JPH0448514B2 - - Google Patents
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- JPH0448514B2 JPH0448514B2 JP59173084A JP17308484A JPH0448514B2 JP H0448514 B2 JPH0448514 B2 JP H0448514B2 JP 59173084 A JP59173084 A JP 59173084A JP 17308484 A JP17308484 A JP 17308484A JP H0448514 B2 JPH0448514 B2 JP H0448514B2
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Description
〔産業上の利用分野〕
本発明は金属、ガラス、プラスチツク等の熱容
量の小さい薄い被洗浄物又はひだもしくは凹部を
有する被洗浄物を沸点の低い塩化メチレン溶剤で
蒸気洗浄する洗浄方法に関する。
〔従来の技術〕
金属、ガラス、プラスチツク等の材料の表面に
は種々の油分が付着しているが、この油分を除去
するために、従来よりハロゲン化炭化水素、アル
コール、ケトン等の有機溶剤を用いた溶剤洗浄法
が広く採用されている。例えば、機械部品等にめ
つきや塗装を施したりなどする場合に、その前処
理としてこれら機械部品等に付着している油分を
上記の有機溶剤で脱脂洗浄することが行われてい
る。
この場合、有機溶剤による脱脂洗浄は、一般に
被洗浄物を常温の有機溶剤に浸漬した後、(なお、
必要により常温の有機溶剤で超音波洗浄すること
もできる)、有機溶剤の飽和蒸気に被洗浄物を接
触させて、蒸気洗浄を行う方法が多く採用され、
このように蒸気洗浄法は溶剤脱脂工程の最終段階
で被洗浄物を仕上げ洗浄すると共に、被洗浄物の
乾燥を併せ行うことを目的として行われている。
ここで、蒸気洗浄法は有機溶剤の飽和蒸気温度
(沸点)より低い温度の被洗浄物を溶剤の飽和蒸
気ゾーンの中に入れることにより、被洗浄物が溶
剤の蒸気から熱を奪うため、被洗浄物の表面に溶
剤の蒸気が凝縮液化し、被洗浄物の表面に付着し
ている汚れを洗い取りながら液雫となつて流れ落
ち、被洗浄物の表面を洗浄するものである。この
場合、溶剤蒸気による洗浄作用は被洗浄物が溶剤
の沸点温度に昇温されるまでの間続き、被洗浄物
の温度が溶剤の沸点温度に到達すると、その表面
での蒸気の凝縮は終結する。その後、溶剤が付着
した状態で被洗浄物を蒸気槽より取り出して大気
中に放置すると溶剤が大気中に揮発し、被洗浄物
が乾燥するものである。
〔発明が解決しようとする課題〕
しかしながら、上述したような筑気洗浄法は、
その乾燥の際、溶剤の気化熱で被洗浄物が冷却さ
れ、大気中の水蒸気が被洗浄物の表面に付着(結
露)してシミを生じさせたり大気中の埃が再付着
するなどして汚れを生じさせる場合がある。ここ
で、被洗浄物の熱容量が大きく、かつ形状も比較
的単純なものの場合はこのような問題が生じるこ
とは比較的少ないが、被洗浄物が熱容量の小さい
薄物などの場合には、この結露がしばしば問題と
なる。また、比較的熱容量の大きい被洗浄物であ
つても、ひだが多い部品や凹部のある部品では、
蒸気洗浄後、蒸気槽から取り出す場合に凝縮した
溶剤の持出し量が多くなるため、蒸発に伴つて失
われる熱量も多くなり、従つて結露を生じること
も多く、しかも持出しによる溶剤ロスも多くなる
ので洗浄コストが上がり、また作業環境面でも問
題を生じさせる。そして、かかる問題は、特に蒸
発熱が約80cal/gで低沸点(約70℃)の塩化メ
チレンを使用した場合に生じ易いものであつた。
即ち、洗浄用の有機溶剤としては1,1,1−
トリクロルエタン,トリクロルエチレン,パーク
ロルエチレンなどが広く使用されているが、これ
らの沸点、蒸発潜熱は1,1,1−トリクロルエ
タンが74.0℃,57.7cal/g,トリクロルエチレン
が87.2℃,57.2cal/g,パークロルエチレンが
121.2℃,50.0cal/gである。また、フロン113は
沸点が47.6℃であるが、蒸発潜熱が35.1cal/gで
速乾性が大きく、このためこれらの溶剤を使用し
た場合には、結露はそれほど重大な問題にならな
い。しかし、塩化メチレンの沸点は40.4℃、蒸発
潜熱は78.7cal/gで、上記溶剤より低沸点であ
る上、蒸発潜熱が大きく、このような塩化メチレ
ンを用いて蒸気洗浄した被洗浄物を大気中に取り
出した場合、被洗浄物が室温以下に冷却され、露
点温度以下になり易く、結露が重大な問題になる
ものであつた。
このため、熱容量の小さい薄い被洗浄物或いは
ひだや凹部の多い被洗浄物を低沸点でしかも蒸発
潜熱の比較的大きい塩化メチレンを用いて蒸気洗
浄した場合、被洗浄物を大気中に取り出すと被洗
浄物に付着した塩化メチレンが気化する際にその
気化熱で被洗浄物を室温以下に冷却してその表面
に大気中の水蒸気が容易に凝縮して結露を生じさ
せるという問題点を解決することが要望された。
更にまた、従来行われている蒸気洗浄法では、
溶剤飽和蒸気の蒸気ゾーン中に冷えた被洗浄物を
搬入すると、蒸気ゾーンは被洗浄物に引きつけら
れるように下降し、被洗浄物の表面で凝縮が始ま
り、被洗浄物の温度が溶剤の沸点温度に達するま
で凝縮が進み、その後再び蒸気ゾーンは上昇し、
所定の位置に蒸気ゾーンを形成する。このような
蒸気ゾーンが降下、上昇して蒸気ゾーンを乱す現
象(蒸気ゾーン破壊現象)は飽和蒸気の温度と被
洗浄物の温度との差及び被洗浄物の熱容量の大小
によつて観察される現象であるが、蒸気ゾーンが
乱れることは溶剤蒸気の飛散によるロスを多くさ
せるものであつた。
従つて、本発明は熱容量の小さい薄い被洗浄物
やひだもしくは凹部を有する被洗浄物を塩化メチ
レンの蒸気で脱脂洗浄するに当り、洗浄後に被洗
浄物の表面に水蒸気が結露することが防止され、
従つて被洗浄物にシミが生じる不都合が防止され
ると共に、溶剤の持ち出しロスをなくすことがで
き、蒸気ゾーン破壊現象を確実に防止して、蒸気
ゾーンを安定に維持できる蒸気洗浄方法を提供す
ることを目的とする。
課題を解決するための手段〕
本発明は、上記目的を達成するため、熱容量の
小さい薄い被洗浄物又はひだもしくは凹部を有す
る被洗浄物を複数の洗浄槽内にそれぞれ収容され
た塩化メチレン溶剤で順次洗浄するに際し、最後
の洗浄槽を塩化メチレン蒸気槽とし、この蒸気槽
内のメチレン蒸気域に過熱用ヒーターを設け、こ
のヒーターにより塩化メチレン蒸気をその沸点よ
りも5〜60℃高温に過熱して上記蒸気槽内上部に
過熱蒸気域を形成すると共に、上記複数の洗浄槽
の上方に、上記過熱蒸気域から流出する過熱蒸気
により上記複数の洗浄槽を覆つて流出過熱蒸気域
を形成し、上記被洗浄物を上記洗浄槽内の塩化メ
チレンで洗浄し、最後の上記流出過熱蒸気域を通
ることにより該流出過熱蒸気域で加熱された被洗
浄物を上記塩化メチレンの沸点より5〜60℃高温
に過熱された蒸気槽内の過熱蒸気域に該過熱蒸気
域を破壊することなく導入し、この過熱蒸気域で
被洗浄物を洗浄すると共に、該過熱蒸気温度にな
るまで加熱乾燥した後、被洗浄物を取り出すよう
にしたものである。
ここで、被洗浄物の材質としては、ガラス、プ
ラスチツク及び各種金属等、有機溶剤に侵されな
い物質で過熱蒸気の温度に耐えるものなら何でも
使用することができる。
〔作 用〕
本発明に係る蒸気洗浄方法は、複数の洗浄槽内
にそれぞれ収容された塩化メチレン溶剤で被洗浄
物を順次洗浄する際、最後の工程で塩化メチレン
の飽和蒸気をその沸点より5〜60℃高温に過熱し
て得られる過熱蒸気に被洗浄物を接触させて洗浄
を行うものであり、これにより被洗浄物の表面に
空気中の水蒸気が結露せず、シミの発生が防止さ
れる。即ち、本発明においては、塩化メチレンの
沸点以下の温度の被洗浄物が塩化メチレンの過熱
蒸気に触れると、この過熱蒸気から熱を受けて過
熱されると同時に過熱蒸気は熱を奪われて冷却さ
れ、被洗浄物の表面に凝縮液化して洗浄が行われ
る。この洗浄は被洗浄物の温度が塩化メチレンの
沸点になるまで継続する。被洗浄物が塩化メチレ
ンの沸点に達すると凝縮は終了するが、周囲が過
熱蒸気なのでその蒸気の温度に達するまでに更に
加熱され、同時に被洗浄物の表面に凝縮して付着
した液状の塩化メチレンは気化蒸発する。従つて
被洗浄物が塩化メチレンの過熱蒸気の温度に到達
した時点ですでに被洗浄物の表面は良く乾燥され
ており、大気中に取り出しても被洗浄物に液状で
付着して洗浄槽の外に持ち出される塩化メチレン
の損失はなくなり、また付着塩化メチレン溶液の
気化蒸発に起因する水蒸気の結露による汚れやシ
ミなどの不都合は避けられるものである。
また、本発明においては、蒸気槽内に過熱蒸気
域が形成され、これは塩化メチレンの沸点より5
〜60℃高温に過熱されているので、通常の蒸気ゾ
ーンより安定で乱れがない上、上記複数の洗浄槽
の上方にもこの蒸気槽から流出する過熱蒸気によ
る流出過熱蒸気域が形成されているため、塩化メ
チレンの沸点以下に冷やされた被洗浄物を蒸気槽
に搬入する場合、流出過熱蒸気により直ちに加熱
され、形成されている蒸気槽内の過熱蒸気域を破
壊することはない。
このため、蒸気槽内の過熱蒸気域が乱されず、
安定した蒸気ゾーンが維持されることにより、塩
化メチレンのロスを極度に押えることができる。
即ち、本発明によれば、被洗浄物として熱容量
の小さいもの或いはひだや凹部の多いものを低沸
点で蒸発潜熱の大きい塩化メチレンで蒸気洗浄し
ても、被洗浄物が十分に乾燥され、塩化メチレン
が被洗浄物に付着して大気中で気化蒸発すること
がなく、大気中の水蒸気の結露によるシミのない
表面状態のきれいな洗浄仕上りが得られると共
に、被洗浄物を洗浄乾燥する蒸気槽内の過熱蒸気
域が流出過熱蒸気域で保護されているため、蒸気
槽内の過熱蒸気域が安定化され、塩化メチレンの
ロスを防止し、かつ安定した洗浄が可能になるも
のである。
次に、本発明の実施例を図面を参照して説明す
る。
〔実施例〕
第1図は本発明の実施に使用する洗浄装置の一
例を示すもので、この装置は、溶剤洗浄槽として
超音波槽1,冷浴槽2,蒸気槽3を順次並設した
三槽式に構成されている。これら槽1,2,3内
にはそれぞれ塩化メチレン溶剤4が収容されてお
り、被洗浄物はまず超音波槽1内において超音波
洗浄され、次いで冷浴槽2内の溶剤(塩化メチレ
ン)で洗浄され、最後に蒸気槽3内に搬入され
る。
ここで、超音波洗浄し、次いで冷浴槽で洗浄
し、最後に蒸気槽に搬入することは公知の方法で
あるが、本発明はこの蒸気槽に搬入した後の蒸気
洗浄方法に特徴を有するものである。
即ち、この蒸気槽3の底部には加熱ヒーター6
が配設され、このヒーター6により蒸気槽3内の
溶剤(塩化メチレン)4が加熱されて溶剤の飽和
蒸気が発生し、溶剤4の上方に飽和蒸気域4aが
形成される。更に、この飽和蒸気域4a内には飽
和蒸気を過熱するための蒸気過熱用ヒーター7が
設置され、この過熱用ヒーター7により飽和蒸気
域4aはその沸点より5〜60℃高温度に過熱さ
れ、蒸気槽3内の上部に過熱蒸気域4bが形成さ
れる。この場合、過熱用ヒーター7は電気ヒータ
ー、熱循環型のヒーター等を使用することがで
き、電気ヒーターを用いる場合には所望する温度
に調節できるようにスライダツク8を電気回路に
接続することができる。
なお過熱用ヒーター7の熱量は飽和蒸気発生用
のヒーター6の熱量の1/4〜1/5程度の熱量でよ
く、この程度の熱量を与えることで十分過熱蒸気
が得られる。また、過熱用ヒーター7は飽和蒸気
域を過熱することが目的であるから、フインなど
を設けて伝熱面積を大きくし、また、邪魔板など
を設けて蒸気4aとの接触を良くし、過熱効率を
挙げることが好ましい。この場合、蒸気槽3外壁
を保温加工等することにより、熱効率を高めるこ
とができる。また、溶剤の過熱蒸気温度はスライ
ダツク8を調整するなどのことにより容易に所望
する温度に調整することができるものであり、溶
剤の沸点、被洗浄物及び溶剤の耐熱性等を考慮し
て適宜決めることができるが、塩化メチレンの沸
点(約40℃)温度よりも5〜60℃高めの温度の範
囲で選定するものである。
また、上記超音波槽1の一側壁及び蒸気槽3の
他側壁はそれぞれ上方に延出され、これら両側壁
に囲まれた各層1,2,3の上方空間には、上記
蒸気槽3の過熱蒸気域4bから過熱蒸気が流れ、
ここに、流出過熱蒸気域4cが形成されている。
この場合、両過熱蒸気域4b,4cの温度は同じ
温度ではなく、また蒸気槽3より超音波槽1の方
向に離れるほど、過熱蒸気温度が低くなる温度分
布を持つものである。なお、上記両側壁の上部に
は蒸気冷却パイプ9が配設されており、流出過熱
蒸気域4cの過熱蒸気は蒸気冷却パイプ9により
冷却されるので、冷却パイプ9配設位置より上方
に飛散することは防止される。ここで、冷却方法
は通常の方法を採用することができ、例えば冷却
パイプ内に水道水や井戸水を供給するか、また低
沸点の洗浄剤を用いた場合は冷凍機により冷却さ
れた冷媒を使用することができる。上記冷却パイ
プ9により凝縮された溶剤は、水分離器10を経
て冷浴槽2内に回収される。
而して、上記のように冷浴槽2で洗浄された被
洗浄物は蒸気槽3内の過熱蒸気域4bで洗浄さ
れ、乾燥されるものであり、このように被洗浄物
は最後に塩化メチレンの過熱蒸気により洗浄され
るので、洗浄後に被洗浄物の表面に水蒸気が結露
することが可及的に防止され、従つて被洗浄物に
シミが生じる不都合が防止されると共に、溶剤の
持ち出しロスを少なくすることができる。また、
このように蒸気槽3内に過熱蒸気域4bが形成さ
れているだけでなく、洗浄装置全体が流出過熱蒸
気域4cで覆われているため、溶剤の沸点以下に
冷やされた被洗浄物を冷浴槽2から蒸気槽3に搬
入した場合でも流出過熱蒸気域4cの過熱蒸気に
より加熱されるので、形成されている蒸気槽3内
の過熱蒸気域4bを破壊することがない。このた
め、過熱蒸気域4bが乱されず、安定した蒸気ゾ
ーンが維持される。
また、第2図は本発明の実施に用いる洗浄装置
の他の例を示すもので、この例は公知の飽和蒸気
洗浄に加えて飽和蒸気洗浄後に過熱蒸気洗浄を行
うようにした装置の例である。
即ち、この装置は、飽和蒸気槽11と過熱蒸気
槽3とをその内部下部において連通した状態で配
設し、飽和蒸気槽11内の上部に形成される飽和
蒸気域4aと過熱蒸気槽3内の上部に形成される
過熱蒸気域4bとを仕切部12により仕切り、飽
和蒸気域4a内には溶剤4の飽和蒸気を充満さ
せ、過熱蒸気域4b内には過熱蒸気を充満させる
ようにしたものであつて、更に両蒸気槽11,3
の上方空間には、第1図の装置の場合と同様に上
記過熱蒸気域4bから流出する過熱蒸気により流
出過熱蒸気域4cが形成されているものである。
この第2図の装置も、このように過熱蒸気槽3
内に過熱蒸気域4bが形成されているだけでな
く、洗浄装置全体が流出過熱蒸気域4cで覆われ
ているため、塩化メチレンの沸点以下に冷やされ
た被洗浄物を搬入した場合、流出過熱蒸気域4c
の過熱蒸気の温度がある程度降下するが、形成さ
れている飽和蒸気槽11の飽和蒸気域4aを破壊
するまでに至らず、過熱蒸気域4bも乱されな
い。このため安定した過熱蒸気域4bが維持さ
れ、溶剤のロスを極度に押えることができると共
に、安定した洗浄が行われるものである。
次に実験例を示す。
実験例 1
溶剤として塩化メチレンを使用し、第1図に示
す装置の蒸気槽を用いて過熱蒸気で洗浄したテス
ト試料及び飽和蒸気で洗浄したテスト試料の結露
発生の有無と溶剤の持ち出しの有無を確認した。
テスト結果を第1表に示す。
[Industrial Field of Application] The present invention relates to a cleaning method for steam cleaning thin objects having a small heat capacity such as metals, glass, plastics, etc., or objects having folds or recesses, using a methylene chloride solvent having a low boiling point. [Prior Art] Various oils adhere to the surfaces of materials such as metals, glass, and plastics, and in order to remove these oils, organic solvents such as halogenated hydrocarbons, alcohols, and ketones have traditionally been used. The solvent cleaning method used has been widely adopted. For example, when applying plating or painting to mechanical parts, etc., as a pretreatment, oil adhering to these mechanical parts is degreased and cleaned using the above-mentioned organic solvent. In this case, degreasing with an organic solvent is generally carried out after immersing the object to be cleaned in an organic solvent at room temperature (in addition,
If necessary, ultrasonic cleaning can be performed using an organic solvent at room temperature), and steam cleaning is often performed by bringing the object to be cleaned into contact with saturated vapor of an organic solvent.
As described above, the steam cleaning method is carried out for the purpose of finishing cleaning the object to be cleaned at the final stage of the solvent degreasing process and also drying the object. Here, in the steam cleaning method, the object to be cleaned, whose temperature is lower than the saturated vapor temperature (boiling point) of the organic solvent, is placed in the saturated steam zone of the solvent, so that the object to be cleaned absorbs heat from the solvent vapor. The vapor of the solvent condenses and liquefies on the surface of the object to be cleaned, and flows down as droplets while washing away the dirt adhering to the surface of the object to be cleaned, thereby cleaning the surface of the object to be cleaned. In this case, the cleaning action of the solvent vapor continues until the temperature of the object to be cleaned reaches the boiling point of the solvent, and when the temperature of the object to be cleaned reaches the boiling point of the solvent, the condensation of the vapor on the surface ends. do. Thereafter, when the object to be cleaned is taken out of the steam bath with the solvent attached and left in the atmosphere, the solvent evaporates into the atmosphere and the object to be cleaned dries. [Problem to be solved by the invention] However, the above-mentioned chikke cleaning method
During drying, the object to be cleaned is cooled by the heat of vaporization of the solvent, causing water vapor in the atmosphere to adhere to the surface of the object (condensation), causing stains, and dust in the atmosphere to re-adhere. May cause stains. If the object to be cleaned has a large heat capacity and is relatively simple in shape, this problem is relatively unlikely to occur, but if the object to be cleaned is thin and has a small heat capacity, this condensation may occur. is often a problem. In addition, even if the object to be cleaned has a relatively large heat capacity, parts with many folds or recesses may
When taking out the solvent from the steam tank after steam cleaning, a large amount of condensed solvent is taken out, so a large amount of heat is lost through evaporation, which often causes condensation, and moreover, solvent loss due to taking out also increases. This increases cleaning costs and also creates problems in the working environment. Such problems are particularly likely to occur when methylene chloride, which has a heat of vaporization of about 80 cal/g and a low boiling point (about 70° C.), is used. That is, as an organic solvent for cleaning, 1,1,1-
Trichloroethane, trichlorethylene, perchlorethylene, etc. are widely used, and their boiling point and latent heat of vaporization are 74.0℃ and 57.7cal/g for 1,1,1-trichloroethane, and 87.2℃ and 57.2cal for trichlorethylene. /g, perchlorethylene
121.2℃, 50.0cal/g. Furthermore, although Freon 113 has a boiling point of 47.6° C., it has a latent heat of vaporization of 35.1 cal/g and dries quickly, so when these solvents are used, condensation does not become a serious problem. However, methylene chloride has a boiling point of 40.4°C and a latent heat of vaporization of 78.7 cal/g, which is lower than the above solvents and has a large latent heat of vaporization. When the object to be cleaned is taken out at a later date, the object to be cleaned is cooled to below room temperature and tends to drop below the dew point temperature, causing dew condensation to become a serious problem. For this reason, if a thin object with a small heat capacity or an object with many folds or recesses is steam-cleaned using methylene chloride, which has a low boiling point and a relatively large latent heat of vaporization, the object will be exposed to the air when it is taken out into the atmosphere. To solve the problem that when methylene chloride adhering to an object to be cleaned evaporates, the object to be cleaned is cooled to below room temperature by the heat of vaporization, and water vapor in the atmosphere easily condenses on the surface of the object, causing dew condensation. was requested. Furthermore, in the conventional steam cleaning method,
When a cold object to be cleaned is brought into the vapor zone of solvent-saturated steam, the vapor zone descends as it is attracted to the object, condensation begins on the surface of the object, and the temperature of the object reaches the boiling point of the solvent. Condensation continues until the temperature is reached, then the vapor zone rises again,
Forming a steam zone at a predetermined location. This phenomenon in which the steam zone descends and rises and disturbs the steam zone (steam zone destruction phenomenon) is observed based on the difference between the temperature of saturated steam and the temperature of the object to be cleaned, and the size of the heat capacity of the object to be cleaned. Although this is a phenomenon, the disturbance of the vapor zone increases the loss of solvent vapor due to scattering. Therefore, the present invention prevents water vapor from condensing on the surface of the object after cleaning when degreasing and cleaning thin objects with small heat capacity or objects having folds or recesses with methylene chloride vapor. ,
Therefore, to provide a steam cleaning method that prevents the inconvenience of stains on objects to be cleaned, eliminates the loss of solvent carried out, reliably prevents the steam zone destruction phenomenon, and maintains the steam zone stably. The purpose is to Means for Solving the Problems] In order to achieve the above object, the present invention cleans a thin object having a small heat capacity or an object to be cleaned having folds or recesses using a methylene chloride solvent contained in a plurality of cleaning tanks. When performing sequential cleaning, the last cleaning tank is a methylene chloride vapor tank, and a superheating heater is provided in the methylene vapor region within this steam tank, and this heater superheats the methylene chloride vapor to a temperature 5 to 60°C higher than its boiling point. forming a superheated steam region in the upper part of the steam tank, and forming an outflow superheated steam region above the plurality of cleaning tanks by covering the plurality of cleaning tanks with superheated steam flowing out from the superheated steam region; The object to be cleaned is washed with methylene chloride in the washing tank, and the object heated in the outflow superheated steam area is heated by 5 to 60°C above the boiling point of the methylene chloride. Introducing the superheated steam region in a steam tank superheated to a high temperature without destroying the superheated steam region, cleaning the object to be cleaned in this superheated steam region, and heating and drying it until the superheated steam temperature reaches, The item to be cleaned is taken out. Here, as the material of the object to be cleaned, any material can be used as long as it is not attacked by organic solvents and can withstand the temperature of superheated steam, such as glass, plastic, and various metals. [Function] In the steam cleaning method according to the present invention, when an object to be cleaned is sequentially cleaned with methylene chloride solvent contained in a plurality of cleaning tanks, the saturated vapor of methylene chloride is heated to 50% above its boiling point in the last step. Cleaning is performed by bringing the object to be cleaned into contact with superheated steam obtained by heating the object to a high temperature of ~60°C. This prevents water vapor in the air from condensing on the surface of the object and prevents stains from forming. Ru. That is, in the present invention, when an object to be cleaned whose temperature is below the boiling point of methylene chloride comes into contact with the superheated vapor of methylene chloride, it receives heat from the superheated vapor and becomes superheated, and at the same time, the superheated vapor removes heat and is cooled. The liquid condenses and liquefies on the surface of the object to be cleaned. This washing continues until the temperature of the object to be washed reaches the boiling point of methylene chloride. Condensation ends when the object to be cleaned reaches the boiling point of methylene chloride, but since the surrounding area is superheated steam, it is heated further by the time it reaches the temperature of the steam, and at the same time, liquid methylene chloride condenses and adheres to the surface of the object to be cleaned. evaporates. Therefore, by the time the object to be cleaned reaches the temperature of the superheated vapor of methylene chloride, the surface of the object to be cleaned has already been well dried, and even if it is taken out into the atmosphere, it will adhere to the object in liquid form and cause the cleaning tank to become dry. There is no loss of methylene chloride carried outside, and inconveniences such as dirt and stains due to condensation of water vapor caused by vaporization of the adhering methylene chloride solution can be avoided. Further, in the present invention, a superheated steam region is formed in the steam tank, and this region is 55% higher than the boiling point of methylene chloride.
Since it is superheated to a high temperature of ~60°C, it is more stable and less turbulent than a normal steam zone, and an outflow superheated steam area is also formed above the multiple cleaning tanks by the superheated steam flowing out from this steam tank. Therefore, when an object to be cleaned that has been cooled to a temperature below the boiling point of methylene chloride is brought into the steam tank, it is immediately heated by the outflowing superheated steam, and the superheated steam region that has been formed in the steam tank is not destroyed. Therefore, the superheated steam area in the steam tank is not disturbed,
By maintaining a stable vapor zone, methylene chloride loss can be extremely reduced. That is, according to the present invention, even if the object to be cleaned has a small heat capacity or has many folds or recesses, it is steam-cleaned with methylene chloride, which has a low boiling point and a large latent heat of vaporization, and the object to be cleaned is sufficiently dried and the chloride is removed. Methylene does not adhere to the object to be cleaned and evaporate in the atmosphere, and a clean surface finish with no stains caused by condensation of water vapor in the atmosphere can be obtained. Since the superheated steam region of the tank is protected by the outflow superheated steam region, the superheated steam region in the steam tank is stabilized, preventing loss of methylene chloride and making stable cleaning possible. Next, embodiments of the present invention will be described with reference to the drawings. [Example] Fig. 1 shows an example of a cleaning device used in carrying out the present invention. It is configured in a tank type. Each of these tanks 1, 2, and 3 contains a methylene chloride solvent 4, and the object to be cleaned is first ultrasonically cleaned in the ultrasonic bath 1, and then washed with the solvent (methylene chloride) in the cold bath 2. and finally transported into the steam tank 3. Here, it is a known method to carry out ultrasonic cleaning, then wash in a cold bath, and finally carry it into a steam tank, but the present invention is characterized by the steam cleaning method after carrying into the steam tank. It is. That is, a heating heater 6 is installed at the bottom of this steam tank 3.
The heater 6 heats the solvent (methylene chloride) 4 in the steam tank 3 to generate saturated vapor of the solvent, and a saturated vapor region 4a is formed above the solvent 4. Furthermore, a steam superheating heater 7 for superheating the saturated steam is installed in the saturated steam region 4a, and the superheating heater 7 superheats the saturated steam region 4a to a temperature 5 to 60° C. higher than its boiling point. A superheated steam region 4b is formed in the upper part of the steam tank 3. In this case, the overheating heater 7 can be an electric heater, a heat circulation type heater, etc. If an electric heater is used, the slider 8 can be connected to an electric circuit so that the temperature can be adjusted to a desired temperature. . Note that the amount of heat of the heater 7 for superheating may be about 1/4 to 1/5 of the amount of heat of the heater 6 for generating saturated steam, and by providing this amount of heat, sufficient superheated steam can be obtained. In addition, since the purpose of the superheating heater 7 is to superheat the saturated steam region, fins etc. are provided to increase the heat transfer area, and baffles etc. are provided to improve contact with the steam 4a. It is preferable to increase efficiency. In this case, thermal efficiency can be increased by subjecting the outer wall of the steam tank 3 to heat insulation processing. In addition, the superheated steam temperature of the solvent can be easily adjusted to a desired temperature by adjusting the slider 8, etc., and can be adjusted as appropriate by considering the boiling point of the solvent, the heat resistance of the object to be cleaned, the solvent, etc. Although it can be determined, the temperature should be selected within a range of 5 to 60°C higher than the boiling point (approximately 40°C) of methylene chloride. Further, one side wall of the ultrasonic tank 1 and the other side wall of the steam tank 3 are each extended upward, and the space above each layer 1, 2, 3 surrounded by these both side walls is filled with superheated parts of the steam tank 3. Superheated steam flows from the steam region 4b,
Here, an outflow superheated steam region 4c is formed.
In this case, the temperatures in both superheated steam regions 4b and 4c are not the same, and the temperature distribution is such that the further away from the steam tank 3 toward the ultrasonic tank 1, the lower the superheated steam temperature becomes. Incidentally, a steam cooling pipe 9 is disposed at the upper part of the above-mentioned both side walls, and the superheated steam in the outflowing superheated steam region 4c is cooled by the steam cooling pipe 9, so that it is scattered upward from the position where the cooling pipe 9 is disposed. This will be prevented. Here, normal cooling methods can be used, such as supplying tap water or well water into the cooling pipe, or using a refrigerant cooled by a refrigerator if a low boiling point cleaning agent is used. can do. The solvent condensed by the cooling pipe 9 is collected into the cooling bath 2 via a water separator 10. The object to be cleaned, which has been washed in the cold bath 2 as described above, is washed and dried in the superheated steam area 4b in the steam bath 3, and in this way, the object to be cleaned is finally washed with methylene chloride. Since the cleaning is performed using superheated steam, condensation of water vapor on the surface of the object to be cleaned is prevented as much as possible after cleaning, thereby preventing the inconvenience of stains on the object to be cleaned, and reducing the loss of solvent carried out. can be reduced. Also,
In this way, not only the superheated steam region 4b is formed in the steam tank 3, but also the entire cleaning device is covered with the outflow superheated steam region 4c, so that the object to be cleaned that has been cooled to below the boiling point of the solvent can be cooled. Even when it is carried into the steam tank 3 from the bathtub 2, it is heated by the superheated steam in the outflow superheated steam region 4c, so that the superheated steam region 4b in the steam tank 3 that has been formed is not destroyed. Therefore, the superheated steam region 4b is not disturbed and a stable steam zone is maintained. Furthermore, Fig. 2 shows another example of a cleaning device used for carrying out the present invention, and this example is an example of a device that performs superheated steam cleaning after saturated steam cleaning in addition to the known saturated steam cleaning. be. That is, in this device, a saturated steam tank 11 and a superheated steam tank 3 are arranged in a state where they are communicated with each other at the lower part thereof, and a saturated steam region 4a formed in the upper part of the saturated steam tank 11 and a superheated steam tank 3 are connected to each other. A superheated steam region 4b formed above is partitioned by a partition part 12, and the saturated steam region 4a is filled with saturated vapor of the solvent 4, and the superheated steam region 4b is filled with superheated steam. Furthermore, both steam tanks 11 and 3
In the space above, an outflow superheated steam region 4c is formed by superheated steam flowing out from the superheated steam region 4b, as in the case of the apparatus shown in FIG. The apparatus shown in FIG. 2 also has a superheated steam tank 3.
Not only is a superheated steam region 4b formed within the cleaning device, but also the entire cleaning device is covered with an outflow superheated steam region 4c, so when an object to be cleaned that has been cooled to below the boiling point of methylene chloride is brought in, the outflow superheat steam area 4c
Although the temperature of the superheated steam decreases to some extent, it does not destroy the saturated steam region 4a of the saturated steam tank 11, and the superheated steam region 4b is not disturbed. Therefore, a stable superheated steam region 4b is maintained, solvent loss can be extremely suppressed, and stable cleaning can be performed. Next, an experimental example will be shown. Experimental Example 1 Using methylene chloride as a solvent, test samples washed with superheated steam and test samples washed with saturated steam using the steam tank of the apparatus shown in Figure 1 were tested to determine whether condensation occurred and whether the solvent was taken out. confirmed. The test results are shown in Table 1.
【表】
第1表の結果より、本発明の過熱蒸気洗浄法に
よれば結露や液の持ち出しがないが、飽和蒸気洗
浄法では結露や液の持ち出しがあることが知見さ
れる。
実験例 2
溶剤として塩化メチレン(沸点40℃)を使用
し、第1図に示す三槽式洗浄装置を用いて稼動中
の溶剤の消費量を本発明の過熱蒸気洗浄法と従来
の飽和蒸気洗浄法についてテストした。
結果を第2表に示す。[Table] From the results in Table 1, it is found that the superheated steam cleaning method of the present invention does not cause dew condensation or liquid take-out, but the saturated steam cleaning method causes dew condensation or liquid take-out. Experimental Example 2 Using methylene chloride (boiling point 40°C) as a solvent, the amount of solvent consumed during operation using the three-tank cleaning equipment shown in Figure 1 was compared between the superheated steam cleaning method of the present invention and the conventional saturated steam cleaning method. Tested on the law. The results are shown in Table 2.
本発明によれば、塩化メチレンを用いて熱容量
の小さい薄い被洗浄物やひだもしくは凹部の多い
被洗浄物を洗浄した場合において、その表面に水
蒸気が結露することによつて生じるシミの発生が
良好に防止されると共に、過熱蒸気ゾーンの破壊
がなく、過熱蒸気ゾーンを安定に維持することが
でき、塩化メチレンの持ち出しロスが防止され、
かつ安定した洗浄が行われるものである。
According to the present invention, when methylene chloride is used to clean a thin object with a small heat capacity or an object to be cleaned that has many folds or recesses, stains caused by water vapor condensing on the surface of the object are effectively suppressed. At the same time, there is no destruction of the superheated steam zone, the superheated steam zone can be maintained stably, and the loss of methylene chloride carried out is prevented.
In addition, stable cleaning can be performed.
第1図は本発明の実施に用いる装置の一例を示
す概略図、第2図は本発明の実施に用いる装置の
他の例を示す概略図である。
3…蒸気槽、4…溶剤、4a…飽和蒸気域、4
b…蒸気槽の過熱蒸気域、4c…流出過熱蒸気
域、7…過熱用ヒーター。
FIG. 1 is a schematic diagram showing one example of an apparatus used for carrying out the present invention, and FIG. 2 is a schematic diagram showing another example of the apparatus used for carrying out the present invention. 3... Steam tank, 4... Solvent, 4a... Saturated steam region, 4
b... Superheated steam area of the steam tank, 4c... Outflow superheated steam area, 7... Superheating heater.
Claims (1)
は凹部を有する被洗浄物を複数の洗浄槽内にそれ
ぞれ収容された塩化メチレン溶剤で順次洗浄する
に際し、最後の洗浄槽を塩化メチレン蒸気槽と
し、この蒸気槽内のメチレン蒸気域に過熱用ヒー
ターを設け、このヒーターにより塩化メチレン蒸
気をその沸点よりも5〜60℃高温に過熱して上記
蒸気槽内上部に過熱蒸気域を形成すると共に、上
記複数の洗浄槽の上方に、上記過熱蒸気域から流
出する過熱蒸気により上記複数の洗浄槽を覆つて
流出過熱蒸気域を形成し、上記被洗浄物を上記洗
浄槽内の塩化メチレンで洗浄し、最後に上記流出
過熱蒸気域を通ることにより該流出過熱蒸気域で
加熱された被洗浄物を上記塩化メチレンの沸点よ
り5〜60℃高温に過熱された蒸気槽内の過熱蒸気
域に該過熱蒸気域を破壊することなく導入し、こ
の過熱蒸気域で被洗浄物を洗浄すると共に、該過
熱蒸気温度になるまで加熱乾燥した後、被洗浄物
を取り出すことを特徴とする蒸気洗浄方法。1. When cleaning thin objects with small heat capacity or objects having folds or recesses with methylene chloride solvent contained in multiple cleaning tanks, the last cleaning tank is a methylene chloride vapor tank, and this steam A superheating heater is provided in the methylene vapor region in the tank, and this heater superheats the methylene chloride vapor to a temperature 5 to 60°C higher than its boiling point to form a superheated vapor region in the upper part of the steam tank. Above the cleaning tank, superheated steam flowing out from the superheated steam area covers the plurality of cleaning tanks to form an outflow superheated steam area, and the object to be cleaned is cleaned with methylene chloride in the cleaning tank, and finally, By passing through the outflow superheated steam area, the object to be cleaned heated in the outflow superheated steam area is transferred to the superheated steam area in the steam tank which is superheated to 5 to 60 degrees Celsius higher than the boiling point of the methylene chloride. A steam cleaning method characterized in that the object to be cleaned is introduced without being destroyed, the object to be cleaned is cleaned in this superheated steam region, and the object to be cleaned is taken out after being heated and dried to the temperature of the superheated steam.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17308484A JPS6152381A (en) | 1984-08-20 | 1984-08-20 | Vapor cleaning method and cleaning device to be used therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17308484A JPS6152381A (en) | 1984-08-20 | 1984-08-20 | Vapor cleaning method and cleaning device to be used therefor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6152381A JPS6152381A (en) | 1986-03-15 |
| JPH0448514B2 true JPH0448514B2 (en) | 1992-08-06 |
Family
ID=15953909
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17308484A Granted JPS6152381A (en) | 1984-08-20 | 1984-08-20 | Vapor cleaning method and cleaning device to be used therefor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6152381A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BR112012015327A2 (en) * | 2009-12-24 | 2015-11-03 | Aqua Doctor Co Ltd | steam sterilization apparatus |
| KR101175758B1 (en) * | 2010-03-29 | 2012-08-22 | 주식회사 두정테크 | steam removal device for heatproof-painting of silencer and thereof. |
| JP2019055896A (en) * | 2017-09-21 | 2019-04-11 | 大和特殊硝子株式会社 | Production method of glass vessel |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2624345C2 (en) * | 1975-06-02 | 1984-08-23 | Boliden Kemi AB, Helsingborg | Device for heat recovery in a degreasing device |
| JPS5570382A (en) * | 1978-11-23 | 1980-05-27 | Daikin Ind Ltd | Washing drying method and its device |
-
1984
- 1984-08-20 JP JP17308484A patent/JPS6152381A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6152381A (en) | 1986-03-15 |
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|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |