JPS59166201A - Distillation equipment for solvent cleaning apparatus - Google Patents

Distillation equipment for solvent cleaning apparatus

Info

Publication number
JPS59166201A
JPS59166201A JP3905283A JP3905283A JPS59166201A JP S59166201 A JPS59166201 A JP S59166201A JP 3905283 A JP3905283 A JP 3905283A JP 3905283 A JP3905283 A JP 3905283A JP S59166201 A JPS59166201 A JP S59166201A
Authority
JP
Japan
Prior art keywords
solvent
vapor
distiller
distilled
generating surface
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.)
Pending
Application number
JP3905283A
Other languages
Japanese (ja)
Inventor
Atsusuke Sakaida
敦資 坂井田
Tadahiko Shibata
柴田 忠彦
Masanori Suzuki
鈴木 正徳
Tetsuo Yagi
屋宜 哲雄
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.)
Denso Corp
Original Assignee
NipponDenso Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by NipponDenso Co Ltd filed Critical NipponDenso Co Ltd
Priority to JP3905283A priority Critical patent/JPS59166201A/en
Publication of JPS59166201A publication Critical patent/JPS59166201A/en
Pending legal-status Critical Current

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  • Cleaning By Liquid Or Steam (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

PURPOSE:To increase the distillation amt. and to reduce the cost of solvent by providing a scraper for scraping vapor foam formed on a vapor generating surface in contact with the vapor generating surface and movably relatively to the vapor generating surface. CONSTITUTION:The solvent to be distilled from a hot bath is introduced into a rotary disk 9 from an intake 13 for a solvent to be distilled through an introducing pipe 8a, and spread from the central part to the circumferential part by centrifugal force due to rotation to form a thin film. The solvent is evaporated by heating the rotary disk with an electric heater 9a. The vapor, passing through vapor discharge ports 14 is cooled in a cooling coil 15, condensed and discharged from a discharge pipe 8b. The concentrated liquid is taken out from a discharge valve 16. The vapor foam 19 generated at the bottom of the rotary disk 9 is forcibly scraped off by chains 18 to be made into solvent vapor.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、溶剤洗浄装置において被洗浄物にょって汚染
された溶剤を蒸留して溶剤洗浄装置内の溶剤を清浄に維
持する蒸留器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a distiller that maintains the solvent in the solvent cleaning device clean by distilling the solvent contaminated by the object to be cleaned in the solvent cleaning device. be.

従来技術 溶剤洗浄装置は、油で汚染された精密機器類(例えばI
C,電子機器、液晶パネル、ポンプ等)をフロン・トリ
クレン等、の洗浄用溶剤中に浸漬するなどして油を除き
洗浄する装置であって、その構造は第1図に示すように
、洗浄装置本体1と蒸留器2とより成り、洗浄装置本体
1内は温浴槽3、冷却槽4、ベーパ一槽5の3槽より構
成されている。被洗浄物(ワーク)は温浴槽3から冷却
槽4へさらにペーパ一槽5へと浸漬して洗浄され、乾燥
して取り出される、温浴槽3内はワークが持ち込む油等
の異物により最も汚れる為、温浴槽3内の溶剤を蒸留器
2に導き、ヒータ6により加熱し溶剤を蒸発して冷却蛇
管7で凝縮し、蒸留した溶剤を冷却槽4に戻す回路とな
っている。このような構成の洗浄装置を運転すると、蒸
留器2内の溶剤液中の油等の異物が時間と共に増大し、
蒸留器2内の溶剤液中の油等の異物濃度が上昇して、溶
側表面に油等が浮きヒータ6表面で蒸発した溶存ヒ蒸側
か油表面で破裂し溶剤蒸発時に油等も一緒に飛散するい
わゆる飛沫同伴が生じる。これを1つの具体例を挙げて
説明すると、蒸留オ÷2中の油濃度が40〜50%にな
ると、蒸留溶剤の油減町は10■/lから40mq/I
Jへと急に悪化し洗浄装置本、体1内の溶剤清浄度も悪
くなV溶剤更新が必要となる。従って更新時には溶剤費
が多く必要になるという問題があった〇 発明の目的 本発明は上記の従来技術の問題点を解決するためになさ
れたものであって、溶剤洗浄装置の蒸留器において、蒸
留すべき溶剤中の油等の異物の濃度が高くなっても、蒸
留溶剤の品質を長く一定に保持できるよう蒸留量を増加
せしめ、溶剤の更新のための時間的間隔を大幅に延長1
〜、溶剤費を低減することのできる溶剤洗浄装置におけ
る蒸留器を提供することにある。
Prior art solvent cleaning equipment has been used to clean oil-contaminated precision equipment (e.g.
This is a device that removes oil and cleans electronic equipment, liquid crystal panels, pumps, etc.) by immersing them in cleaning solvents such as Freon and Triclean, and its structure is shown in Figure 1. It consists of an apparatus main body 1 and a distiller 2, and the inside of the cleaning apparatus main body 1 is composed of three tanks: a hot tub 3, a cooling tank 4, and a vapor tank 5. The object to be cleaned (workpiece) is immersed from the hot tub 3 into the cooling tank 4 and further into the paper tank 5, where it is washed, dried, and taken out.The interior of the hot tub 3 is most contaminated by foreign substances such as oil brought in by the workpiece. This circuit leads the solvent in the hot tub 3 to the distiller 2, heats it with the heater 6, evaporates the solvent, condenses it in the cooling corrugated pipe 7, and returns the distilled solvent to the cooling tank 4. When a cleaning device with such a configuration is operated, foreign substances such as oil in the solvent solution in the distiller 2 increase over time.
The concentration of foreign substances such as oil in the solvent solution in the distiller 2 increases, and the oil floats on the surface of the solution side and evaporates on the surface of the heater 6.The dissolved fumes evaporate on the oil surface, and when the solvent evaporates, the oil and other substances are taken with it. So-called droplet entrainment occurs. To explain this using one specific example, when the oil concentration in the distilled oil ÷ 2 becomes 40 to 50%, the oil reduction rate of the distilled solvent will decrease from 10 mq/l to 40 mq/l.
The cleanliness of the cleaning equipment and the solvent inside the body 1 deteriorated suddenly to J, and the solvent cleanliness inside the body 1 deteriorated, requiring replacement of the V solvent. Therefore, there was a problem in that a large amount of solvent was required at the time of renewal.Object of the InventionThe present invention was made to solve the above-mentioned problems of the prior art. Even if the concentration of foreign substances such as oil in the solvent increases, the amount of distillation can be increased to keep the quality of the distilled solvent constant for a long time, and the time interval for renewing the solvent can be significantly extended1.
An object of the present invention is to provide a distiller in a solvent cleaning device that can reduce solvent costs.

発明の構成 本発明は上記の目的を達成するため、その構成として、
洗浄溶剤を蒸留する蒸留器本体内の、洗浄溶剤の蒸気発
生面に接し2てこの蒸気発生面に生じる蒸り気泡の掻き
取り具を設けるとともに、この掻き取り具と蒸気発生面
とを相対移動可能としたことを特徴とするものである。
Composition of the Invention In order to achieve the above object, the present invention has the following composition:
A device for scraping steam bubbles generated on the steam generation surface of the cleaning solvent in contact with the steam generation surface of the cleaning solvent in the distiller body for distilling the cleaning solvent is provided, and the scraping tool and the steam generation surface are moved relative to each other. It is characterized by the fact that it is possible.

実施例 本発明の実施例を図面を参照して説明する。第2図及び
第3図は本発明の第1の実施例を示し、■1中8rよ蒸
留器本体で、図示し7ていない温浴槽からの被蒸留溶剤
を導入する導入配管8aと、蒸留後の溶剤を図示してい
ない冷却槽に排出する排出間W8 bとが接続されてい
る。9は断面コの字形をjた溶剤蒸発用の回転ディスク
で、この回転ディスク9の底部には溶剤加熱用の電熱ヒ
ータ9aが取り付けられている。そしてこの回転ディス
ク9は多段に、例えば3段に配役し7各デイスク9は共
通の回転シャフトlOに水平に固定され、この回転シャ
フト10はプーリー11を介してモータ12で回転が与
えられる。、13は被蒸留溶剤を回転ディスク9に導く
被蒸留溶剤取り入れ口で、各ディスク9の子方に配役さ
れたトレイ13aの中央部に開口している。]4け回転
ディスク9上で蒸発り、た溶剤Mりを一ヒ方に導く溶剤
蒸気放出口で、各トレイ13aの周辺部にその付値を左
右父互にずらせてジグザグ状に配し固定されている。1
5け蒸留器本体8の上部に固定されている冷却軸、管で
、回転ディスク9で蒸発した溶剤蒸気を凝縮させるもの
である。16は蒸留器本体8の喝部に設けた排出用バル
ブで、本体8の底部に凝縮され貯留し7た油等の異物を
排出するためのものである。
Embodiment An embodiment of the present invention will be described with reference to the drawings. Figures 2 and 3 show a first embodiment of the present invention; (1) 8r is the distiller main body; A discharge port W8b is connected to discharge the subsequent solvent to a cooling tank (not shown). Reference numeral 9 denotes a rotating disk with a U-shaped cross section for evaporating the solvent, and an electric heater 9a for heating the solvent is attached to the bottom of the rotating disk 9. The rotating disks 9 are arranged in multiple stages, for example, in three stages, and each disk 9 is horizontally fixed to a common rotating shaft 10, and this rotating shaft 10 is rotated by a motor 12 via a pulley 11. , 13 is a distillate solvent inlet for guiding the distillate solvent to the rotating disks 9, and is opened in the center of a tray 13a arranged on the side of each disk 9. ] Solvent vapor discharge ports that evaporate on the four rotating disks 9 and guide the solvent to one side are arranged and fixed in a zigzag pattern around the periphery of each tray 13a with their assigned values being shifted from left to right. has been done. 1
A cooling shaft and tube fixed to the upper part of the 5-box distiller main body 8 condense the solvent vapor evaporated on the rotating disk 9. Reference numeral 16 denotes a discharge valve provided at the bottom of the distiller main body 8, and is for discharging foreign substances such as oil condensed and stored at the bottom of the main body 8.

17は本体8の底部に設けられた油等の異物を収容する
濃縮槽であり、17a&′iこの濃縮槽17内に設置し
7た電熱ヒータで濃縮槽内の被蒸留溶媒をさらに濃縮(
80〜90%)するとともに、濃縮された油等の異物が
固化しないためのも′のである。
Reference numeral 17 is a concentrating tank provided at the bottom of the main body 8 to accommodate foreign substances such as oil, and the electric heater 7 installed in this concentrating tank 17 further condenses the solvent to be distilled in the concentrating tank (
80 to 90%), and also to prevent foreign substances such as concentrated oil from solidifying.

18は前記回転ディスク9の底面に発生り、た蒸気気泡
を強制的に掻き取るチェーンで、トレイ13 lI(’
)F面にtll下してあり、回転ディスク9の底面に接
触するよう設置する(第3図)、19は溶剤蒸気気泡で
、前記回転ディスク9底部表面に発生するものである。
18 is a chain for forcibly scraping off steam bubbles generated on the bottom surface of the rotating disk 9,
) The solvent vapor bubbles 19 are located on the bottom surface of the rotary disk 9 and are installed so as to be in contact with the bottom surface of the rotary disk 9 (FIG. 3).

上記の構成よりなる本実施例の作動は次のとおりである
The operation of this embodiment having the above configuration is as follows.

モータ12を駆動[7てプーリー11及び回転シャフト
10を介して回転ディスク9を回転させ、一方温浴槽(
図示しない)からの被蒸留溶剤を導入配管8aを経て被
蒸留溶剤取り入れ口13がら回転ディスク9内に導入す
る。この際の被蒸留溶剤の供給は1個の回転ディスク9
では蒸発しきれない過剰の量を導入するものとし、第1
段の回転ディスク9で蒸発しきれ−ない被蒸留溶剤が溢
れて次の第2段の回転ディスク9へ流入し、以下同様に
して順次下段の回転ディスク9へ流入するようにする。
The motor 12 is driven [7 to rotate the rotating disc 9 via the pulley 11 and the rotating shaft 10, while the hot tub (
A solvent to be distilled from a solvent (not shown) is introduced into the rotating disk 9 through an inlet 13 for the solvent to be distilled through an introduction pipe 8a. At this time, the solvent to be distilled is supplied by one rotating disk 9.
In this case, an excess amount that cannot be evaporated is introduced, and the first
The solvent to be distilled that has not been completely evaporated on the rotating disk 9 of the stage overflows and flows into the rotating disk 9 of the next second stage, and in the same way, it sequentially flows into the rotating disk 9 of the lower stage.

第1段の回転ディスク9に導入された被蒸留溶剤は回転
ディスク9の回転に伴う遠心力によりその中心部から周
辺部へと拡がり薄膜が形成され、電熱ヒータ9ILによ
り回転ディスク9は加熱されているため、ディスク9の
表面で蒸発が始まり溶剤蒸気となる。この時回転ディス
ク9の底部で発生した蒸気気泡19は、チェーン18に
衝突してこれにより強制的に掻き取られ溶剤蒸気となる
The solvent to be distilled introduced into the first-stage rotating disk 9 spreads from the center to the periphery due to centrifugal force as the rotating disk 9 rotates, forming a thin film, and the rotating disk 9 is heated by the electric heater 9IL. As a result, evaporation begins on the surface of the disk 9 and becomes solvent vapor. At this time, the steam bubbles 19 generated at the bottom of the rotating disk 9 collide with the chain 18 and are forcibly scraped off thereby, turning into solvent vapor.

第2図の実線矢印に示すように、第1段目の回転ディス
ク9上で蒸発せず溢・れた被蒸留溶剤は第2段目の被蒸
留用剤取り入れ口13から第2段目の回転ディスク9に
導入される。此処でまた蒸発し蒸発しなかった被蒸留溶
剤は同様にして第3段目の回転ディスク9に導入される
。このようにして回転ディスク9上で蒸発しきれずに溢
れた被蒸留溶剤は順次下段の回転ディスク9に流入し、
第1段目、第2段目、第3段目の各回転ディスク9内の
油等の濃度は下段に行くに従って上昇し、蒸留器本体8
底部すなわち濃縮?1J17内の溶剤中の油等の濃度が
最も高くなる。
As shown by the solid line arrow in FIG. It is introduced into the rotating disk 9. Here, the solvent to be distilled is again evaporated and the unevaporated solvent is introduced into the third stage rotating disk 9 in the same manner. In this way, the solvent to be distilled that has not been completely evaporated on the rotating disk 9 and overflows sequentially flows into the lower rotating disk 9,
The concentration of oil, etc. in each of the rotating disks 9 in the first, second, and third stages increases toward the bottom, and the distiller main body 8
Bottom i.e. concentration? The concentration of oil, etc. in the solvent in 1J17 is the highest.

一方回転ディスク9において蒸発し7た被蒸留溶剤蒸気
は第2図の破線矢印に示すように、溶剤蒸気放出口14
を介して上方へ移動し、冷却蛇管15内で冷却され凝縮
して排出配管8bを経て冷浴槽(図示しない)へ供給さ
れる。
On the other hand, the solvent vapor to be distilled that has evaporated on the rotating disk 9 is transferred to the solvent vapor outlet 14 as shown by the broken line arrow in FIG.
The liquid then moves upward through the cooling tube 15, is cooled and condensed, and is supplied to the cooling bath (not shown) via the discharge pipe 8b.

ところで回転ディスク9の底部に発生り、た溶剤蒸気気
泡19はフロン蒸気気泡膜を形成し、電熱ヒータ9aよ
りの熱伝導を妨げ、その結果、総括伝熱係数はこのフロ
ン蒸気気泡臥により支配されてし7まうことになる。例
えばフロン蒸気の熱伝導度は0.0046 Km/m−
h・℃と非宮に小さい。しかし本実施例によれば、第3
図に示されているように設備コストの安価なチェーン1
8により強制的にフロン蒸気気泡19を掻き取V総括伝
熱係数を大きくシ、その結果、第4図に示すように蒸留
量をチェーンを設けていない場合に比して10%アップ
することができた。
By the way, the solvent vapor bubbles 19 generated at the bottom of the rotating disk 9 form a fluorocarbon vapor bubble film and impede heat conduction from the electric heater 9a.As a result, the overall heat transfer coefficient is dominated by the fluorocarbon vapor bubbles. It will take 7 days. For example, the thermal conductivity of fluorocarbon vapor is 0.0046 Km/m-
H・℃ is extremely small. However, according to this embodiment, the third
Chain 1 with low equipment cost as shown in the figure
8 forcibly scrapes off the fluorocarbon vapor bubbles 19 and greatly increases the overall heat transfer coefficient. As a result, as shown in Fig. 4, the distillation amount can be increased by 10% compared to the case without the chain. did it.

なお、蒸気気泡を掻き取る手段として本実施例では吊下
チェーンを用いたが、この他に回転ディスク9の底面に
沿いかつ溶剤に対し抵抗の小さい例えば細い丸棒、テフ
ロン等の板材のような掻き■り具を用いてもよい。
Although a hanging chain was used in this embodiment as a means for scraping off steam bubbles, other means such as a thin round bar or a plate made of Teflon or the like that runs along the bottom surface of the rotating disk 9 and has low resistance to solvents may be used as a means for scraping off steam bubbles. A scraping tool may also be used.

本実施例によれば、従来装置のように被蒸留溶剤である
温浴槽液を濃縮槽17内の濃縮液中に直接流入させない
為に、蒸留本体8底部の油濃度が80%になっても蒸留
液中の油#度が10 mg / l以下の高清浄度の蒸
留液が借られた。従って従来の装置では油濃度が、40
〜50%になると洗浄装置内の溶剤更新が必要であった
のに対し7、本実施例では蒸留器本体8底部の油濃度が
80%でも溶剤更新が不必要で、濃縮液を排出バルブ1
6から抜く必要があるだけであり、溶剤費を大幅に低減
できた。
According to this embodiment, since the hot bath liquid, which is the solvent to be distilled, is not directly flowed into the concentrated liquid in the concentrating tank 17 as in the conventional apparatus, even if the oil concentration at the bottom of the distillation main body 8 reaches 80%, A highly clean distillate with an oil content of 10 mg/l or less was borrowed. Therefore, in the conventional equipment, the oil concentration is 40
While it was necessary to replace the solvent in the cleaning device when the concentration reached ~50%7, in this example, even if the oil concentration at the bottom of the distiller main body 8 was 80%, there was no need to replace the solvent, and the concentrated liquid was removed from the discharge valve 1.
It was only necessary to remove it from 6, and the cost of solvent could be reduced significantly.

本実施例ではまた特に回転ディスク9によって被蒸留用
溶剤に遠心力を寿える為、ディスク9上で溶剤が流動し
て境膜jvさを小さくし熱伝導率を上げることができ、
従来装置に比較して蒸留1:を増加させることもできる
In this embodiment, the rotating disk 9 applies centrifugal force to the solvent to be distilled, so the solvent flows on the disk 9, reducing the thickness of the film and increasing the thermal conductivity.
It is also possible to increase the distillation 1: compared to conventional equipment.

これにさらに回転ディスク9の枚数(段数)を増しfr
−t)回転ディスク9の回転数を増やしたりすれば蒸留
量を容易に増大することができる。
In addition, the number of rotating disks 9 (number of stages) is further increased fr
-t) The amount of distillation can be easily increased by increasing the number of rotations of the rotating disk 9.

なお、本実施例では回転ディスク9の加か源とし2て電
熱ヒータ9aを用いたが、これに代えて回転ディスク9
及び回転シャフト10内に温水回路を構成1.7、温水
加熱により洗浄溶剤を蒸発させるようにしてもよい。
In this embodiment, the electric heater 9a was used as the force source 2 for the rotating disk 9, but instead of this, the rotating disk 9
A hot water circuit may also be provided in the rotary shaft 10 to evaporate the cleaning solvent by heating the hot water.

第5図に本発明の第2実施例を示す。本実施例は小蒸留
量の蒸留器に適用するもので、第1実施例のように回転
ディスクを用いず、蒸留器本体8の底板20においての
み溶剤を蒸発させ、底板20表面K ’IP3生ずる溶
剤蒸気気泡19を、チェーン18の掻き取り具を取り付
けたアーム22をモータ21により回転される回転シャ
フト23を介[7て回転させることにより、掻き取り除
去するものである。
FIG. 5 shows a second embodiment of the present invention. This embodiment is applied to a distiller with a small distillation volume, and unlike the first embodiment, a rotating disk is not used, and the solvent is evaporated only on the bottom plate 20 of the distiller main body 8, so that K'IP3 is generated on the surface of the bottom plate 20. The solvent vapor bubbles 19 are scraped off by rotating an arm 22 attached to a scraping tool of the chain 18 via a rotary shaft 23 rotated by a motor 21.

このような構成によっても、従来例に比べ蒸留量を約1
0%増加させることができた。
Even with this configuration, the distillation amount can be reduced by about 1 compared to the conventional example.
We were able to increase it by 0%.

発明の効果 本発明は蒸留器本体内の溶剤蒸気発生面に生じる蒸気気
泡を強制的に掻き取り、この気泡による熱伝導率の低下
の影響をなくするものであるから蒸留量を増加すること
ができ、したがって被蒸留溶剤液中の油等の異物の濃度
が高くなっても蒸留溶剤の品質を長く一定に保持でき溶
剤更新のための時間的間隔を大幅に延長し、溶剤費を低
減することができるという効果がある。
Effects of the Invention The present invention forcibly scrapes off steam bubbles generated on the solvent vapor generation surface in the distiller main body, and eliminates the effect of lowering thermal conductivity due to these bubbles, so it is possible to increase the distillation amount. Therefore, even if the concentration of foreign substances such as oil in the solvent to be distilled increases, the quality of the distilled solvent can be maintained constant for a long time, significantly extending the time interval for replacing the solvent, and reducing solvent costs. It has the effect of being able to.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来の溶剤洗浄装置の縦断面図、第2図は本発
明の第1実#i秒’、lの拡大縦断面図、第3図は第2
図の要部の拡大縦断面図、第4図は同上実施例と従来例
との蒸留量の比較を示すグラフ、第5図は本発明の第2
実施例の拡大縦断面図である。 1・・・洗浄装置本体、2・・・蒸留器、8・・・蒸留
器本体、9・・・回転ディスク、9a・・・電熱ヒータ
、10・・・回転シャフト、13a・・・トレイ、18
・・・チェーン、19・・・蒸気気泡、20・・・蒸留
器本体底面、22・・・アーム、23・・・回転シャフ
ト。 特許出願人 日本電装株式会社 傷−許出願代理人 弁理士 宵 木   朗 弁理士 西 舘 和 之 イ]ユ理土中山恭介 弁理士 山 口 昭 之 第2図 19 第4図 回転数(rpm )
FIG. 1 is a vertical cross-sectional view of a conventional solvent cleaning device, FIG. 2 is an enlarged vertical cross-sectional view of the first actual #i second', l of the present invention, and FIG.
FIG. 4 is a graph showing a comparison of the distillation amount between the above example and the conventional example, and FIG.
FIG. 3 is an enlarged vertical cross-sectional view of the embodiment. DESCRIPTION OF SYMBOLS 1... Cleaning device main body, 2... Distiller, 8... Distiller main body, 9... Rotating disk, 9a... Electric heater, 10... Rotating shaft, 13a... Tray, 18
... Chain, 19 ... Steam bubble, 20 ... Bottom of distiller body, 22 ... Arm, 23 ... Rotating shaft. Patent Applicant: Nippondenso Co., Ltd. Patent Attorney: Akira Yoiki, Patent Attorney: Kazuyuki Nishidate] Kyosuke Yuri, Patent Attorney: Akira Yamaguchi, Patent Attorney: Figure 2 19 Figure 4: Rotation speed (rpm)

Claims (1)

【特許請求の範囲】 1 洗浄溶剤を蒸留する蒸留器本体内の、洗浄溶剤の蒸
気発生面に接1.てこの蒸気発生面に生じる蒸気気泡の
掻き散り具を設けるとともに、この掻き取り具と蒸気発
生面とを相対移動可能としたことを特徴とする溶剤洗浄
装置用蒸留器。 2、前記蒸気発生面を回転可能とした特許請求の範囲第
1項記載の溶剤洗浄装置用蒸留器。 3、前記蒸気気泡の掻き取り具を回転可能とした特許請
求の範囲第1項記載の溶剤洗浄装置用蒸留器。 4、前記蒸気気泡の掻きをv班として吊下したチェーン
を用いた特許請求の範囲第1項記載の溶剤洗浄装置用蒸
留器。
[Scope of Claims] 1. In contact with the vapor generating surface of the cleaning solvent in the distiller main body for distilling the cleaning solvent. A distiller for a solvent cleaning device, characterized in that a tool for scraping off steam bubbles generated on a steam generating surface of a lever is provided, and the scraping tool and the steam generating surface are movable relative to each other. 2. The distiller for a solvent cleaning device according to claim 1, wherein the steam generating surface is rotatable. 3. The distiller for a solvent cleaning device according to claim 1, wherein the steam bubble scraping tool is rotatable. 4. The distiller for a solvent cleaning device according to claim 1, which uses a chain suspended from the steam bubbles as a V group.
JP3905283A 1983-03-11 1983-03-11 Distillation equipment for solvent cleaning apparatus Pending JPS59166201A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3905283A JPS59166201A (en) 1983-03-11 1983-03-11 Distillation equipment for solvent cleaning apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3905283A JPS59166201A (en) 1983-03-11 1983-03-11 Distillation equipment for solvent cleaning apparatus

Publications (1)

Publication Number Publication Date
JPS59166201A true JPS59166201A (en) 1984-09-19

Family

ID=12542353

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3905283A Pending JPS59166201A (en) 1983-03-11 1983-03-11 Distillation equipment for solvent cleaning apparatus

Country Status (1)

Country Link
JP (1) JPS59166201A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49106968A (en) * 1973-02-02 1974-10-11
JPS54115471A (en) * 1978-02-28 1979-09-08 Nippon Jietsuto Kougiyou Kk Dryer
JPS562881A (en) * 1979-06-21 1981-01-13 Shigeo Baba Solvent recovery apparatus

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49106968A (en) * 1973-02-02 1974-10-11
JPS54115471A (en) * 1978-02-28 1979-09-08 Nippon Jietsuto Kougiyou Kk Dryer
JPS562881A (en) * 1979-06-21 1981-01-13 Shigeo Baba Solvent recovery apparatus

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