored in a main tank of a pre-treatment tank. It is immersed in a treatment liquid such as a chemical conversion liquid. A plurality of V-shaped bottoms for accumulating sludge settling on the bottom of the main tank are formed at the bottom of the main tank. At each V-shaped bottom, the sludge collected on the bottom is sucked and discharged out of the tank together with the processing liquid. A sludge discharge pipe is connected (Japanese Utility Model Publication No. 63-761). The processing 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)。
In the pretreatment tank, the processing liquid overflowing from the main tank into the sub-tank is sent to a heat exchanger in order to maintain the processing liquid in the main tank in which the object to be processed is immersed at a predetermined control temperature. A processing liquid circulation pipe for heating and returning the heated processing liquid into the main tank is provided (Japanese Utility Model Publication No. Sho 60-31083).

【0004】[0004]

【考案が解決しようとする課題】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 apparatus constructed as described above, for example, conversion sludge adheres to the inside of a heat exchanger for heating a coating solution, which is a processing solution, so that the heat transfer coefficient is reduced. Therefore, the inside is periodically cleaned with nitric acid. However, if the cleaning frequency is low, it is extremely difficult to completely remove the formed chemical sludge which is stuck in the form of stone. In addition, in order to keep the processing liquid stored in the main tank of the pretreatment tank at a predetermined control temperature, the processing liquid overflowing from the main tank into the sub-tank is sent to a heat exchanger, and the hot water heated by steam is heated. However, the processing liquid overflowing into the sub tank is a relatively high temperature processing liquid existing on the liquid surface of the main tank, and the temperature of the processing liquid sent from the sub tank to the heat exchanger is Since there is no great difference from the temperature of the processing liquid in the main tank heated by the heat exchanger, the heat exchange efficiency of the heat exchanger is never good.

【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。
Therefore, the present invention increases the heat exchange efficiency of a heat exchanger that heats a processing solution in a pretreatment tank to a predetermined control temperature, and forms sludge that reduces the heat transmission coefficient inside the heat exchanger. It is a technical problem to prevent adhesion.

【0006】[0006]

【課題を解決するための手段】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。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention provides an outgoing pipe for sending a processing liquid in a pretreatment tank to a heat exchanger, and a processing liquid heated by the heat exchanger. And a sludge discharge pipe for sucking and discharging sludge settled from the V-shaped bottom forming the tank bottom of the pretreatment tank together with the processing liquid. In the pretreatment apparatus, the sludge discharge pipe forms an outgoing pipe of the processing liquid circulation pipe, and a centrifugal separator that removes sludge contained in the processing liquid discharged from the sludge discharge pipe is interposed in the outgoing pipe. Then, a clean processing liquid from which sludge has been removed by the centrifuge is sent to the heat exchanger.

【0007】[0007]

【作用】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, V which forms the bottom of the pretreatment tank is used.
Since the processing liquid sucked and discharged from the bottom of the letter by the sludge discharge pipe is sent to the heat exchanger and heated, the heat exchange efficiency of the heat exchanger is very good. That is, the temperature of the processing liquid stored in the pretreatment tank is lower as it is closer to the bottom of the tank, and particularly at the V-shaped bottom where the processing liquid tends to stagnate. Heat exchangers that heat up have significantly higher heat exchange efficiency.

【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。
[0008] The outgoing pipe of the processing liquid circulation pipe for sending the processing liquid in the pretreatment tank to the heat exchanger is formed by a sludge discharge pipe for discharging the processing liquid containing a larger amount of sludge than ever before. However, since the sludge discharge pipe is equipped with a centrifuge that removes sludge from the processing solution,
A clean processing liquid having a lower sludge content is sent to the heat exchanger. Therefore, it is possible to reliably prevent sludge from adhering to the inside of the heat exchanger, and it is possible to greatly reduce the frequency of cleaning the heat exchanger.

【0009】[0009]

【実施例】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。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a flow sheet diagram showing an example of a pretreatment device 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 FIG. 1, reference numeral 1 denotes a pre-treatment tank comprising a main tank 2 for immersing an object to be processed in a processing liquid and a sub-tank 3 for storing a processing liquid overflowing from the main tank 2. A plurality of V-shaped bottoms 4 for accumulating sludge settling on the bottom of the tank are formed at the bottom of the tank 2, and a sludge discharge pipe 6 for suctioning and discharging the sludge settled and accumulated on each V-shaped bottom 4 by a pump 5. 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1
1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 for sending the processing liquid in the pretreatment tank 1 to the heat exchanger 8 and a return pipe 10 for returning the processing liquid heated in the heat exchanger 8 to the pretreatment tank 1 again. The outgoing pipe 9 is formed by a sludge discharge pipe 6, and the outgoing pipe 9 has a centrifugal separator for removing sludge contained in the processing liquid discharged from the sludge discharge pipe 6. Machine 1
1, a clean processing liquid from which sludge has been removed by the centrifugal separator 11 is sent to the heat exchanger 8. The sludge separated from the processing liquid by the centrifuge 11 is discharged out of the system from a 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。
The return pipe 10 for returning the processing solution heated through the heat exchanger 8 to the pretreatment tank 1 is connected to the main tank 2.
Is connected to a spray riser pipe 13 that sprays a jet of a processing liquid onto the sludge settled on the outlet-side slope of the main tank 2 and drops the sludge on the tank-side slope of the main tank 2. The spray riser pipe 14 is connected to a circulation pipe 16 for returning the processing liquid overflowing from the main tank 2 into the sub tank 3 to the main tank 2 by the pump 15. Reference numeral 17 denotes a hot water circulation pipe for sending hot water in a hot water tank 19 heated by steam injected from a steam pipe 18 into the heat exchanger 8 by a 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。
The processing liquid sent from the main tank 2 to the heat exchanger 8 through the sludge discharge pipe 6 is the lowest temperature processing liquid discharged from the V-shaped bottom 4 formed at the bottom of the main tank 2. Therefore, the efficiency of heat exchange 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, in the processing liquid sent to the heat exchanger 8 through the sludge discharge pipe 6, since the sludge is effectively removed by the centrifugal separator 11 on the way, the amount of the sludge adhering to the inside of the heat exchanger 8 is large. To decrease.

【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 an experiment, when a processing solution 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 250 P.PM. .PM, but only about 100 P.P.
M. When the processing liquid from which the sludge has been removed by the centrifugal separator 11 is passed through the heat exchanger 8, the amount of the sludge adhering to the inside of the heat exchanger 8 has been reduced to about one third of the conventional one. In addition, the frequency of cleaning the heat exchanger 8 was also greatly reduced.

【0015】[0015]

【考案の効果】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 that heats the processing solution in the pretreatment tank to a predetermined control temperature is improved, and at the same time, the amount of sludge adhering inside the heat exchanger. Is greatly reduced, and the frequency of cleaning the heat exchanger is greatly reduced.

【図面の簡単な説明】[Brief description of the 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 flowchart illustrating an example of a pretreatment apparatus 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 DESCRIPTION OF SYMBOLS 1 ... Pretreatment tank 4 ... V-shaped bottom 6 ... Sludge discharge pipe 7 ... Processing liquid circulation pipe 8 ... Heat exchanger 9 ... Outgoing pipe 10 ... Return pipe 11 ··centrifuge

Claims (1)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【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. An outgoing pipe (9) for sending a processing liquid in a pretreatment tank (1) to a heat exchanger (8), and a processing liquid heated in the heat exchanger (8) is again supplied to the pretreatment tank. A processing liquid circulation pipe (7) comprising a return pipe (10) returning to (1), and sludge settled from the V-shaped bottom (4) forming a tank bottom of the pretreatment tank (1) together with the processing liquid. In the pretreatment device provided with a sludge discharge pipe (6) for suction and discharge, the sludge discharge pipe (6) is connected to the forward pipe (9) of the processing liquid circulation pipe (7).
And a centrifuge (11) for removing sludge contained in the processing liquid discharged from the sludge discharge pipe (6) is interposed in the forward pipe (9), and the centrifuge (11) The pretreatment apparatus is characterized in that the clean processing liquid from which sludge has been removed in (1) 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 JPH0639960U (en) 1994-05-27
JP2560590Y2 true 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)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100229672B1 (en) * 1995-09-28 1999-12-01 에모토 간지 Method and apparatus of discharging setting solid particle

Also Published As

Publication number Publication date
JPH0639960U (en) 1994-05-27

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