JP3379019B2 - Work cleaning device - Google Patents

Work cleaning device

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Publication number
JP3379019B2
JP3379019B2 JP30313592A JP30313592A JP3379019B2 JP 3379019 B2 JP3379019 B2 JP 3379019B2 JP 30313592 A JP30313592 A JP 30313592A JP 30313592 A JP30313592 A JP 30313592A JP 3379019 B2 JP3379019 B2 JP 3379019B2
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JP
Japan
Prior art keywords
solvent
tank
specific gravity
cleaning
gravity separation
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
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JP30313592A
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Japanese (ja)
Other versions
JPH06126257A (en
Inventor
康嗣 梶原
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.)
SHIN-OHTSUKA CO., LTD.
Original Assignee
SHIN-OHTSUKA CO., LTD.
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Application filed by SHIN-OHTSUKA CO., LTD. filed Critical SHIN-OHTSUKA CO., LTD.
Priority to JP30313592A priority Critical patent/JP3379019B2/en
Publication of JPH06126257A publication Critical patent/JPH06126257A/en
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Publication of JP3379019B2 publication Critical patent/JP3379019B2/en
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Description

【発明の詳細な説明】 【0001】 【産業上の利用分野】この発明は、例えば、電気部品、
電子部品、プレス部品等のワークを洗浄処理するために
用いられるワーク洗浄装置に関する。 【0002】 【従来の技術】従来、上述例のようなワークの洗浄方法
としては、例えば、洗浄槽に貯液された塩素系溶剤中に
ワーク全体を浸漬し、同洗浄槽に取付けた超音波振動子
を振動させて、塩素系溶剤のキャビテーション作用によ
りワークに付着した切粉や油分等の異物を除去する洗浄
方法がある。 【0003】 【発明が解決しようとする課題】しかし、上述のように
ワークを塩素系溶剤のみで洗浄処理する場合、塩素系溶
剤は人体及び環境に有害であるだけでなく、樹脂材料を
溶解しやすいため、プリント基板等の樹脂製品を洗浄処
理するのに不向きな溶剤である。且つ、熱容量の小さな
ワークを塩素系溶剤で洗浄処理した場合、ワーク乾燥時
に結露が発生し、結露部分に塵埃やゴミ等の付着した跡
が残るため、溶剤による洗浄効果が損なわてしまうと
いう問題点を有している。 【0004】この発明は上記問題に鑑み、未洗浄のワー
クを石油系溶剤で洗浄してからFC系溶剤中に浸漬して
洗浄処理することにより、高度な技術を必要とする残渣
の無い洗浄処理が簡単に行え、ワーク全体を確実且つ綺
麗に洗浄処理できるワーク洗浄装置の提供を目的とす
る。 【0005】 【課題を解決するための手段】この発明のワーク洗浄装
置は、未洗浄のワークを、該ワークに付着する異物を分
離除去するのに適した温度に加温された石油系溶剤中に
浸漬して洗浄処理する第1洗浄槽の後段位置に、該ワー
クを上記石油系溶剤よりも溶剤自体の比重が重く温度の
低いFC系溶剤中に浸漬して洗浄処理する第2洗浄槽を
配設し、上記第2洗浄槽の下流側に、上記第2洗浄槽か
ら石油系溶剤とFC系溶剤とが乳化した溶剤のオーバー
フローを許容するとともに、オーバーフローした該溶剤
を貯液し比重分離する第1比重分離槽を配設し、上記第
1比重分離槽に、上記第1比重分離槽によって分離され
て液面部分に浮上した比重の軽い石油系溶剤のみを槽外
に排出する排油路を形成し、上記第1比重分離槽の下
流側に、上記第1比重分離槽からFC系溶剤のオーバー
フローを許容するとともに、上記第1比重分離槽によっ
て分離された比重の重いFC系溶剤を貯液する第2比重
分離槽を配設し、上記第2比重分離槽の下流側に、上記
第2比重分離槽からのFC系溶剤のオーバーフローを許
容するとともに、上記第2洗浄槽の上方に設定した洗浄
済みワークを乾燥処理する蒸気乾燥領域にFC系溶剤の
蒸気を放出する溶剤蒸留槽を配設し、上記第2洗浄槽
に、上記第2比重分離槽に貯液したFC系溶剤を上記第
2洗浄槽の液面部分に循環供給して吐出し、該液面部分
に浮上した石油系溶剤を積極的にオーバーフローさせる
液面洗浄ノズルを配設したワーク洗浄装置であることを
特徴とする。 【0006】 【作用】本願発明のワーク洗浄装置は、ワーク全体を、
ワークに付着する異物を分離除去するのに適した温度に
加温された第1洗浄槽の石油系溶剤に浸漬して、ワーク
に付着した切粉や油分等の異物を洗浄除去した後、石油
系溶剤よりも温度の低い第2洗浄槽のFC系溶剤に浸漬
して、ワークに付着した異物が含まれる石油系溶剤を、
FC系溶剤との間に生じる温度差と比重差との相乗作用
により剥離除去する。また、比重の軽い石油系溶剤と比
重の重いFC系溶剤とが乳化した溶剤を第1比重分離槽
で貯液し比重分離して、FC系溶剤の液面部分に比重の
軽い石油系溶剤を自然浮上させる。第1比重分離槽の
面部分に浮上した比重の軽い石油系溶剤のみを排油路に
より槽外部に排出する。 第2比重分離槽により、第1比
重分離槽で分離された比重の重いFC系溶剤をオーバー
フローさせ貯液する。 第2洗浄槽の上方に設定した蒸気
乾燥領域に、溶剤蒸留槽により第2比重分離槽からオー
バーフローした比重の重いFC系溶剤を加熱してFC系
溶剤の蒸気を放出する。 さらに、上記第2洗浄槽に、上
記第2比重分離槽に貯液したFC系溶剤を上記 第2洗浄
槽の液面部分に循環供給して吐出し、該液面部分に浮上
した石油系溶剤を積極的にオーバーフローさせる液面洗
浄ノズルを配設し、第2洗浄槽の液面全体にFC系溶剤
が常時露出している状態を保つ。 【0007】 【発明の効果】この発明によれば、未洗浄のワークに付
着する異物を、所定温度に加温された温度の高い石油系
溶剤により洗浄除去した後、そのワークを石油系溶剤よ
りも温度の低いFC系溶剤に浸漬して、ワークに付着す
る異物が含まれる石油系溶剤を、FC系溶剤との間に生
じる温度差と比重差との相乗作用により剥離除去するの
で、石油系溶剤を剥離するのに必要な大きな分離力が得
られ、従来方法では除去することが困難であった石油系
溶剤の残渣をも確実に洗浄除去することができ、高度な
技術を必要とする残渣の無い洗浄処理が簡単に行える。
しかも、ワークに残着した石油系溶剤を剥離除去して、
FC系溶剤のみでワーク全体を仕上げ洗浄するため、ワ
ーク全体を確実且つ綺麗に洗浄処理でき、電子部品や電
気部品等の精密部品を洗浄処理するのに最適である。
た、石油系溶剤とFC系溶剤とが乳化した溶剤を比重分
離して、FC系溶剤の液面部分に比重の軽い石油系溶剤
を自然浮上させて分離することにより、FC系溶剤の循
環供給を可能とし、再利用率の向上を図ることができ
る。 さらに、第1比重分離槽の液面部分に浮上した比重
の軽い石油系溶剤のみを排油路により槽外部に排出する
ことで、FC系溶剤の循環供給を容易にし、また、複雑
な排油手段を設けることなく、確実に石油系溶剤のみを
槽外部に排出することができる。 第2比重分離槽によ
り、第1比重分離槽で分離された比重の重いFC系溶剤
をオーバーフローさせ貯液することにより、循環供給す
るFC系溶剤の純度を高く保持することができる。 また
加えて、第2洗浄槽の上方に設定した蒸気乾燥領域に、
溶剤蒸留槽により第2比重分離槽からオーバーフローし
た比重の重いFC系溶剤を加熱してFC系溶剤の蒸気を
放出することで、第2洗浄槽から取り出されたワークを
適宜温度に加熱して乾燥処理することができる。 且つ、
第2洗浄槽の液面部分に浮上した石油系溶剤を、液面洗
浄ノズルから吐出されるFC系溶剤により第1比重分離
槽側に向けて積極的にオーバーフローさせるので、第2
洗浄槽の液面部分に石油系溶剤が停滞せず、プリント基
板Wを第2洗浄槽から取り出すとき石油系溶剤が再び付
着するのを防止することができる。 【0008】 【実施例】この発明の一実施例を以下図面に基づいて詳
述する。図面はワークの一例としてスルーホール付きプ
リント基板を洗浄処理するために用いられるワーク洗浄
装置を示し、図1に於いて、このワーク洗浄装置1は、
気密状態に密閉される洗浄室2の内部空間に、所定量貯
液された石油系溶剤L(商品名=ナフテゾール)にプリ
ント基板W全体を浸漬して切粉や油分等の異物を洗浄除
去する第1洗浄槽3と、所定量貯液されたFC系溶剤F
(商品名=フロリナートFC−72)にプリント基板W
全体を浸漬して残留溶剤を洗浄除去する第2洗浄槽4
と、洗浄処理に使用された石油系溶剤LとFC系溶剤F
とを比重分離する比重分離槽5と、分離回収されたFC
系溶剤Fを蒸溜する溶剤蒸溜槽6とを配設している。 【0009】上述の第1洗浄槽3には、プリント基板W
全体が浸漬される貯液レベルに石油系溶剤L(商品名=
ナフテゾール)を所定量貯液し、同槽底部の内壁面に石
油系溶剤Lを超音波振動するための超音波振動子7を配
設し、例えば、27KHz 〜200KHz の振動周波数で超
音波振動子7を振動させて石油系溶剤Lに超音波振動を
誘起する。且つ、同槽底部の内壁面に石油系溶剤Lを加
熱するための加熱ヒータ8を配設し、例えば、適宜温度
に加熱された油や水等の媒体を加熱ヒータ8に循環供給
して石油系溶剤Lを、プリント基板Wに付着する切粉や
油分等の異物を分離除去するのに適した適宜温度(例え
ば、約60℃)に加熱する。 【0010】且つ、第1洗浄槽3の下部貯液領域にバル
ブ9と、循環ポンプ10と、フィルター11と、熱交換
器12とを介して液循環路13の一端側を接続すると共
に、同液循環路13の他端側をバルブ14を介して第1
洗浄槽3の上部貯液領域に接続している。すなわち、循
環ポンプ10を駆動して、第1洗浄槽3に貯液された石
油系溶剤Lをフィルター11及び熱交換器12を介して
循環供給する。 【0011】前述の各槽4,5,6は、同室内部に形成
した仕上げ室15の底面部に各槽4,5,6を順次配設
し、第2洗浄槽4と対応する直上位置にプリント基板W
が出入許容される大きさのワーク出入口16を形成し、
同第2洗浄槽4の上方蒸気領域と対応するワーク出入口
16の下部側壁面に沿って冷却ジャケット17を配設
し、同ワーク出入口16の下部側壁面に連設した水分離
槽19の上方蒸気領域に冷却コイル18を配設し、例え
ば、適宜温度に冷却された冷媒を冷却ジャケット17及
び冷却コイル18に循環供給して、第2洗浄槽4の上方
蒸気領域に放出されたFC系溶剤Fの蒸気Fa及び室内
に侵入する大気中の水分が凝縮液化する温度に冷却ジャ
ケット17及び冷却コイル18を保温する。 【0012】前述の第2洗浄槽4には、プリント基板W
全体が浸漬される貯液レベルに上述の石油系溶剤Lより
も溶剤自体の比重が重く、低い温度に保たれたFC系溶
剤F(商品名=フロリナートFC−72)を所定量貯液
し、同槽底部の内壁面にFC系溶剤Fを超音波振動する
ための超音波振動子20を配設し、例えば、27KHz〜
200KHz の振動周波数で超音波振動子20を振動させ
てFC系溶剤Fに超音波振動を誘起する。且つ、第2洗
浄槽4の液面部分に浮上する石油系溶剤Lに対して水平
となる高さ位置の上流側壁面に液面洗浄ノズル21を配
設すると共に、同液面洗浄ノズル21の吐出方向を下流
側に配設した比重分離槽5側に向けて位置固定してい
る。 【0013】且つ、上流側に配設した第2洗浄槽4と下
流側に配設した比重分離槽5との上端壁部間に、上流側
の第2洗浄槽4から下流側の比重分離槽5に向けて乳化
した各溶剤L,Fをオーバーフローするための流下板2
2を斜設している。 【0014】前述の比重分離槽5には、同槽内部の貯液
領域を第1分離槽5aと第2分離槽5bとに左右分割す
る位置に仕切り板5cを立設し、第2分離槽5bの貯液
領域を左右分割する位置に仕切り板5dを立設してい
る。 【0015】且つ、第1分離槽5aの液面部分に浮上す
る石油系溶剤Lの油分浮上領域にバルブ23を介して排
油路24を接続し、第2分離槽5bの下部貯液領域にバ
ルブ25と、循環ポンプ26と、フィルター27と、熱
交換器28とを介して液循環路29の一端側を接続する
と共に、同液循環路29の他端側を各バルブ30,31
を介して第2洗浄槽4の上部貯液領域と液面洗浄ノズル
21とに夫々接続している。すなわち、循環ポンプ26
を駆動して、比重分離槽5の第2分離槽5bに貯液され
たFC系溶剤Fをフィルター27及び熱交換器28を介
して第2洗浄槽4の上部貯液領域と液面洗浄ノズル21
とに循環供給する。 【0016】前述の溶剤蒸溜槽6には、同槽底部の内壁
面にFC系溶剤Fを加熱するための加熱ヒータ32を配
設し、例えば、適宜温度に加熱された油や水等の媒体を
加熱ヒータ32に循環供給してFC系溶剤Fが蒸発気化
する沸点温度(例えば、約56℃)に加熱する。且つ、
上流側に配設した比重分離槽5と下流側に配設した溶剤
蒸溜槽6との上端壁部間に、上流側の比重分離槽5から
下流側の溶剤蒸溜槽6に向けて比重分離されたFC系溶
剤Fをオーバーフローするための流下板33を斜設して
いる。 【0017】図示実施例は上記の如く構成するものとし
て、以下、ワーク洗浄装置1によるプリント基板Wの洗
浄方法を説明する。先ず、図1に示すように、第1洗浄
槽3に配設した加熱ヒータ8を加熱して、同槽内部に貯
液された石油系溶剤Lを、プリント基板Wに付着する異
物を分離除去するのに適した適宜温度(例えば、約60
℃)に加熱する。この後、未洗浄のプリント基板Wを洗
浄室2内に搬入して、第1洗浄槽3に貯液された石油系
溶剤L中にプリント基板W全体を浸漬後、同槽底部に配
設した超音波振動子7を振動させて、石油系溶剤Lのキ
ャビテーション作用によりプリント基板Wを洗浄除去す
るので、プリント基板Wに付着した切粉や油分等の異物
を石油系溶剤Lの洗浄力により確実に洗浄除去すること
ができる。同時に、循環ポンプ10を駆動して、第1洗
浄槽3に貯液された石油系溶剤Lをフィルター11及び
熱交換器12を介して循環供給する。 【0018】次に、溶剤蒸溜槽6に配設した加熱ヒータ
32を加熱して、同槽内部に貯液されたFC系溶剤Fを
適宜温度(例えば、約56℃)に加熱すると共に、蒸発
気化したFC系溶剤Fの蒸気Faを仕上げ室15全体に
放出する。この後、一次洗浄されたプリント基板Wを仕
上げ室15内に搬入して、第2洗浄槽4の上方蒸気領域
に放出されたFC系溶剤Fの蒸気Fa中を通過させ、同
槽内部に貯液された石油系溶剤Lよりも溶剤自体の比重
が重く、温度の低いFC系溶剤F中に上方から浸漬後、
同槽底部に配設した超音波振動子20を振動させて、F
C系溶剤Fのキャビテーション作用によりプリント基板
Wに付着した異物が含まれる石油系溶剤Lを剥離除去す
る。 【0019】すなわち、FC系溶剤Fはフロン等に比べ
て表面張力が小さく、浸透性に優れているため、プリン
ト基板Wの表面部分に付着した石油系溶剤Lを確実に剥
離除去することができる。同時に、プリント基板Wから
剥離除去した温度の高い石油系溶剤LをFC系溶剤F中
に乳化させて、第2洗浄槽4の液面部分に温度が高く比
重の軽い石油系溶剤Lを自然浮上させる。 【0020】且つ、循環ポンプ26を駆動して、比重分
離槽5の第2分離槽5bに貯液されたFC系溶剤Fをフ
ィルター27及び熱交換器28を介して第2洗浄槽4の
液面洗浄ノズル21に循環供給し、同液面洗浄ノズル2
1から吐出するFC系溶剤Fで第2洗浄槽4の液面部分
に浮上した異物が含まれる石油系溶剤Lを比重分離槽5
の第1分離槽5a側に向けて積極的にオーバーフローさ
せ、第2洗浄槽4の液面全体にFC系溶剤Fが常時露出
している状態を保つ。 【0021】次に、比重の異なる各溶剤L,Fを乳化し
た状態のまま比重分離槽5の第1分離槽5a側にオーバ
ーフローして、比重の重いFC系溶剤Fと、比重の軽い
石油系溶剤Lとに比重分離する。すなわち、比重分離槽
5の第1分離槽5aに貯液されたFC系溶剤Fの液面部
分に比重の軽い石油系溶剤Lを自然浮上させ、第1分離
槽5aの液面部分に浮上した比重の軽い石油系溶剤Lの
みを排油路24から槽外部に排出する。一方、第1分離
槽5aの下部貯液領域に貯液された比重の重いFC系溶
剤Fを第2分離槽5b側にオーバーフローさせ、同第2
分離槽5bに貯液されたFC系溶剤Fを溶剤蒸溜槽6側
にオーバーフローさせる。 【0022】同時に、溶剤蒸溜槽6に貯液されたFC系
溶剤Fを加熱ヒータ32で加熱して、仕上げ室15全体
にFC系溶剤Fの蒸気Faを放出すると共に、第2洗浄
槽4の上方蒸気領域に配設した冷却ジャケット17でF
C系溶剤Fの蒸気Faを凝縮液化するので、蒸溜された
FC系溶剤Fが第2洗浄槽4に滴下供給される。 【0023】次に、洗浄終了後、第2洗浄槽4に貯液さ
れたFC系溶剤F中からプリント基板W全体を上方に取
り出し、同槽の上方蒸気領域に放出されたFC系溶剤F
の蒸気Faでプリント基板W全体を適宜温度に加熱して
乾燥処理する。この後、洗浄済みのプリント基板Wを仕
上げ室15から搬出し、同プリント基板Wを洗浄室2か
ら搬出することで、一つのプリント基板Wの洗浄処理が
完了する。 【0024】以上のように、未洗浄のプリント基板Wに
付着する異物を所定温度に加温された温度の高い石油系
溶剤Lで洗浄除去した後、そのプリント基板Wを石油系
溶剤Lよりも溶剤自体の比重が重く温度の低いFC系溶
剤Fに浸漬して、プリント基板Wに付着する異物が含ま
れる石油系溶剤Lを、FC系溶剤Fとの間に生じる温度
差と比重差との相乗作用により剥離除去するので、石油
系溶剤Lを剥離するのに必要な大きな分離力が得られ、
従来方法では除去することが困難であった石油系溶剤L
の残渣をも確実に洗浄除去することができ、高度な技術
を必要とする残渣の無い洗浄処理が簡単に行える。しか
も、プリント基板Wに残着した石油系溶剤Lを剥離除去
して、FC系溶剤Fのみでプリント基板Wを仕上げ洗浄
するため、プリント基板W全体を確実且つ綺麗に洗浄処
理でき、電子部品や電気部品等の精密部品を洗浄処理す
るのに最適である。また、石油系溶剤とFC系溶剤とが
乳化した溶剤を比重分離して、FC系溶剤の液面部分に
比重の軽い石油系溶剤を自然浮上させて分離することに
より、FC系溶剤の循環供給を可能とし、再利用率の向
上を図ることができる。 さらに、第1比重分離槽の液面
部分に浮上した比重の軽い石油系溶剤のみを排油路によ
り槽外部に排出することで、FC系溶剤の循環供給を容
易にし、また、複雑な排油手段を設けることなく、確実
に石油系溶剤のみを槽外部に排出することができる。
2比重分離槽により、第1比重分離槽で分離された比重
の重いFC系溶剤をオーバーフローさせ貯液することに
より、循環供給するFC系溶剤の純度を高く保持するこ
とができる。 また加えて、第2洗浄槽の上方に設定した
蒸気乾燥領域に、溶剤蒸留槽により第2比重分離槽から
オーバーフローした比重の重いFC系溶剤を加熱してF
C系溶剤の蒸気を放出することで、第2洗浄槽から取り
出されたワークを適宜温度に加熱して乾燥処理すること
ができる。且つ、第2洗浄槽4の液面部分に浮上した石
油系溶剤Lを、噴射ノズル21から吐出されるFC系溶
剤Fにより比重分離槽5側に向けて積極的にオーバーフ
ローさせるので、第2洗浄槽4の液面部分に石油系溶剤
Lが停滞せず、プリント基板Wを第2洗浄槽4から取り
出すとき石油系溶剤Lが再び付着するのを防止すること
ができる。 【0025】この発明の構成と、上述の実施例との対応
において、この発明のワークは、実施例のプリント基板
Wに対応するも、この発明は、上述の実施例の構成のみ
に限定されるものではない。 【0026】上述の実施例では、FC系溶剤F(商品名
=フロリナートFC−72)でプリント基板Wを洗浄処
理するが、例えば、FC−40、FC−43、FC−7
0、FC−75、FC−77、FC−104等のFC系
溶剤Fを用途に応じて選択使用するもよい。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention
The present invention relates to a work cleaning apparatus used for cleaning a work such as an electronic component and a pressed component. 2. Description of the Related Art Conventionally, as a method of cleaning a work as described above, for example, an entire work is immersed in a chlorine-based solvent stored in a cleaning tank, and an ultrasonic wave is attached to the cleaning tank. There is a cleaning method in which a vibrator is vibrated to remove foreign substances such as cutting chips and oil attached to a work by cavitation action of a chlorine-based solvent. [0003] However, when the work is cleaned only with a chlorine-based solvent as described above, the chlorine-based solvent is not only harmful to the human body and the environment, but also dissolves the resin material. It is an unsuitable solvent for cleaning resin products such as printed circuit boards because it is easy to use. And, if a small work capacity and washing treatment with chlorinated solvent, condensation occurs at the time of the work dry, since the deposited marks such as dust or dirt in the condensation portions remain, that the cleaning effect of the solvent is impaired problem Have a point. [0004] In view of the above problems, the present invention provides a residue-free cleaning process that requires an advanced technique by cleaning an uncleaned workpiece with a petroleum-based solvent and then immersing the workpiece in an FC-based solvent. It is an object of the present invention to provide a workpiece cleaning apparatus capable of easily performing the cleaning and cleaning the entire workpiece reliably and neatly. SUMMARY OF THE INVENTION [0005] A work cleaning apparatus according to the present invention is a method for cleaning an uncleaned work in a petroleum solvent heated to a temperature suitable for separating and removing foreign substances adhering to the work. A second washing tank for immersing the workpiece in an FC solvent having a higher specific gravity of the solvent itself and a lower temperature than the petroleum solvent is provided at a position subsequent to the first washing tank for performing the washing treatment by immersion in the second washing tank. The second cleaning tank is disposed downstream of the second cleaning tank.
Of solvent in which petroleum solvent and FC solvent are emulsified
Allow the flow and overflow the solvent
Is disposed and a first specific gravity separation tank for separating specific gravity is provided.
Separated by the first specific gravity separation tank into the first specific gravity separation tank
Only the petroleum solvent with a low specific gravity that floats on the liquid surface
Forming an oil discharge passage for discharging to the lower part of the first specific gravity separation tank.
On the flow side, excess FC solvent from the first specific gravity separation tank
While allowing the flow, the first specific gravity separation tank
Specific gravity for storing the FC solvent with high specific gravity separated by separation
A separation tank is provided, and the separation tank is provided downstream of the second specific gravity separation tank.
Allow overflow of FC solvent from second specific gravity separation tank
And the cleaning set above the second cleaning tank.
FC-based solvent in the steam drying area to dry processed workpieces
A solvent distillation tank for releasing steam is provided, and the second washing tank is provided.
Then, the FC solvent stored in the second specific gravity separation tank is
2 Circulating supply to the liquid surface of the washing tank and discharging,
Aggressively overflows petroleum-based solvents that have surfaced
It is a workpiece cleaning device provided with a liquid level cleaning nozzle . According to the work cleaning apparatus of the present invention , the whole work is
After being immersed in a petroleum-based solvent in a first cleaning tank heated to a temperature suitable for separating and removing foreign matter adhering to the work, foreign matter such as cutting chips and oil adhering to the work is washed and removed. The petroleum-based solvent containing foreign matter attached to the work is immersed in the FC-based solvent in the second cleaning tank having a lower temperature than the system-based solvent.
Peeling and removal are performed by a synergistic effect of a temperature difference and a specific gravity difference generated between the FC-based solvent. Compared to petroleum-based solvents with low specific gravity
The first emulsification tank separates the solvent emulsified with the heavy FC solvent.
And separate the specific gravity.
Allows light petroleum solvents to float naturally. Liquid in the first specific gravity separation tank
Only light petroleum-based solvents floating on the surface part
Drain more out of the tank. The first specific gravity is separated by the second specific gravity separation tank.
Excessive heavy FC solvent separated by heavy separation tank
Allow to flow and store. Steam set above the second washing tank
In the drying area, use the solvent distillation tank to
Heat the FC-based solvent with a high specific gravity by bar-flow
Releases solvent vapor. Further, the upper part of the second cleaning tank is
The FC solvent stored in the second specific gravity separation tank is subjected to the second washing.
Circulates and supplies to the liquid surface of the tank and discharges it, and floats on the liquid surface
Surface washing to actively overflow the oil-based solvent
A cleaning nozzle is provided to keep the FC solvent constantly exposed to the entire liquid surface of the second cleaning tank. According to the present invention, foreign matter adhering to an uncleaned work is cleaned and removed by a high-temperature petroleum solvent heated to a predetermined temperature, and then the work is removed from the petroleum solvent. Is also immersed in a low-temperature FC solvent to remove the petroleum solvent containing foreign substances adhering to the work by synergistic action between the temperature difference and the specific gravity difference generated with the FC solvent. The separation power required to remove the solvent is obtained, and the residue of petroleum-based solvents, which was difficult to remove by conventional methods, can be reliably removed by washing. Washing process without any problems can be easily performed.
Moreover, the petroleum solvent remaining on the work is peeled off and removed.
Since the entire work is finish-cleaned only with the FC solvent, the entire work can be surely and cleanly cleaned, and is optimal for cleaning precision parts such as electronic parts and electric parts. Ma
The solvent in which the petroleum-based solvent and FC-based solvent are emulsified
Separate and place light petroleum-based solvent on the liquid surface of FC-based solvent.
Floats naturally and separates it, thereby circulating the FC solvent.
Recycling is possible, and the recycling rate can be improved.
You. Furthermore, the specific gravity floating on the liquid surface of the first specific gravity separation tank
Only light petroleum solvents are discharged outside the tank through the oil drain
This facilitates the circulating supply of FC-based solvents,
Ensures that only petroleum-based solvents are
It can be discharged outside the tank. By the second specific gravity separation tank
FC solvent with high specific gravity separated in the first specific gravity separation tank
Circulates by overflowing and storing
High purity of the FC solvent can be maintained. Also
In addition, in the steam drying area set above the second washing tank,
Overflow from the second specific gravity separation tank by the solvent distillation tank
Heated FC solvent with high specific gravity
By discharging, the work taken out from the second cleaning tank
The drying treatment can be performed by heating to an appropriate temperature. and,
The petroleum solvent floating on the liquid surface of the second cleaning tank is cleaned
First specific gravity separation by FC solvent discharged from purification nozzle
Since the water overflows positively toward the tank,
The petroleum-based solvent does not stagnate on the liquid level in the
When removing the plate W from the second washing tank, the petroleum-based solvent is attached again.
Wearing can be prevented. An embodiment of the present invention will be described below in detail with reference to the drawings. The drawing shows a work cleaning apparatus used for cleaning a printed circuit board with through holes as an example of a work. In FIG.
The entire printed circuit board W is immersed in a petroleum-based solvent L (trade name: naphthesol) stored in a predetermined amount in the internal space of the cleaning chamber 2 that is hermetically sealed to wash and remove foreign substances such as cutting chips and oil. First cleaning tank 3 and FC solvent F stored in a predetermined amount
(Product name = Florinert FC-72) Printed circuit board W
Second washing tank 4 for immersing the whole to wash and remove the residual solvent
And the petroleum solvent L and FC solvent F used in the cleaning process
Separation tank 5 for specific gravity separation of FC and FC separated and recovered
A solvent distillation tank 6 for distilling the system solvent F is provided. The first cleaning tank 3 has a printed circuit board W
Petroleum solvent L (trade name =
Naphthesol) is stored in a predetermined amount, and an ultrasonic vibrator 7 for ultrasonically vibrating the petroleum solvent L is provided on the inner wall surface at the bottom of the tank. For example, the ultrasonic vibrator has a vibration frequency of 27 KHz to 200 KHz. 7 is vibrated to induce ultrasonic vibration in the petroleum solvent L. Further, a heater 8 for heating the petroleum-based solvent L is provided on the inner wall surface at the bottom of the tank, and for example, a medium such as oil or water heated to an appropriate temperature is supplied to the heater 8 by circulating the medium. The system solvent L is heated to an appropriate temperature (for example, about 60 ° C.) suitable for separating and removing foreign matter such as cutting chips and oil attached to the printed circuit board W. In addition, one end of a liquid circulation path 13 is connected to the lower liquid storage area of the first washing tank 3 via a valve 9, a circulation pump 10, a filter 11, and a heat exchanger 12, and the same. The other end of the liquid circulation path 13 is connected to the first
It is connected to the upper storage area of the washing tank 3. That is, the circulating pump 10 is driven to circulate and supply the petroleum solvent L stored in the first cleaning tank 3 via the filter 11 and the heat exchanger 12. The above-described tanks 4, 5, and 6 are arranged sequentially on the bottom of a finishing chamber 15 formed inside the same chamber, and are positioned immediately above the second cleaning tank 4. Printed circuit board W
Forms a work entrance 16 of a size that allows entry and exit,
A cooling jacket 17 is provided along the lower side wall surface of the work entrance 16 corresponding to the upper steam region of the second cleaning tank 4, and the upper steam of the water separation tank 19 connected to the lower side wall surface of the work entrance 16 is provided. A cooling coil 18 is disposed in the region, and for example, a refrigerant cooled to an appropriate temperature is circulated and supplied to the cooling jacket 17 and the cooling coil 18, and the FC solvent F discharged into the upper steam region of the second washing tank 4 is discharged. The temperature of the cooling jacket 17 and the cooling coil 18 is maintained at a temperature at which the vapor Fa and the moisture in the air entering the room condense and liquefy. The above-mentioned second cleaning tank 4 contains a printed circuit board W
A predetermined amount of FC solvent F (trade name: Florinert FC-72), which has a higher specific gravity of the solvent itself than the petroleum solvent L described above and is kept at a low temperature, is stored at the storage level where the whole is immersed, An ultrasonic vibrator 20 for ultrasonically vibrating the FC-based solvent F is provided on the inner wall surface of the bottom of the tank.
The ultrasonic vibrator 20 is vibrated at a vibration frequency of 200 KHz to induce ultrasonic vibration in the FC solvent F. In addition, a liquid level cleaning nozzle 21 is disposed on the upstream side wall surface at a height level that is horizontal with respect to the petroleum solvent L floating on the liquid level portion of the second cleaning tank 4. The discharge direction is fixed toward the specific gravity separation tank 5 disposed downstream. In addition, between the upper end wall of the second washing tank 4 arranged on the upstream side and the specific gravity separation tank 5 arranged on the downstream side, the specific gravity separation tank on the downstream side from the second washing tank 4 on the upstream side. 5 for overflowing each of the solvents L and F emulsified toward 5
2 is oblique. In the specific gravity separation tank 5, a partition plate 5c is provided upright at a position where the liquid storage area inside the tank is divided into a first separation tank 5a and a second separation tank 5b. A partition plate 5d is provided upright at a position where the liquid storage region 5b is divided into right and left. An oil drainage path 24 is connected via a valve 23 to the oil floating area of the petroleum solvent L floating on the liquid surface of the first separation tank 5a, and is connected to the lower liquid storage area of the second separation tank 5b. One end of the liquid circulation path 29 is connected via a valve 25, a circulation pump 26, a filter 27, and a heat exchanger 28, and the other end of the liquid circulation path 29 is connected to each of valves 30 and 31.
Are connected to the upper liquid storage area of the second cleaning tank 4 and the liquid level cleaning nozzle 21 via the second cleaning tank 4. That is, the circulation pump 26
To drive the FC solvent F stored in the second separation tank 5b of the specific gravity separation tank 5 via the filter 27 and the heat exchanger 28 into the upper storage area of the second cleaning tank 4 and the liquid level cleaning nozzle. 21
And circulate supply. The solvent distillation tank 6 is provided with a heater 32 for heating the FC solvent F on the inner wall surface at the bottom of the tank, for example, a medium such as oil or water heated to an appropriate temperature. Is circulated and supplied to the heater 32 to heat the FC solvent F to a boiling point at which the FC solvent F evaporates (for example, about 56 ° C.). and,
Between the upper end walls of the specific gravity separation tank 5 disposed on the upstream side and the solvent distillation tank 6 disposed on the downstream side, the specific gravity is separated from the specific gravity separation tank 5 on the upstream side toward the solvent distillation tank 6 on the downstream side. The falling plate 33 for overflowing the FC solvent F is inclined. Assuming that the illustrated embodiment is configured as described above, a method of cleaning the printed circuit board W by the work cleaning apparatus 1 will be described below. First, as shown in FIG. 1, a heater 8 disposed in the first cleaning tank 3 is heated to separate and remove the petroleum-based solvent L stored in the tank from foreign matters adhering to the printed circuit board W. Suitable temperature (eg, about 60
(° C). Thereafter, the uncleaned printed circuit board W is carried into the cleaning chamber 2, and the entire printed circuit board W is immersed in the petroleum-based solvent L stored in the first cleaning tank 3, and then disposed at the bottom of the tank. Since the ultrasonic vibrator 7 is vibrated to wash and remove the printed circuit board W by the cavitation action of the petroleum-based solvent L, foreign substances such as chips and oil adhering to the printed-circuit board W can be reliably removed by the cleaning power of the petroleum-based solvent L. Can be washed away. At the same time, the circulating pump 10 is driven to circulate and supply the petroleum-based solvent L stored in the first washing tank 3 via the filter 11 and the heat exchanger 12. Next, the heater 32 disposed in the solvent distillation tank 6 is heated to heat the FC solvent F stored in the tank to an appropriate temperature (for example, about 56 ° C.) and to evaporate. The vapor Fa of the vaporized FC solvent F is discharged to the entire finishing chamber 15. Thereafter, the printed circuit board W subjected to the primary cleaning is carried into the finishing chamber 15, passed through the vapor Fa of the FC solvent F discharged into the upper vapor region of the second cleaning tank 4, and stored in the tank. After being immersed from above in the FC solvent F, which has a higher specific gravity than the liquid petroleum solvent L and has a lower temperature,
By vibrating the ultrasonic transducer 20 disposed at the bottom of the tank, F
The petroleum-based solvent L containing foreign matter adhered to the printed circuit board W is removed by cavitation of the C-based solvent F. That is, since the FC solvent F has a lower surface tension and is superior in permeability as compared with chlorofluorocarbon and the like, the petroleum solvent L attached to the surface portion of the printed circuit board W can be reliably peeled and removed. . At the same time, the high-temperature petroleum solvent L peeled and removed from the printed circuit board W is emulsified in the FC solvent F, and the high-temperature, light-weight petroleum solvent L is spontaneously floated on the liquid surface of the second cleaning tank 4. Let it. The circulating pump 26 is driven to remove the FC solvent F stored in the second separation tank 5 b of the specific gravity separation tank 5 via the filter 27 and the heat exchanger 28 into the liquid in the second washing tank 4. The liquid is supplied to the surface cleaning nozzle 21 in a circulating manner.
The petroleum-based solvent L containing foreign matters floating on the liquid surface of the second washing tank 4 is removed from the FC-based solvent F discharged from the tank 1 by a specific gravity separation tank 5.
Is positively overflowed toward the first separation tank 5a, and the state in which the FC solvent F is always exposed to the entire liquid surface of the second washing tank 4 is maintained. Next, the respective solvents L and F having different specific gravities overflow to the first separation tank 5a side of the specific gravity separation tank 5 in a state of being emulsified, and the FC solvent F having a high specific gravity and the petroleum system having a light specific gravity are overflowed. Separation from solvent L by specific gravity. That is, the petroleum-based solvent L having a low specific gravity naturally floats on the liquid surface of the FC solvent F stored in the first separation tank 5a of the specific gravity separation tank 5, and floats on the liquid surface of the first separation tank 5a. Only the petroleum-based solvent L having a low specific gravity is discharged from the oil discharge passage 24 to the outside of the tank. On the other hand, the heavy FC-based solvent F stored in the lower storage area of the first separation tank 5a overflows to the second separation tank 5b side,
The FC solvent F stored in the separation tank 5b overflows to the solvent distillation tank 6 side. At the same time, the FC solvent F stored in the solvent distillation tank 6 is heated by the heater 32 to release the vapor Fa of the FC solvent F to the entire finishing chamber 15 and to remove the vapor Fa from the second cleaning tank 4. The cooling jacket 17 disposed in the upper steam area
Since the vapor Fa of the C-based solvent F is condensed and liquefied, the distilled FC-based solvent F is supplied dropwise to the second cleaning tank 4. Next, after the cleaning is completed, the entire printed circuit board W is taken out from the FC solvent F stored in the second cleaning tank 4, and the FC solvent F discharged into the upper vapor region of the tank is removed.
The entire printed circuit board W is heated to an appropriate temperature with the steam Fa and dried. Thereafter, the cleaned printed circuit board W is unloaded from the finishing chamber 15 and the printed circuit board W is unloaded from the cleaning chamber 2 to complete the cleaning process for one printed circuit board W. As described above, after the foreign matter adhering to the uncleaned printed circuit board W is removed by washing with the high temperature petroleum solvent L heated to a predetermined temperature, the printed circuit board W is removed more than the petroleum solvent L. The specific gravity of the solvent itself is immersed in the FC solvent F having a large specific gravity and a low temperature, and the petroleum solvent L containing the foreign matter adhering to the printed circuit board W is separated from the temperature difference and the specific gravity difference generated between the solvent L and the FC solvent F. Since separation and removal are performed by synergistic action, a large separation force required for separating the petroleum-based solvent L is obtained,
Petroleum-based solvent L, which was difficult to remove by conventional methods
Residue can be reliably removed by washing, and a residue-free washing process requiring advanced technology can be easily performed. Moreover, since the petroleum-based solvent L remaining on the printed circuit board W is peeled off and the printed circuit board W is finished and cleaned only with the FC-based solvent F, the entire printed circuit board W can be reliably and cleanly cleaned, and electronic components and the like can be cleaned. Ideal for cleaning precision parts such as electrical parts. In addition, petroleum solvents and FC solvents
The emulsified solvent is separated by specific gravity and applied to the liquid surface of the FC solvent.
Separating natural petroleum solvents with low specific gravity by floating naturally
This makes it possible to circulate and supply FC solvents and improve the recycling rate.
You can aim up. Further, the liquid level of the first specific gravity separation tank
Only the petroleum solvent with a low specific gravity that floats on the part
Discharge to the outside of the tank so that the FC solvent can be circulated and supplied.
Simplicity and without the need for complex oil drains
Only the petroleum solvent can be discharged outside the tank. No.
Specific gravity separated in the first specific gravity separation tank by 2 specific gravity separation tank
To overflow and store heavy FC solvent
The purity of the circulating FC solvent should be kept high.
Can be. In addition, it was set above the second washing tank.
In the steam drying area, from the second specific gravity separation tank by the solvent distillation tank
The overflowed heavy FC solvent is heated to F
By releasing the vapor of the C-based solvent, it is removed from the second cleaning tank.
Heating the delivered work to an appropriate temperature for drying
Can be. Further, the petroleum-based solvent L floating on the liquid surface portion of the second cleaning tank 4 is positively overflowed toward the specific gravity separation tank 5 by the FC-based solvent F discharged from the injection nozzle 21, so that the second cleaning is performed. The petroleum-based solvent L does not stagnate on the liquid surface portion of the tank 4, and it is possible to prevent the petroleum-based solvent L from adhering again when the printed circuit board W is taken out from the second cleaning tank 4. In correspondence between the configuration of the present invention and the above-described embodiment, the work of the present invention corresponds to the printed circuit board W of the embodiment, but the present invention is limited to only the configuration of the above-described embodiment. Not something. In the above embodiment, the printed circuit board W is cleaned with the FC solvent F (trade name: Fluorinert FC-72). For example, FC-40, FC-43, and FC-7 are used.
FC solvent F such as 0, FC-75, FC-77, and FC-104 may be selected and used according to the intended use.

【図面の簡単な説明】 【図1】ワーク洗浄装置による洗浄方法を示す全体構成
図。 【符号の説明】 W…プリント基板 L…石油系溶剤 F…FC系溶剤 1…ワーク洗浄装置 3…第1洗浄槽 4…第2洗浄槽 5…比重分離槽 6…溶剤蒸溜槽 7,20…超音波振動子
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is an overall configuration diagram showing a cleaning method using a work cleaning apparatus. [Description of Signs] W ... Printed circuit board L ... Petroleum solvent F ... FC solvent 1 ... Work cleaning device 3 ... First cleaning tank 4 ... Second cleaning tank 5 ... Specific gravity separation tank 6 ... Solvent distillation tanks 7, 20 ... Ultrasonic transducer

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B08B 1/00 - 7/04 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int.Cl. 7 , DB name) B08B 1/00-7/04

Claims (1)

(57)【特許請求の範囲】 【請求項1】未洗浄のワークを、該ワークに付着する異
物を分離除去するのに適した温度に加温された石油系溶
剤中に浸漬して洗浄処理する第1洗浄槽の後段位置に、
該ワークを上記石油系溶剤よりも溶剤自体の比重が重く
温度の低いFC系溶剤中に浸漬して洗浄処理する第2洗
浄槽を配設し、 上記第2洗浄槽の下流側に、上記第2洗浄槽から石油系
溶剤とFC系溶剤とが乳化した溶剤のオーバーフローを
許容するとともに、オーバーフローした該溶剤を貯液し
比重分離する第1比重分離槽を配設し、 上記第1比重分離槽に、上記第1比重分離槽によって分
離されて液面部分に浮上した比重の軽い石油系溶剤のみ
を槽外部に排出する排油路を形成し、 上記第1比重分離槽の下流側に、上記第1比重分離槽か
らFC系溶剤のオーバーフローを許容するとともに、上
記第1比重分離槽によって分離された比重の重いFC系
溶剤を貯液する第2比重分離槽を配設し、 上記第2比重分離槽の下流側に、上記第2比重分離槽か
らのFC系溶剤のオーバーフローを許容するとともに、
上記第2洗浄槽の上方に設定した洗浄済みワークを乾燥
処理する蒸気乾燥領域にFC系溶剤の蒸気を放出する溶
剤蒸留槽を配設し、 上記第2洗浄槽に、上記第2比重分離槽に貯液したFC
系溶剤を上記第2洗浄槽の液面部分に循環供給して吐出
し、該液面部分に浮上した石油系溶剤を積極的にオーバ
ーフローさせる液面洗浄ノズルを配設した ワーク洗浄装
置。
(57) [Claims] [Claim 1] A cleaning process in which an uncleaned work is immersed in a petroleum-based solvent heated to a temperature suitable for separating and removing foreign matters adhering to the work. In the position after the first washing tank
A second cleaning tank for immersing the workpiece in an FC solvent having a higher specific gravity of the solvent itself than the petroleum solvent itself and having a lower temperature is disposed , and the second cleaning tank is provided downstream of the second cleaning tank. From 2 washing tanks to petroleum
Solvent overflow of solvent emulsified with FC solvent
Allow and store the overflowed solvent.
A first specific gravity separation tank for performing specific gravity separation is provided, and the first specific gravity separation tank is separated into the first specific gravity separation tank by the first specific gravity separation tank.
Only petroleum-based solvents with a low specific gravity that have separated and floated on the liquid surface
An oil discharge passage for discharging the oil to the outside of the tank, and the first specific gravity separation tank is provided downstream of the first specific gravity separation tank.
Allow the FC solvent to overflow,
FC system with heavy specific gravity separated by the first specific gravity separation tank
A second specific gravity separation tank for storing a solvent is provided, and the second specific gravity separation tank is provided downstream of the second specific gravity separation tank.
While allowing the overflow of these FC solvents,
Dry the cleaned work set above the second cleaning tank
Solvent that releases vapor of FC solvent into the steam drying area to be treated
A FC distillation tank is disposed in the second washing tank and the FC stored in the second specific gravity separation tank.
The system solvent is circulated and supplied to the liquid surface of the second cleaning tank and discharged.
And the oil-based solvent floating on the liquid surface
-A workpiece cleaning device equipped with a liquid level cleaning nozzle for flow .
JP30313592A 1992-10-14 1992-10-14 Work cleaning device Expired - Lifetime JP3379019B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30313592A JP3379019B2 (en) 1992-10-14 1992-10-14 Work cleaning device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30313592A JP3379019B2 (en) 1992-10-14 1992-10-14 Work cleaning device

Publications (2)

Publication Number Publication Date
JPH06126257A JPH06126257A (en) 1994-05-10
JP3379019B2 true JP3379019B2 (en) 2003-02-17

Family

ID=17917308

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30313592A Expired - Lifetime JP3379019B2 (en) 1992-10-14 1992-10-14 Work cleaning device

Country Status (1)

Country Link
JP (1) JP3379019B2 (en)

Also Published As

Publication number Publication date
JPH06126257A (en) 1994-05-10

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