JPH064953Y2 - Cleaning equipment using organic solvent - Google Patents
Cleaning equipment using organic solventInfo
- Publication number
- JPH064953Y2 JPH064953Y2 JP5459588U JP5459588U JPH064953Y2 JP H064953 Y2 JPH064953 Y2 JP H064953Y2 JP 5459588 U JP5459588 U JP 5459588U JP 5459588 U JP5459588 U JP 5459588U JP H064953 Y2 JPH064953 Y2 JP H064953Y2
- Authority
- JP
- Japan
- Prior art keywords
- organic solvent
- cleaning tank
- vapor
- cleaning
- 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.)
- Expired - Lifetime
Links
Landscapes
- Cleaning By Liquid Or Steam (AREA)
Description
【考案の詳細な説明】 (産業上の利用分野) この考案に係る洗浄装置は、フロン等の有機溶剤を用い
て、金型、或はIC基板等、各種物品を洗浄する場合に
利用する。DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The cleaning apparatus according to the present invention is used for cleaning various articles such as a mold or an IC substrate using an organic solvent such as CFC.
(従来の技術) 各種物品に付着した汚れを落とす場合、従来からフロン
等の有機溶剤を使用した洗浄装置が使用されている。(Prior Art) In order to remove stains attached to various articles, a cleaning device using an organic solvent such as CFC has been conventionally used.
洗浄作業を行なう場合は、気密性を有する洗浄槽の内部
に被洗浄物を収納した後、真空ポンプによってこの洗浄
槽内部の空気を排出し、被洗浄物の表面に存在する細か
い凹凸や、内部に存在する微細な空隙の内部に迄有機溶
剤が進入し易い状態としてから、洗浄槽内部に洗浄用の
有機溶剤を送り込む。When performing cleaning work, after the object to be cleaned is stored inside a cleaning tank that is airtight, the air inside the cleaning tank is exhausted by a vacuum pump to remove fine irregularities or internal The organic solvent for the cleaning is fed into the cleaning tank after the organic solvent is easily allowed to enter even the inside of the minute voids existing in.
洗浄槽内部への有機溶剤の送り込み後、この有機溶剤を
超音波振動子によって加振したり、或は攪拌翼によって
攪拌し、被洗浄物の表面に付着した油等の汚れを落と
す。After feeding the organic solvent into the cleaning tank, the organic solvent is vibrated by an ultrasonic vibrator or stirred by a stirring blade to remove dirt such as oil adhering to the surface of the object to be cleaned.
一度の洗浄作業で汚れを十分に落とせない場合は、洗浄
槽内部から有機溶剤を排出した後、真空ポンプによって
洗浄槽内部の気体を排出し、再び洗浄槽内部に有機溶剤
を送り込む。When the dirt cannot be removed sufficiently by one cleaning operation, the organic solvent is discharged from the inside of the cleaning tank, the gas inside the cleaning tank is discharged by the vacuum pump, and the organic solvent is fed again into the cleaning tank.
(考案が解決しようとする課題) ところが、上述の様な従来の有機溶剤を用いる洗浄装置
に於いては、洗浄用の有機溶剤の一部が外部に漏れる事
が避けられず、周囲の環境を悪化させる場合があった。(Problems to be solved by the invention) However, in the conventional cleaning apparatus using the organic solvent as described above, it is inevitable that a part of the cleaning organic solvent leaks to the outside, and the surrounding environment is It could make it worse.
特に、洗浄用の有機溶剤として広く使用されるフロン
は、オゾン層を破壊する等、地球全体としての環境破壊
に繋る事が報告されており、周囲に漏れる事を極力低く
抑える必要がある。In particular, chlorofluorocarbon widely used as an organic solvent for cleaning has been reported to lead to environmental destruction of the entire earth such as depletion of the ozone layer, and it is necessary to suppress leakage to the surroundings as low as possible.
本考案の有機溶剤を用いる洗浄装置は、この様な問題を
解決するものである。The cleaning apparatus using the organic solvent of the present invention solves such a problem.
(課題を解決する為の手段) 本考案の有機溶剤を用いる洗浄装置は、上方が開口した
有底筒状で、上端開口と気密に塞ぐ事の出来る蓋を有す
る洗浄槽と、この洗浄槽の内部に有機溶剤の蒸気を送り
込む蒸気供給手段と、洗浄槽の内部に送り込む為の有機
溶剤を貯溜し、上部空間を有機溶剤の蒸気で満たした貯
溜槽と、この貯溜槽と洗浄槽とを結び、両槽の間で有機
溶剤の給排を行なう給排手段と、液状の有機溶剤を加熱
蒸発させる為のヒータと有機溶剤の蒸気を凝縮させる為
の冷却器とを組み合わせ、凝縮した有機溶剤を上記貯溜
槽に送る蒸留器と、途中に真空ポンプを設け、洗浄槽か
ら排出した有機溶剤蒸気を、上記蒸留器に送り込む排出
管と、途中に真空ポンプを設け、洗浄槽から空気を排出
する排気管と、洗浄槽内に空気を送り込む吸気管とから
構成されている。(Means for Solving the Problems) A cleaning device using an organic solvent of the present invention is a bottomed cylindrical shape with an open upper part, a cleaning tank having an upper end opening and a lid that can be hermetically closed, and a cleaning tank of this cleaning tank. The vapor supply means for sending the vapor of the organic solvent to the inside, the storage tank for storing the organic solvent to be fed into the cleaning tank, and the upper space filled with the vapor of the organic solvent, and this storage tank and the cleaning tank are connected. , A supply / discharge means for supplying / discharging the organic solvent between both tanks, a heater for heating and evaporating the liquid organic solvent and a cooler for condensing the vapor of the organic solvent are combined to collect the condensed organic solvent. Exhaust that discharges air from the cleaning tank by installing a distiller for sending to the storage tank and a vacuum pump in the middle, and installing an exhaust pipe for sending the organic solvent vapor discharged from the cleaning tank to the distiller and a vacuum pump in the middle A suction pipe that pumps air into the cleaning tank. It is composed of the trachea.
(作用) 上述の様に構成される本考案の有機溶剤を用いる洗浄装
置により、被洗浄物の洗浄を行なう場合、この被洗浄物
を洗浄槽内部に収納した後、洗浄槽の蓋を閉じ、排気管
の途中に設けた真空ポンプを運転して、この洗浄槽内部
の空気を排出する。(Operation) When the object to be cleaned is cleaned by the cleaning apparatus using the organic solvent of the present invention configured as described above, after storing the object to be cleaned in the cleaning tank, the lid of the cleaning tank is closed, The vacuum pump provided in the middle of the exhaust pipe is operated to discharge the air inside the cleaning tank.
洗浄槽内部の空気を排出した後、給排手段を通じて、貯
溜槽内の有機溶剤を洗浄槽内部に送り込み、被洗浄物の
洗浄を行なう。After the air in the cleaning tank is discharged, the organic solvent in the storage tank is fed into the cleaning tank through the supply / discharge means to clean the object to be cleaned.
液状の有機溶剤による洗浄作業が完了したならば、給排
手段により洗浄槽中の液状有機溶剤を、徐々に貯溜槽に
戻しつつ、蒸気供給手段から洗浄槽中に有機溶剤の蒸気
を供給する。When the cleaning work with the liquid organic solvent is completed, the liquid organic solvent in the cleaning tank is gradually returned to the storage tank by the supply / discharge means, and the vapor of the organic solvent is supplied from the vapor supply means into the cleaning tank.
この結果、洗浄槽中の被洗浄物は、その一部が液状有機
溶剤の液面上に露出し、この露出部分で有機溶剤の蒸気
が凝縮し、この凝縮分で被洗浄物の表面が洗浄される、
所謂蒸気洗浄が行なわれる。As a result, part of the object to be cleaned in the cleaning tank is exposed on the liquid surface of the liquid organic solvent, the vapor of the organic solvent is condensed at this exposed part, and the surface of the object to be cleaned is cleaned by this condensed portion. Will be
So-called steam cleaning is performed.
蒸気洗浄を行ないつつ、洗浄槽中の液状有機溶剤を総て
貯溜槽に戻したならば、排出管の途中に設けた真空ポン
プを運転し、洗浄槽内に残留している有機溶剤蒸気を蒸
留器内に排出する。この様に、排出管を通じて蒸留器に
排出された有機溶剤の蒸気は、この蒸留器に設けた冷却
器によって凝縮液化されて回収される。この際、蒸留器
内に空気が混入する事はない。真空ポンプの運転に伴っ
て、洗浄槽内が所定の真空度に達したならば、上記真空
ポンプを停止し、吸気管を通じて洗浄槽内に空気を送り
込む。When all the liquid organic solvent in the cleaning tank is returned to the storage tank while performing the steam cleaning, the vacuum pump installed in the middle of the discharge pipe is operated to distill the organic solvent vapor remaining in the cleaning tank. Discharge into the container. As described above, the vapor of the organic solvent discharged to the distiller through the discharge pipe is condensed and liquefied by the cooler provided in the distiller and collected. At this time, air is not mixed in the distiller. When the inside of the cleaning tank reaches a predetermined vacuum level with the operation of the vacuum pump, the vacuum pump is stopped and air is sent into the cleaning tank through the intake pipe.
この結果、洗浄槽内の圧力が大気圧程度に迄上昇したな
らば、この洗浄槽の蓋を開き、洗浄作業が完了した被洗
浄物の取り出しを行なう。As a result, if the pressure in the cleaning tank rises to about atmospheric pressure, the lid of the cleaning tank is opened and the object to be cleaned after cleaning is taken out.
(実施例) 次に、図示の実施例を説明しつつ、本考案を更に詳しく
説明する。(Embodiment) Next, the present invention will be described in more detail with reference to the illustrated embodiment.
第1図は本考案の有機溶剤を用いる洗浄装置の全体構成
を示している。1は、上方が開口した有底筒状の洗浄槽
で、上端開口を気密に塞ぐ事の出来る蓋2を有し、底面
には超音波振動子16、16を装着して、洗浄槽1の内
部に送り込んだ液状の有機溶剤を加振し、この有機溶剤
に浸漬された被洗浄物36の洗浄を効率良く行なえる様
にしている。FIG. 1 shows the overall structure of a cleaning apparatus using an organic solvent of the present invention. Reference numeral 1 is a bottomed cylindrical cleaning tank having an upper opening, which has a lid 2 capable of airtightly closing the upper opening, and ultrasonic vibrators 16, 16 are attached to the bottom surface of the cleaning tank 1. The liquid organic solvent sent into the interior is vibrated so that the object 36 to be cleaned immersed in the organic solvent can be efficiently cleaned.
この様な洗浄槽1に有機溶剤の蒸気を送り込む為の蒸気
供給手段は、ヒータ3を内蔵し、内部に貯溜した有機溶
剤を加熱蒸発させる為の蒸発器4と、途中に電磁弁5を
設け、両端を蒸発器4の上部と洗浄槽1の上部とにそれ
ぞれ接続した吸蒸管6とから構成されており、上記電磁
弁5の開放により、洗浄槽1の上部空間内に有機溶剤の
蒸気を送り込める様にしている。The vapor supply means for feeding the vapor of the organic solvent into the cleaning tank 1 has a heater 3 built therein, an evaporator 4 for heating and evaporating the organic solvent stored therein, and a solenoid valve 5 in the middle. , The vaporization pipe 6 having both ends connected to the upper portion of the evaporator 4 and the upper portion of the cleaning tank 1, respectively. When the solenoid valve 5 is opened, the vapor of the organic solvent is introduced into the upper space of the cleaning tank 1. I am trying to send you.
洗浄槽1の内部に送り込む為の有機溶剤を貯溜した貯溜
槽7は、上記洗浄槽1よりも高所に設けられており、こ
の貯溜槽7の底部に一端を接続し、途中に電磁弁8を設
けた給液管37の他端を洗浄槽1に接続する事で、電磁
弁8の開放に伴って、貯溜槽7内に貯溜された液状の有
機溶剤が、重力により洗浄槽1に流下する様にしてい
る。The storage tank 7 that stores the organic solvent to be fed into the cleaning tank 1 is provided at a higher place than the cleaning tank 1, and one end is connected to the bottom of the storage tank 7, and the solenoid valve 8 is provided on the way. By connecting the other end of the liquid supply pipe 37 provided with the cleaning tank 1, the liquid organic solvent stored in the storage tank 7 flows down to the cleaning tank 1 by gravity due to the opening of the solenoid valve 8. I am trying to do it.
又、上記貯溜槽7の上部に一端を接続した接続管9の他
端は、後述する蒸留器10の中間部に接続している。蒸
留器10から貯溜槽10の中間部に接続している。蒸留
器10の中間部に接続している。蒸留器10から貯溜槽
7へは、この接続管9を通じて液状の有機溶剤の他、有
機溶剤の蒸気が送り込まれ、その結果、貯溜槽7の上部
空間は、常に有機溶剤の蒸気で満たされている。Further, the other end of the connection pipe 9 having one end connected to the upper part of the storage tank 7 is connected to an intermediate part of a distiller 10 described later. The distiller 10 is connected to the middle portion of the storage tank 10. It is connected to the middle part of the distiller 10. In addition to the liquid organic solvent, the vapor of the organic solvent is sent from the distiller 10 to the storage tank 7 through the connecting pipe 9, and as a result, the upper space of the storage tank 7 is always filled with the vapor of the organic solvent. There is.
更に、洗浄槽1の底部に一端を接続し、中間部に電磁弁
13と送液ポンプ11とを設けた排液管12の他端は、
貯溜槽7に接続して、上記電磁弁13の開放と送液ポン
プ11の運転とに伴って、洗浄槽1内の液状有機溶剤を
貯溜槽7に戻せる様にしている。Furthermore, one end is connected to the bottom of the cleaning tank 1, and the other end of the drainage pipe 12 provided with the solenoid valve 13 and the liquid feed pump 11 in the middle is
It is connected to the storage tank 7 so that the liquid organic solvent in the cleaning tank 1 can be returned to the storage tank 7 when the solenoid valve 13 is opened and the liquid feed pump 11 is operated.
前記接続管9により貯溜槽7と接続された蒸留器10
は、下半の蒸発器14と上半の凝縮器15とを組み合わ
せる事で構成されている。液状の有機溶剤を貯溜出来る
様に、有底筒状に形成された蒸発器ケーシング17の底
部には、液状の有機溶剤を加熱蒸発させる為のヒータ1
8を、上端開口部を蓋22で塞いだ筒状の凝縮器ケーシ
ング19の内周面には有機溶剤の蒸気を凝縮させる為の
冷却器20を、それぞれ配設している。Distiller 10 connected to the storage tank 7 by the connecting pipe 9
Is configured by combining the lower half evaporator 14 and the upper half condenser 15. A heater 1 for heating and evaporating the liquid organic solvent is provided at the bottom of an evaporator casing 17 formed in a cylindrical shape with a bottom so that the liquid organic solvent can be stored.
A condenser 20 for condensing the vapor of the organic solvent is provided on the inner peripheral surface of a cylindrical condenser casing 19 whose upper end opening is closed by a lid 22.
上記蒸発器ケーシング17の横断面積は、凝縮器ケーシ
ング19の横断面積よりも小さくし、且つ、蒸発器ケー
シング17の上端縁を凝縮器ケーシング19の底面より
も上方に突出させて、この突出部の外側に、凝縮液受部
21を形成している。そして凝縮器ケーシング19の内
周面に配設された冷却器20は、この凝縮液受部21の
上方に位置させて、冷却器20に触れて凝縮した有機溶
剤が、凝縮液受部21に流下する様にしている。The cross-sectional area of the evaporator casing 17 is smaller than the cross-sectional area of the condenser casing 19, and the upper end edge of the evaporator casing 17 is made to project above the bottom surface of the condenser casing 19 so that A condensate receiving portion 21 is formed on the outside. The cooler 20 arranged on the inner peripheral surface of the condenser casing 19 is positioned above the condensate receiving portion 21, and the organic solvent condensed by touching the cooler 20 is transferred to the condensate receiving portion 21. I am trying to run down.
又、凝縮器ケーシング19の上端開口を塞いだ蓋22に
一端を接続し、他端を活性炭フィルタ23に接続した排
気管24の途中には、第二の冷却器25を内蔵した第二
の凝縮器26を設けている。In addition, a second condenser having a second cooler 25 built therein is provided in the middle of the exhaust pipe 24, one end of which is connected to the lid 22 that closes the upper end opening of the condenser casing 19 and the other end of which is connected to the activated carbon filter 23. A container 26 is provided.
更に、一端を前記洗浄槽1に接続し、途中に電磁弁28
と真空ポンプ27とを設けた排出管29の他端は二又に
分岐して、第一、第二の分岐管部30、31としてい
る。それぞれ、途中に電磁弁32、33を設けた両分岐
管部30、31の内、第一の分岐管部30の端部は蒸留
器10の蒸発器14に、第二の分岐管部31の端部は活
性炭フィルタ23に、それぞれ接続している。Further, one end of the solenoid valve 28 is connected to the cleaning tank 1 and
The other end of the discharge pipe 29 provided with the vacuum pump 27 is bifurcated into first and second branch pipe portions 30 and 31. Of the two branch pipe portions 30 and 31 provided with the solenoid valves 32 and 33 on the way, the end portion of the first branch pipe portion 30 is connected to the evaporator 14 of the distiller 10 and the end portion of the second branch pipe portion 31. The ends are connected to the activated carbon filter 23, respectively.
34は、洗浄槽1内に空気を送り込む吸気管で、途中に
電磁弁35を設け、一端を洗浄槽1に接続すると共に、
他端を大気に開放している。Reference numeral 34 is an intake pipe for sending air into the cleaning tank 1, and an electromagnetic valve 35 is provided on the way to connect one end to the cleaning tank 1 and
The other end is open to the atmosphere.
上述の様に構成される本考案の有機溶剤を用いる洗浄装
置により、被洗浄物36の洗浄を行なう場合、洗浄槽1
の上端に設けた蓋2を開き、この洗浄槽1内に被洗浄物
36を収納した後、洗浄槽1の蓋2を閉じてから、排気
管を兼ねる排出管29の途中に設けた電磁弁28を開く
と共に真空ポンプ27を運転して、この洗浄槽1の内部
に存在する空気を排出し、この洗浄槽1内を真空にす
る。When the object 36 to be cleaned is cleaned by the cleaning apparatus using the organic solvent of the present invention configured as described above, the cleaning tank 1
After opening the lid 2 provided at the upper end of the cleaning tank 1 to store the object to be cleaned 36 in the cleaning tank 1, the lid 2 of the cleaning tank 1 is closed, and then a solenoid valve provided in the middle of the discharge pipe 29 also serving as the exhaust pipe. 28 is opened and the vacuum pump 27 is operated to discharge the air existing inside the cleaning tank 1 to make the inside of the cleaning tank 1 a vacuum.
この際、第二の分岐管部31に設けた電磁弁33を開
き、第一の分岐管部30に設けた電磁弁32を閉じて、
洗浄槽1から吸引した気体を、活性炭フィルタ23を通
じて大気中に放散する。この為、洗浄槽1内に、先の洗
浄作業の際に使用した有機溶剤が微量残留していた場合
に於いても、この残留分は活性炭フィルタ23に吸着さ
れ、大気中に迄有機溶剤の分子が放散される事はない。At this time, the solenoid valve 33 provided in the second branch pipe portion 31 is opened, and the solenoid valve 32 provided in the first branch pipe portion 30 is closed,
The gas sucked from the cleaning tank 1 is diffused into the atmosphere through the activated carbon filter 23. Therefore, even if a small amount of the organic solvent used in the previous cleaning operation remains in the cleaning tank 1, this residue is adsorbed by the activated carbon filter 23, and the organic solvent remains in the atmosphere. The molecule is never dissipated.
洗浄槽1内部の空気を排出したならば、給排手段を構成
する給液管37の途中の電磁弁8を開き、この吸液管3
7を通じて、貯溜槽7内の有機溶剤を洗浄槽1の内部に
送り込む。この送り込みは、貯溜槽7が洗浄槽1よりも
高い場所に存在する事による重力の作用と、洗浄槽1内
が真空である事による吸引作用とにより、効率良く、迅
速に行なわれる。When the air in the cleaning tank 1 is discharged, the solenoid valve 8 in the middle of the liquid supply pipe 37 constituting the supply / discharge means is opened, and the liquid suction pipe 3
The organic solvent in the storage tank 7 is fed into the inside of the cleaning tank 1 through 7. This feeding is performed efficiently and quickly by the action of gravity due to the storage tank 7 being located at a higher position than the washing tank 1 and the suction action due to the vacuum inside the washing tank 1.
洗浄槽1内に十分量の有機溶剤の送り込みが行なわれた
ならば、洗浄槽1の底部に設けた超音波振動子16、1
6に通電する事により、この振動子16、16を振動さ
せ、上記有機溶剤を加振して、この有機溶剤に浸漬され
た被洗浄物36の洗浄を行なう。If a sufficient amount of the organic solvent is fed into the cleaning tank 1, the ultrasonic vibrators 16 and 1 provided at the bottom of the cleaning tank 1 will be described.
By energizing 6, the vibrators 16 and 16 are vibrated, the organic solvent is vibrated, and the object to be cleaned 36 immersed in the organic solvent is cleaned.
尚、洗浄槽1内に収納された被洗浄物36の洗浄を、一
層効率良く行なわせる為には、第2図に示す様に、給液
管37の先端部にシャワーノズル38を設け、洗浄槽1
内への有機溶剤の送り込み時に、この有機溶剤を被洗浄
物36に吹き付けたり、或は図示は省略したが、洗浄槽
1内に設けた攪拌翼や循環ポンプにより、洗浄槽1内の
有機溶剤を流動させる事も出来る。但し、被洗浄物36
が物理的な衝撃に弱いものである場合は、単に被洗浄物
36を有機溶剤中に浸漬するだけ(超音波による加振も
行なわない。)でも良い。In order to perform the cleaning of the object to be cleaned 36 stored in the cleaning tank 1 more efficiently, as shown in FIG. 2, a shower nozzle 38 is provided at the tip of the liquid supply pipe 37 to perform cleaning. Tank 1
When the organic solvent is fed into the cleaning tank 1, the organic solvent is sprayed onto the object to be cleaned 36, or, though not shown, the organic solvent in the cleaning tank 1 is supplied by a stirring blade or a circulation pump provided in the cleaning tank 1. Can be made to flow. However, the object to be cleaned 36
Is weak against physical impact, it is sufficient to simply immerse the article to be cleaned 36 in an organic solvent (no ultrasonic vibration is applied).
液状の有機溶剤による洗浄作業が完了したならば、給排
手段を構成する排液管12の途中に設けた送液ポンプ1
1を低速で運転する事により、洗浄槽1内の液状有機溶
剤を、徐々に貯溜槽7に戻す。これと同時に、蒸気供給
手段を構成する蒸発器4内のヒータ3に通電すると共に
給蒸管6の途中の電磁弁5を開放し、この蒸発器4から
洗浄槽1内に、比較的温度の高い有機溶剤の蒸気を供給
する。When the cleaning work with the liquid organic solvent is completed, the liquid feed pump 1 provided in the middle of the drain pipe 12 constituting the supply / discharge means.
By operating 1 at a low speed, the liquid organic solvent in the cleaning tank 1 is gradually returned to the storage tank 7. At the same time, the heater 3 in the evaporator 4 which constitutes the vapor supply means is energized and the solenoid valve 5 in the middle of the steam supply pipe 6 is opened, so that a relatively high temperature is maintained in the cleaning tank 1 from the evaporator 4. Supply high organic solvent vapors.
この結果、洗浄槽1内の被洗浄物36は、その一部が液
状有機溶剤の液面上に露出し、この露出部分で有機溶剤
の蒸気が凝縮し、この極めて洗浄な凝縮分で被洗浄物3
6の表面が仕上洗浄される、所謂蒸気洗浄が行なわれ
る。As a result, part of the object 36 to be cleaned in the cleaning tank 1 is exposed on the liquid surface of the liquid organic solvent, and the vapor of the organic solvent is condensed at this exposed part, and the extremely clean condensed portion is used for cleaning. Thing 3
The so-called steam cleaning, in which the surface of 6 is finally cleaned, is performed.
この蒸気洗浄を行なうに就いて、本考案の洗浄装置の場
合は、被洗浄物36の一部のみが液状有機溶剤の液面上
に露出し、この被洗浄物26の残部は液状有機溶剤中に
浸漬されたままの状態となる為、被洗浄物36と蒸発器
4から供給される有機溶剤蒸気との間の温度差を、蒸気
洗浄の全行程に亘って充分に保ち、被洗浄物36表面で
の有機溶剤の凝縮量を充分に確保する事が出来る。即
ち、被洗浄物36の全体を液状の有機溶剤から露出させ
て蒸気洗浄を行なった場合、被洗浄物36の温度が、有
機溶剤の凝縮に伴って上昇し、被洗浄物36の温度と有
機溶剤の蒸気の温度とに差がなくなる為、被洗浄物36
の表面での、有機溶剤蒸気の凝縮が効率良く行なわれな
くなるが、被洗浄物36の一部を液状の有機溶剤中に浸
漬したままとした場合は、被洗浄物36が液状の有機溶
剤により冷却される為、上述の様に、被洗浄物36と蒸
発器4から供給される有機溶剤蒸気との間の温度差を充
分に確保して、被洗浄物36の表面での有機溶剤の蒸気
凝縮を効率良く行なえる。In performing the vapor cleaning, in the case of the cleaning apparatus of the present invention, only a part of the object to be cleaned 36 is exposed on the liquid surface of the liquid organic solvent, and the rest of the object to be cleaned 26 is in the liquid organic solvent. Since it remains soaked in, the temperature difference between the object to be cleaned 36 and the organic solvent vapor supplied from the evaporator 4 is sufficiently maintained throughout the entire vapor cleaning process, and the object to be cleaned 36 is It is possible to secure a sufficient amount of organic solvent condensed on the surface. That is, when the entire cleaning object 36 is exposed from the liquid organic solvent and vapor cleaning is performed, the temperature of the cleaning object 36 rises as the organic solvent condenses, and Since there is no difference in the temperature of the solvent vapor,
The organic solvent vapor is not efficiently condensed on the surface of the object, but if a part of the object to be cleaned 36 is left immersed in the liquid organic solvent, the object to be cleaned 36 will be exposed to the liquid organic solvent. Since it is cooled, as described above, the temperature difference between the object to be cleaned 36 and the organic solvent vapor supplied from the evaporator 4 is sufficiently secured, and the vapor of the organic solvent on the surface of the object to be cleaned 36 is secured. It can be condensed efficiently.
尚、この様な蒸気洗浄を行なう場合に於いて、(送液ポ
ンプ11を省略し、代りに)蒸発器4から洗浄槽1内に
送り込む有機溶剤蒸気の圧力で、この洗浄槽1内の液状
有機溶剤を貯溜槽7に戻す様にし、蒸気洗浄を行なう際
の洗浄槽1内の圧力を高くすれば、有機溶剤蒸気の凝縮
温度を高くして蒸気の凝縮量を多くし、より一層蒸気洗
浄の効率を高める事が出来る。In the case of performing such vapor cleaning, the liquid in the cleaning tank 1 is liquefied by the pressure of the organic solvent vapor sent from the evaporator 4 into the cleaning tank 1 (instead of omitting the liquid feed pump 11). By returning the organic solvent to the storage tank 7 and increasing the pressure in the cleaning tank 1 at the time of performing the steam cleaning, the condensation temperature of the organic solvent vapor is increased to increase the condensation amount of the steam, and thus the steam cleaning is further performed. The efficiency of can be improved.
但し、洗浄槽1と貯溜槽7との間で有機溶剤の出し入れ
をする為の給排手段の構成は、一方向の溶剤移動を重力
により行ない、他方向への移動をポンプ或は蒸気圧力に
行なう他、両方向の移動を何れもポンプにより行なう
等、被洗浄物36の性状、装置の規模等に応じて、設計
的に定める。However, the structure of the supply / discharge means for taking in and out the organic solvent between the cleaning tank 1 and the storage tank 7 is such that the solvent is moved in one direction by gravity and the other direction is moved by a pump or vapor pressure. In addition to the movement, both movements in both directions are performed by a pump or the like, which is determined by design according to the property of the object to be cleaned 36, the scale of the apparatus, and the like.
上述の様な蒸気洗浄を行ないつつ、洗浄槽1中の液状有
機溶剤を総て貯溜槽7に戻したならば、排出管29の途
中に設けた電磁弁28を開放すると共に真空ポンプ27
を起動する。この際、第一の分岐管部30に設けた電磁
弁32を開き、第二の分岐管部31に設けた電磁弁33
を閉じて、洗浄槽1内に残留していた有機溶剤蒸気を、
蒸留器10内に排出する。When all the liquid organic solvent in the cleaning tank 1 is returned to the storage tank 7 while performing the above-described vapor cleaning, the solenoid valve 28 provided in the middle of the discharge pipe 29 is opened and the vacuum pump 27 is used.
To start. At this time, the solenoid valve 32 provided in the first branch pipe section 30 is opened, and the solenoid valve 33 provided in the second branch pipe section 31 is opened.
To close the organic solvent vapor remaining in the cleaning tank 1,
Discharge into the still 10.
この様に、排出管29、第一の分岐管部30を通じて蒸
留器10に排出された有機溶剤の蒸気は、元々この蒸留
器10内に存在していた有機溶剤の蒸気と共に、この蒸
気器10に設けた冷却器20によって凝縮液化され、凝
縮液受部21に捕集されて、接続管9を通じて貯溜槽7
に回収される。As described above, the vapor of the organic solvent discharged to the distiller 10 through the discharge pipe 29 and the first branch pipe portion 30 together with the vapor of the organic solvent originally present in the distiller 10 is the vaporizer 10 It is condensed and liquefied by the cooler 20 provided in the storage tank 7 and is collected in the condensate receiving portion 21 and is supplied to the storage tank 7 through the connecting pipe 9.
Will be collected.
真空ポンプ27の運転に伴って、洗浄槽1内が所定の真
空度に達したならば、電磁弁28を閉じ、真空ポンプ2
7を停止すると共に、それ迄閉じていた電磁弁35を開
き、吸気管34を閉じて洗浄槽1内に空気を送り込む。When the inside of the cleaning tank 1 reaches a predetermined degree of vacuum with the operation of the vacuum pump 27, the electromagnetic valve 28 is closed and the vacuum pump 2
7 is stopped, the solenoid valve 35 which was closed until then is opened, the intake pipe 34 is closed, and air is sent into the cleaning tank 1.
この結果、洗浄槽1内の圧力が上昇する為、この圧力が
大気圧程度に迄上昇したならば、洗浄槽1の蓋2を開
き、洗浄作業が完了した被洗浄物36の取り出しを行な
う。尚、蒸留器10の凝縮器15内に存在する有機溶剤
蒸気のレベル(有機溶剤蒸気の層と空気の層との境界の
高さ位置)は、排出管29、第一の分岐管部30を通じ
ての有機溶剤蒸気の送り込み、及びその停止に伴って昇
降し、この昇降量が大きいと、有機溶剤蒸気を含む気体
が排気管24から送り出され易くなるが、蒸留器10に
設けたヒータ18への通電量と、冷却器20への冷媒送
り込み量とを適当に調節する事で、上記レベルの変動を
少なくすれば、排気管24を通じての有機溶剤蒸気の排
出量を僅少に抑える事が出来る。As a result, the pressure in the cleaning tank 1 rises, and if this pressure rises to about atmospheric pressure, the lid 2 of the cleaning tank 1 is opened and the object 36 to be cleaned which has been cleaned is taken out. The level of the organic solvent vapor existing in the condenser 15 of the distiller 10 (the height of the boundary between the organic solvent vapor layer and the air layer) is measured through the discharge pipe 29 and the first branch pipe portion 30. The organic solvent vapor is sent up and down, and ascends and descends with it, and if the amount of elevation is large, the gas containing the organic solvent vapor is easily sent out from the exhaust pipe 24, but the heater 18 provided in the distiller 10 By appropriately adjusting the amount of electricity and the amount of refrigerant sent to the cooler 20, the fluctuation of the above level can be reduced, so that the discharge amount of the organic solvent vapor through the exhaust pipe 24 can be suppressed to a slight extent.
更に図示の例に於いては、排気管24の途中に、第二の
冷却器25を内蔵した第二の凝縮器26を設けると共
に、この排気管24の端部を活性炭フィルタ23に接続
する事により、排気管24を通じて排出される有機溶剤
蒸気の量の減少と、不可避的に排出される微量の有機溶
剤蒸気の処理とを図っている。Further, in the illustrated example, a second condenser 26 containing a second cooler 25 is provided in the middle of the exhaust pipe 24, and the end portion of the exhaust pipe 24 is connected to the activated carbon filter 23. Thus, the amount of the organic solvent vapor discharged through the exhaust pipe 24 is reduced and the trace amount of the organic solvent vapor unavoidably discharged is treated.
この様に、有機溶剤蒸気回収用の第二の凝縮器26を設
ける場合、第7図に示す様に、凝縮分を蒸発器14に戻
すトラップ管43と、凝縮器15から排気する排気管2
4とを独立させれば、凝縮器15からの排気と凝縮分の
還流とを、互いに干渉させる事なく、効率良く行なう事
が出来る。In this way, when the second condenser 26 for recovering the organic solvent vapor is provided, as shown in FIG. 7, the trap pipe 43 for returning the condensed component to the evaporator 14 and the exhaust pipe 2 for exhausting from the condenser 15
If 4 and 4 are independent, the exhaust from the condenser 15 and the recirculation of the condensed portion can be efficiently performed without interfering with each other.
但し、蒸留器10を密閉式にして排気管24を省略した
構造とすれば、第二の凝縮器26は不要となる。この場
合は、ヒータ18への通電量と冷却20への冷媒供給利
用とを適宜調節する事で、蒸留器10内の圧力が高くな
り過ぎたり、反対に低くなり過ぎたりするのを防止す
る。However, if the distiller 10 is hermetically sealed and the exhaust pipe 24 is omitted, the second condenser 26 is not necessary. In this case, by appropriately adjusting the amount of electricity supplied to the heater 18 and the use of the refrigerant supplied to the cooling 20, it is possible to prevent the pressure inside the distiller 10 from becoming too high, or conversely becoming too low.
又、第8図に示す様に、吸気管44と排気管24とを互
いに独立させ、吸気管44に吸気方向にのみ気体を通す
逆止弁45を、排気管24に、第二の凝縮器26と、排
気方向にのみ気体を通す逆止弁46とを設ける事も出来
る。Further, as shown in FIG. 8, a check valve 45, which separates the intake pipe 44 and the exhaust pipe 24 from each other and allows gas to pass through the intake pipe 44 only in the intake direction, is provided in the exhaust pipe 24 with a second condenser. 26 and a check valve 46 that allows gas to pass only in the exhaust direction can be provided.
尚、貯溜層7と蒸留器10とは、第1図に示す様に、互
いに独立して設けても良いが、第3図に示す様に、蒸留
器10の蒸発器ケーシング17の上部と、貯溜層7の上
部とを互いに連通させて形成しても良く、更には第4図
に示す様に、複数個の貯溜層7、7を互いに直列に配置
し、最も下流側の貯溜層7と洗浄槽1とを給液管37
(第1図参照)で接続しても良い。The storage layer 7 and the distiller 10 may be provided independently of each other as shown in FIG. 1, but as shown in FIG. 3, the upper part of the evaporator casing 17 of the distiller 10 and The upper part of the storage layer 7 may be formed so as to communicate with each other. Further, as shown in FIG. 4, a plurality of storage layers 7, 7 are arranged in series with each other, and the storage layer 7 on the most downstream side is The cleaning tank 1 and the liquid supply pipe 37
(See FIG. 1).
又、貯溜槽7の上部空間を有機溶剤の蒸気で満たす為の
手段としては、第1図に示す様に、蒸留器10の蒸発器
14の上部空間と貯溜槽7の上部空間とを接続管9で連
通させる他、第5図に示す様に、別途設けた蒸気発生器
40(洗浄槽1に蒸気を供給する為の蒸発器4と兼用さ
せる事も出来る。)により、貯溜槽7の上部空間に有機
溶剤の蒸気を供給する事も出来る。但し、前記第3図に
示した構造の場合、特に手段を講じなくても、貯溜槽7
の上部空間を有機溶剤の蒸気で満たす事が出来る。Further, as means for filling the upper space of the storage tank 7 with the vapor of the organic solvent, as shown in FIG. 1, the upper space of the evaporator 14 of the distiller 10 and the upper space of the storage tank 7 are connected by a connecting pipe. In addition to communicating with 9, the vapor generator 40 (which can also be used as the evaporator 4 for supplying the vapor to the cleaning tank 1) provided separately as shown in FIG. It is also possible to supply the organic solvent vapor to the space. However, in the case of the structure shown in FIG. 3, there is no need to take any special measures.
The upper space of the can be filled with organic solvent vapor.
又、洗浄槽1の上部空間に有機溶剤の蒸気を供給する為
の手段は、第1図に示した様に、別途蒸発器4を設けた
他、第6図に示す様に、蒸留器10の蒸発器14の上部
空間と洗浄槽1の上部空間とを、途中に電磁弁41を設
けた管42により連通する事でも構成出来る。The means for supplying the vapor of the organic solvent to the upper space of the cleaning tank 1 is provided with a separate evaporator 4 as shown in FIG. 1 and a distiller 10 as shown in FIG. The upper space of the evaporator 14 and the upper space of the cleaning tank 1 may be connected by a pipe 42 provided with a solenoid valve 41 on the way.
又、第1図に示した実施例の場合、洗浄槽1内の空気を
排出する為の真空ポンプと、洗浄槽1内の有機溶剤蒸気
を排出する為の真空ポンプとを、1個の真空ポンプ27
で兼用し、この真空ポンプ27の吐出側配管を第一、第
二の分岐管部30、31に二分しているが、空気排出用
の真空ポンプと有機溶剤蒸気排出用の真空ポンプとは別
途設け、両真空ポンプの配管を互いに独立させても良
い。In the case of the embodiment shown in FIG. 1, a vacuum pump for discharging the air in the cleaning tank 1 and a vacuum pump for discharging the organic solvent vapor in the cleaning tank 1 are combined into one vacuum. Pump 27
The discharge side pipe of the vacuum pump 27 is divided into the first and second branch pipe portions 30 and 31, but the air discharge vacuum pump and the organic solvent vapor discharge vacuum pump are separately provided. The vacuum pumps may be provided and the pipes of both vacuum pumps may be independent of each other.
又、蒸留器10を構成する蒸発器14と凝縮器15と
は、第1図に示す様に、凝縮器15を蒸発器14よりも
大径とし、凝縮器15を蒸発器14の上方に連設した
り、或は第9図に示す様に、凝縮器15を蒸発器14よ
りも小径として、凝縮器15を蒸発器14の上部に内蔵
したり、更には、第10図に示す様に、蒸発器14と凝
縮器15とを互いに独立して構成しても良い。Further, as shown in FIG. 1, the evaporator 14 and the condenser 15 constituting the distiller 10 have a diameter larger than that of the evaporator 14, and the condenser 15 is connected above the evaporator 14. Alternatively, as shown in FIG. 9, the condenser 15 may have a smaller diameter than the evaporator 14, and the condenser 15 may be built in the upper portion of the evaporator 14. Further, as shown in FIG. The evaporator 14 and the condenser 15 may be configured independently of each other.
更に、第1図に鎖線で示したように、貯溜槽7と蒸留
器10とを傾斜管47で連結しておけば、貯溜槽7内の
液状有機溶剤が一定量を越すに従って、これを蒸留器1
0の蒸発器14へ溢流させ、洗浄作業の繰り返しにより
汚れた有機溶剤を蒸溜し浄化することができる。Further, as shown by the chain line in FIG. 1, if the storage tank 7 and the distiller 10 are connected by an inclined pipe 47, as the liquid organic solvent in the storage tank 7 exceeds a certain amount, this is distilled. Bowl 1
It is possible to distill the organic solvent contaminated by repeating the washing operation by overflowing it to the evaporator 14 of 0 and purifying it.
(考案の効果) 本考案の有機溶剤を用いる洗浄装置は、以上に述べた通
り構成され作用する為、有機溶剤を、その蒸気を含めて
外部に漏らす事なく、被洗浄物の洗浄を行なう事が可能
となり、周囲の環境を保護する効果が大きい。(Effect of the Invention) Since the cleaning apparatus using the organic solvent of the present invention is configured and operates as described above, it is possible to clean the object to be cleaned without leaking the organic solvent including its vapor to the outside. This makes it possible to protect the surrounding environment.
第1図は本考案の有機溶剤を用いる洗浄装置の全体構成
を示す略縦断面図、第2図は洗浄槽の別例を示す略縦断
面図、第3〜4図は貯溜槽と蒸留器との構造の2例を示
すそれぞれ略縦断面図、第5図は貯溜槽への蒸気供給手
段を示す略縦断面図、第6図は洗浄槽への蒸気供給手段
の別例を示す略縦断面図、第7〜8図は蒸留器の上部空
間での気体給排機構の2例を示すそれぞれ略縦断面図、
第9〜10図は蒸留器の別の2例を示すそれぞれ略縦断
面図である。 1:洗浄槽、2:蓋、3:ヒータ、4:蒸発器、5:電
磁弁、6:給蒸管、7:貯溜槽、8:電磁弁、9:接続
管、10:蒸留器、11:送液ポンプ、12:排液管、
13:電磁弁、14:蒸発器、15:凝縮器、16:超
音波振動子、17:蒸発器ケーシング、18:ヒータ、
19:凝縮器ケーシング、20:冷却器、21:凝縮液
受部、22:蓋、23:活性炭フィルタ、24:排気
管、25:第二の冷却器、26:第二の凝縮器、27:
真空ポンプ、28:電磁弁、29:排出管、30:第一
の分岐管部、31:第二の分岐管部、32、33:電磁
弁、34:吸気管、35:電磁弁、36:被洗浄物、3
7:給液管、38:シャワーノズル、40:蒸気発生
器、41:電磁弁、42:管、43:トラップ管、4
4:吸気管、45、46:逆止弁、47:傾斜管。FIG. 1 is a schematic vertical sectional view showing the whole constitution of a cleaning apparatus using an organic solvent of the present invention, FIG. 2 is a schematic vertical sectional view showing another example of a cleaning tank, and FIGS. 3 to 4 are a storage tank and a distiller. And FIG. 5 is a schematic vertical sectional view showing a steam supplying means to the storage tank, and FIG. 6 is a schematic vertical sectional view showing another example of the steam supplying means to the cleaning tank. FIGS. 7 and 8 are schematic vertical cross-sectional views showing two examples of gas supply and discharge mechanism in the upper space of the still,
9 to 10 are respectively schematic vertical sectional views showing another two examples of the still. 1: Washing tank, 2: Lid, 3: Heater, 4: Evaporator, 5: Solenoid valve, 6: Steam supply pipe, 7: Storage tank, 8: Solenoid valve, 9: Connection pipe, 10: Distiller, 11 : Liquid delivery pump, 12: Drainage pipe,
13: solenoid valve, 14: evaporator, 15: condenser, 16: ultrasonic transducer, 17: evaporator casing, 18: heater,
19: Condenser casing, 20: Cooler, 21: Condensate receiving part, 22: Lid, 23: Activated carbon filter, 24: Exhaust pipe, 25: Second cooler, 26: Second condenser, 27:
Vacuum pump, 28: solenoid valve, 29: exhaust pipe, 30: first branch pipe part, 31: second branch pipe part, 32, 33: solenoid valve, 34: intake pipe, 35: solenoid valve, 36: Items to be cleaned, 3
7: liquid supply pipe, 38: shower nozzle, 40: steam generator, 41: solenoid valve, 42: pipe, 43: trap pipe, 4
4: intake pipe, 45, 46: check valve, 47: inclined pipe.
Claims (1)
密に塞ぐ事の出来る蓋を有し、大気との連通及び遮断を
制御される洗浄槽と、この洗浄槽の内部に有機溶剤の蒸
気を送り込む蒸気供給手段と、洗浄槽の内部に送り込む
溜の有機溶剤を貯溜し、上部空間を有機溶剤の蒸気で満
たした貯溜槽と、この貯溜為と洗浄槽とを結び、両槽の
間で有機溶剤の給排を行なう給排手段と、液状の有機溶
剤を加熱蒸発させる為のヒータと有機溶剤の蒸気を凝縮
させる為の冷却器とを組み合わせ、凝縮した有機溶剤を
上記貯溜槽に送ると共に、蓋により密閉されたケーシン
グ内を、第二の凝縮器を通る排気管により活性炭フィル
タを経て大気に通じさせた蒸留器と、途中に真空ポンプ
を設け、洗浄槽から排出した有機溶剤蒸気を上記蒸留器
に送り込む排出管と、途中に真空ポンプを設け、洗浄槽
内の空気を活性炭フィルタを通して排出する排気管とか
ら成る、有機溶剤を用いる洗浄装置。1. A cleaning tank having a bottomed cylindrical shape having an opening at the top and a lid capable of airtightly closing the upper opening, and controlling the communication and interruption with the atmosphere, and an organic material inside the cleaning tank. A vapor supply means for feeding solvent vapor and a reservoir tank for storing the organic solvent in the reservoir fed into the cleaning tank and filling the upper space with the vapor of the organic solvent, and connecting this reservoir with the cleaning tank. A supply / discharge means for supplying / discharging the organic solvent between them, a heater for heating and evaporating the liquid organic solvent, and a cooler for condensing the vapor of the organic solvent are combined, and the condensed organic solvent is stored in the storage tank. The organic solvent discharged from the cleaning tank was installed in the casing sealed with a lid, and a distiller was introduced into the atmosphere through an activated carbon filter through an exhaust pipe passing through the second condenser, and a vacuum pump was installed on the way. Discharge pipe for sending steam to the above distiller , The middle vacuum pump provided in the air in the cleaning tank made of an exhaust pipe for discharging through the activated charcoal filter, cleaning apparatus using organic solvents.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5459588U JPH064953Y2 (en) | 1988-04-25 | 1988-04-25 | Cleaning equipment using organic solvent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5459588U JPH064953Y2 (en) | 1988-04-25 | 1988-04-25 | Cleaning equipment using organic solvent |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01163486U JPH01163486U (en) | 1989-11-14 |
JPH064953Y2 true JPH064953Y2 (en) | 1994-02-09 |
Family
ID=31280517
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5459588U Expired - Lifetime JPH064953Y2 (en) | 1988-04-25 | 1988-04-25 | Cleaning equipment using organic solvent |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH064953Y2 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03243207A (en) * | 1990-02-19 | 1991-10-30 | Toshiba Corp | Device for controlling meandering of rolled stock |
AU639160B2 (en) * | 1991-09-23 | 1993-07-15 | Wooltech Limited | Animal fibre processing |
DE4138400C1 (en) * | 1991-11-22 | 1993-02-18 | Aichelin Gmbh, 7015 Korntal-Muenchingen, De | |
JP3032938B2 (en) * | 1994-09-07 | 2000-04-17 | 株式会社三社電機製作所 | Vacuum cleaning and drying equipment |
JP2001123285A (en) * | 1999-10-28 | 2001-05-08 | Hisaka Works Ltd | Non-through hole cleaning method and apparatus |
JP4083436B2 (en) * | 2002-02-01 | 2008-04-30 | 株式会社日阪製作所 | Steam cleaning method and apparatus |
-
1988
- 1988-04-25 JP JP5459588U patent/JPH064953Y2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH01163486U (en) | 1989-11-14 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR970007621B1 (en) | Cleaning method and apparatus using organic solvent | |
JPH064953Y2 (en) | Cleaning equipment using organic solvent | |
TW200846095A (en) | Cleaning and drying device | |
KR101978690B1 (en) | Vacuum Degreaser | |
JPH0615239A (en) | Method for vacuum washing and drying and equipment therefor | |
JP2636319B2 (en) | Recovery method of organic solvent vapor in cleaning equipment using organic solvent | |
JPS62502107A (en) | Means for restoring initial cleanliness conditions in quartz tubes used as reaction chambers for integrated circuit manufacturing | |
JPH064954Y2 (en) | Cleaning equipment using organic solvent | |
WO2003006184A1 (en) | Washing device and washing method | |
JPH1071370A (en) | Completely hermetic washing apparatus | |
KR100555836B1 (en) | Test piece automatic cleaning device | |
CA2019578C (en) | Cleaning method and system using a solvent | |
JPH0326383A (en) | Cleaning device using organic solvent | |
JP6526858B2 (en) | Cleaning solution distillation regenerating apparatus, parts cleaning apparatus, and method for regenerating distillation of cleaning solution | |
JP3448009B2 (en) | Cleaning equipment | |
JPH03293072A (en) | Operation method for washing equipment with organic solvent utilized therefor | |
CN115007523B (en) | Gasified cleaning liquid recovery device | |
JPH07166385A (en) | Vacuum degreasing and washing equipment | |
JPH0389984A (en) | Method for operating washing apparatus using organic solvent | |
JP2010240606A (en) | Sealed washing apparatus | |
JP2834794B2 (en) | Cleaning equipment using organic solvents | |
JP6927827B2 (en) | Cleaning equipment | |
JP2771846B2 (en) | Operating method of cleaning device using organic solvent | |
JPH075841Y2 (en) | Solvent reclaiming and recovering device using organic solvent | |
JPH1157637A (en) | Cleaning device |