JPH05309205A - Device for regenerating drying liquid - Google Patents

Device for regenerating drying liquid

Info

Publication number
JPH05309205A
JPH05309205A JP14354592A JP14354592A JPH05309205A JP H05309205 A JPH05309205 A JP H05309205A JP 14354592 A JP14354592 A JP 14354592A JP 14354592 A JP14354592 A JP 14354592A JP H05309205 A JPH05309205 A JP H05309205A
Authority
JP
Japan
Prior art keywords
liquid
tank
drying
separating
ipa
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.)
Granted
Application number
JP14354592A
Other languages
Japanese (ja)
Other versions
JP3272400B2 (en
Inventor
Mitsuo Goto
光夫 後藤
雅道 ▲ひじ▼野
Masamichi Hijino
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.)
Olympus Corp
Original Assignee
Olympus Optical 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 Olympus Optical Co Ltd filed Critical Olympus Optical Co Ltd
Priority to JP14354592A priority Critical patent/JP3272400B2/en
Publication of JPH05309205A publication Critical patent/JPH05309205A/en
Application granted granted Critical
Publication of JP3272400B2 publication Critical patent/JP3272400B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To normally regenerate drying liquid even if continuous washing is performed to keep the purity of the drying liquid constant by providing a washing tank for housing nonaqeous drying liquid and a separating tank for separating dehydrating liquid dissolved in the drying liquid and circulating the drying liquid between the washing tank and the separating tank. CONSTITUTION:Drying liquid 5 mixed with IPA in an inner tank 2 of a washing tank 1 overflows from the top of the inner tank 2 to flow in an external tank 3 and is discharged from a hole 10 of a drying liquid discharge pipe 8 into separating liquid 9 in a separating tank 7 through a recovery pipe 6. Since the separating liquid 9 has higher compatibility to IPA than the drying liquid 5, the IPA in the drying liquid 5 is dissolved in the separating liquid 9 and the regenerated drying liquid 5 layer is deposited on the separating liquid 9. The drying liquid 5 in a layer above a separating tank 7 is supplied to the inner tank 2 from the bottom of the washing tank 1 through a regenerated liquid circulating pipe 11. On the other hand, the separating liquid 9 in which IPA is mixed is discharged to a drain storage tank through a separated liquid discharge pipe 20, and simultaneously, the separating liquid 9 is supplied from pure water supply device through a separated liquid supply pipe 19.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ガラスレンズ・プリズ
ム等の光学部品の洗浄の際の乾燥工程に使用する乾燥液
の再生装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for regenerating a drying liquid used in a drying process for cleaning optical parts such as glass lenses and prisms.

【0002】[0002]

【従来の技術】従来、工業製品の洗浄に際しては、フロ
ンあるいはトリクロロエタン等の塩素系有機溶剤が用い
られていた。しかし、フロンやトリクロロエタン等の使
用は大気中のオゾン層の破壊の原因になるとされ、世界
的に使用的に使用が禁止される方向にあるため、上記塩
素系有機溶剤の代替品が開発されている。Surfac
e Control&洗浄設計No.49(近年編集社
発行;,91.4.1;P2〜11)にはシリコーン化
合物を主成分とした洗浄液が記載されている。また、光
学部品の洗浄手順としては、図5に示すように洗浄によ
る洗浄工程→水あるいは純水によるリンス工程→IPA
(イソプロピルアルコール)による脱水工程→フロンベ
ーパーによる乾燥工程が一般的である(例えば、精密洗
浄装置と最新応用技術、570頁〜574頁(株)工業
資料センター(1991年11月8日発行)。
2. Description of the Related Art Conventionally, chlorine-based organic solvents such as freon or trichloroethane have been used for cleaning industrial products. However, the use of CFCs, trichloroethane, etc. is said to cause the destruction of the ozone layer in the atmosphere, and there is a tendency to globally prohibit the use thereof.Therefore, alternatives to the above chlorine-based organic solvents have been developed. There is. Surfac
e Control & Cleaning Design No. 49 (Recently published by editorial company ; , 91.4.1; P2 to 11) describes a cleaning liquid containing a silicone compound as a main component. Further, as a procedure for cleaning the optical parts, as shown in FIG. 5, a cleaning process by cleaning → rinsing process with water or pure water → IPA
A dehydration process with (isopropyl alcohol) → a drying process with CFC vapor is common (for example, precision cleaning device and latest applied technology, pages 570 to 574, Industrial Materials Center Co., Ltd. (issued November 8, 1991).

【0003】[0003]

【発明が解決しようとする課題】レンズ等の光学部品
は、最終製造工程として反射防止用のコーティングを施
す。よって、膜剥離を生じさせないために洗浄では高度
の洗浄性が要求される。しかし、光学部品の洗浄手順に
おいて、フロンの代わりに上記シリコーン化合物を主成
分とした乾燥液を使用すると、洗浄物に付着したIPA
濃度が増加する。その結果、洗浄物表面からの乾燥液の
乾燥速度にばらつきが生じてシミやむらができる不具合
があった。本発明は、上記従来の問題点に鑑みなされた
もので、複数の光学部品を連続して洗浄しても乾燥液の
純度が低下せず、外観品質を良好に維持するための、乾
燥液の再生装置を提供することを目的とする。
Optical components such as lenses are coated with antireflection coating as a final manufacturing process. Therefore, in order to prevent film peeling, a high degree of cleaning property is required for cleaning. However, in the cleaning procedure of the optical parts, if the drying liquid containing the above silicone compound as the main component is used instead of CFC, the IPA adhered to the cleaning object
The concentration increases. As a result, there has been a problem that the drying speed of the dried liquid from the surface of the washed product varies and stains and unevenness occur. The present invention has been made in view of the above conventional problems, the purity of the drying liquid does not decrease even after continuously cleaning a plurality of optical components, and in order to maintain good appearance quality, the drying liquid An object is to provide a reproducing device.

【0004】[0004]

【課題を解決するための手段】上記目的と達成するため
に、本発明の第1の構成は、非水系乾燥液を収容する洗
浄槽と、前記乾燥液との相溶性が低く脱水液との相溶性
が高い分離液を下部に収容し、乾燥液に溶解した脱水液
を分離する分離槽と、洗浄槽から分離槽の下部に洗浄液
を導く配管と、分離槽の上部から洗浄槽に乾燥液を導く
配管と、乾燥液を洗浄槽と分離槽との間で循環させるポ
ンプとを設けて構成した。また、本発明の第2の構成
は、非水系乾燥液を上部に収容し、前記乾燥液との相溶
性が低く脱水液との相溶性が高い分離液を下部に収容し
て乾燥液に溶解した脱水液を分離する洗浄槽と、洗浄槽
の上部から排出した乾燥液を当該洗浄槽の下部に導く配
管と、乾燥液を洗浄槽の上部と洗浄槽の下部との間で循
環させるポンプとを設けて構成した。
In order to achieve the above object, the first structure of the present invention is such that a cleaning tank for containing a non-aqueous dry liquid and a dehydrating liquid having low compatibility with the dry liquid. A separation tank that contains a highly compatible separation liquid in the lower part and separates the dehydrated liquid dissolved in the drying liquid, a pipe that guides the cleaning liquid from the cleaning tank to the lower part of the separation tank, and a drying liquid from the upper part of the separation tank to the cleaning tank And a pump for circulating the dry liquid between the cleaning tank and the separation tank. The second configuration of the present invention is that the non-aqueous dry liquid is contained in the upper portion, and the separated liquid having low compatibility with the dry liquid and high compatibility with the dehydrated liquid is contained in the lower portion and dissolved in the dry liquid. A cleaning tank for separating the dehydrated liquid, a pipe for guiding the dry liquid discharged from the upper part of the cleaning tank to the lower part of the cleaning tank, and a pump for circulating the dry liquid between the upper part of the cleaning tank and the lower part of the cleaning tank. Is provided and configured.

【0005】[0005]

【作用】上記第1及び第2の構成によれば、脱水液とし
て用いるIPAは、乾燥液として用いるシリコーン化合
物への相溶性が高いため洗浄槽中では溶解している。そ
こで、上記乾燥液をシリコーン化合物との相溶性が低
く、かつ、IPAの相溶性がシリコーン化合物のそれよ
りも高い水からなる分離液を通すことにより、シリコー
ン化合物中に溶解していたIPAは水に引き寄せられ
る。その結果、シリコーン化合物中からIPAが除去さ
れる。シリコーン化合物は水よりも比重が軽いためIP
Aが溶解した水の上に層を形成する。乾燥液は、分離液
を分離槽あるいは洗浄槽の下部に収容し、分離液下部か
ら排出することで容易に分離液中を通過させることがで
きる。また、脱水液が溶解した分離液は、定期的に廃棄
することで高い分離能力を維持できる。
According to the first and second configurations, the IPA used as the dehydrating liquid has a high compatibility with the silicone compound used as the drying liquid, and therefore is dissolved in the cleaning tank. Therefore, the dried liquid is passed through a separation liquid containing water having a low compatibility with the silicone compound and a higher compatibility with IPA than that of the silicone compound, so that the IPA dissolved in the silicone compound is dissolved in water. Attracted to. As a result, IPA is removed from the silicone compound. IP because silicone compounds have a lower specific gravity than water
A layer is formed on the water in which A is dissolved. The dried liquid can be easily passed through the separated liquid by accommodating the separated liquid in the lower portion of the separation tank or the washing tank and discharging from the lower portion of the separated liquid. Further, the separated liquid in which the dehydrated liquid is dissolved can be maintained at a high separation capacity by periodically discarding it.

【0006】上記の相溶性は、SP値(溶解度パラメー
ター;Solubility Parameter)を
使って説明できる。実験によると、水(SP値=23.
4),IPA(SP値=11.45),シリコーン(S
P値=5.5)の3成分を混合した場合に、IPAはシ
リコーンよりも水に対して相溶性が高いことが、IRの
分析にて確認された。なお、本発明にあっては、分離液
として水あるいは純水を使用し、脱水液としてIPAを
使用したが、それに限定されるものではなく、SP値を
目安にして、水あるいは純水の代替として、巣酸溶液、
塩酸溶液、硝酸溶液、硫酸溶液を使用でき、また、IP
Aの代替として、アセトン、エタノール、メタノール、
MEK(メチルエチルケトン)を使用することができ
る。
The above-mentioned compatibility can be explained by using SP value (solubility parameter; Solubility Parameter). According to the experiment, water (SP value = 23.
4), IPA (SP value = 11.45), silicone (S
It was confirmed by IR analysis that IPA was more compatible with water than silicone when the three components having a P value of 5.5) were mixed. In the present invention, water or pure water was used as the separation liquid, and IPA was used as the dehydration liquid, but the present invention is not limited to this. As formic acid solution,
Hydrochloric acid solution, nitric acid solution, sulfuric acid solution can be used.
As an alternative to A, acetone, ethanol, methanol,
MEK (methyl ethyl ketone) can be used.

【0007】[0007]

【実施例】まず、本発明に係る乾燥液の再生装置の実施
例を説明する前に、乾燥液の再生装置を用いたレンズ等
の光学部品からなる洗浄物を洗浄する手順の一例を図3
に示して説明する。第一の洗浄工程において、洗浄物に
付着している切削油、指紋等の有機物汚れあるいは酸化
セリウム、ほこり等の無機物汚れを洗剤により除去す
る。第二のリンス工程において、洗剤をあるいは純水で
洗い流す。第三の脱水工程において、洗浄物に付着した
水をIPAで置換する。第四の乾燥工程において、本発
明の乾燥液の再生装置が用いられ洗浄物を乾燥液に浸漬
してIPAを乾燥液で置換する。引き上げ後、洗浄な空
気で温風乾燥し、あるいは、減圧乾燥して洗浄完了す
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS First, before explaining an embodiment of a drying liquid regenerating apparatus according to the present invention, an example of a procedure for cleaning a cleaning object made of optical parts such as lenses using the drying liquid regenerating apparatus is shown in FIG.
Will be described. In the first cleaning step, cutting oil, organic stains such as fingerprints, or inorganic stains such as cerium oxide and dust adhering to the washed object are removed with a detergent. In the second rinse step, the detergent is washed away with pure water. In the third dehydration step, the water attached to the washed product is replaced with IPA. In the fourth drying step, the apparatus for regenerating the dried liquid of the present invention is used to immerse the washed product in the dried liquid to replace IPA with the dried liquid. After pulling up, drying with warm air with clean air or drying under reduced pressure is completed.

【0008】[0008]

【実施例1】図1は、本発明に係る乾燥液の再生装置の
実施例1を示す断面図、図2は、再生装置における分離
槽を示す斜視図である。図1において1で示すのは洗浄
槽で、内槽2と外槽3とからなり、外槽3の外側底部中
央には超音波発振器4が設けられている。外槽3は、内
槽2からオーバーフローしたシリコーン化合物からなる
乾燥液5を受け止めるもので、内槽2と外槽3との隙間
における外槽3の底部には、乾燥液5の回収パイプ6が
接続されている。回収パイプ6は、分離槽7の下部に接
続され、その先端は乾燥液排出パイプ8となり、分離槽
7の内部に引き込まれている。分離槽7内には、乾燥液
5と水とからなる分離液9が、その比重差によって上下
に分離した状態で溜められるようになっている。上記乾
燥液排出パイプ8は、分離槽7の下方に溜められた分離
液9内に位置され、回収パイプ6で回収された乾燥液5
中に含まれるIPAが分離液9に効率よく溶解するよう
に、多数の穴10(図2参照)が開口されている。
[Embodiment 1] FIG. 1 is a sectional view showing Embodiment 1 of a drying liquid regenerating apparatus according to the present invention, and FIG. 2 is a perspective view showing a separation tank in the regenerating apparatus. In FIG. 1, reference numeral 1 denotes a cleaning tank, which is composed of an inner tank 2 and an outer tank 3, and an ultrasonic oscillator 4 is provided at the center of the outer bottom of the outer tank 3. The outer tank 3 receives the drying liquid 5 made of a silicone compound that overflows from the inner tank 2, and a recovery liquid 6 recovery pipe 6 is provided at the bottom of the outer tank 3 in the gap between the inner tank 2 and the outer tank 3. It is connected. The recovery pipe 6 is connected to the lower portion of the separation tank 7, and the tip of the recovery pipe 6 serves as a dry liquid discharge pipe 8 and is drawn into the inside of the separation tank 7. A separation liquid 9 composed of the dry liquid 5 and water is stored in the separation tank 7 in a vertically separated state due to the difference in specific gravity. The dry liquid discharge pipe 8 is located in the separated liquid 9 stored below the separation tank 7, and the dried liquid 5 collected by the recovery pipe 6 is collected.
A large number of holes 10 (see FIG. 2) are opened so that the IPA contained therein is efficiently dissolved in the separation liquid 9.

【0009】乾燥液5が収納される分離槽7の上部側面
には、再生液循環パイプ11が接続され、その他端は外
槽3の底部から内槽2の底部に接続されている。再生液
循環パイプ11には、途中にポンプ12とフィルター1
3が配置され、乾燥液5を洗浄槽1→分離槽7→洗浄槽
1の経路で循環させている。フィルター13は、液中の
微粒子を除去するためのものである。分離槽7には上蓋
14が設けられ、上蓋14には、乾燥液5の液面感知用
のフロートスイッチ15と乾燥液5の新液槽16と連通
した新液供給パイプ17が取り付けられている。新液供
給パイプ17には、途中に弁18が設けられ、フロート
スイッチ15により乾燥液5の液面低下が感知されると
弁18が開いて、新液槽16から乾燥液5の新液が分離
槽7に供給されるようになっている。さらに、分離槽7
の底部には、分離液供給パイプ19と分離液排出パイプ
20が接続されている。分離液供給パイプ19は、図示
しない純水供給装置に接続され、分離分離液供給パイプ
20は、図示しない排水貯蔵タンクに接続されている。
分離液供給パイプ19および分離液排出パイプ20に
は、途中にそれぞれ弁21及び弁22が設けられ、分離
液9が供給及び排出自在となっている。そして、分離槽
7内には、分離液供給パイプ19を介して純水供給装置
から供給された水が分離液9として半分ほど溜められる
ようになっている。
A regeneration liquid circulation pipe 11 is connected to the upper side surface of the separation tank 7 in which the dry liquid 5 is stored, and the other end is connected from the bottom of the outer tank 3 to the bottom of the inner tank 2. The regeneration liquid circulation pipe 11 has a pump 12 and a filter 1 on the way.
3 is arranged, and the dry liquid 5 is circulated in the route of the cleaning tank 1 → the separation tank 7 → the cleaning tank 1. The filter 13 is for removing fine particles in the liquid. The separation tank 7 is provided with an upper lid 14, and the upper lid 14 is provided with a float switch 15 for detecting the liquid level of the drying liquid 5 and a new liquid supply pipe 17 communicating with a new liquid tank 16 of the drying liquid 5. .. The fresh liquid supply pipe 17 is provided with a valve 18 on the way, and when the float switch 15 detects that the liquid level of the dry liquid 5 is lowered, the valve 18 is opened and the fresh liquid of the dry liquid 5 is discharged from the fresh liquid tank 16. It is supplied to the separation tank 7. Furthermore, the separation tank 7
A separated liquid supply pipe 19 and a separated liquid discharge pipe 20 are connected to the bottom of the. The separated liquid supply pipe 19 is connected to a pure water supply device (not shown), and the separated liquid supply pipe 20 is connected to a drainage storage tank (not shown).
The separation liquid supply pipe 19 and the separation liquid discharge pipe 20 are respectively provided with valves 21 and 22 in the middle thereof, so that the separation liquid 9 can be supplied and discharged freely. Then, about half of the water supplied from the pure water supply device via the separation liquid supply pipe 19 is stored as the separation liquid 9 in the separation tank 7.

【0010】次に、本実施例の再生装置の作用を説明す
る。前工程の脱水工程で水から置換され洗浄物に付着し
ているIPAは、洗浄槽12の内槽5の乾燥液5中に洗
浄物を浸漬することにより、乾燥液5に溶解して混入
し、洗浄物5から外り除かれる。内槽2の上部からオー
バーフローし外槽3内に流れ込んだIPA混入の乾燥液
5は、回収パイプ6を通って乾燥液排出パイプ8の穴1
0から分離液9中に放出される。この分離液9は、乾燥
液5よりもIPAとの相容性が高いため、乾燥液5が分
離液9中を通って上面にまで達する間に乾燥液5中のI
PAが分離液9に溶解し、再生された乾燥液5層が分離
液9の上にたまる。分離槽7の上層の乾燥液5は、再生
液循環パイプ11を通って洗浄槽1の底部から内槽2内
に供給される。一方、IPAの混入した分離液9は、分
離液排出パイプ20を通って定期的に排出貯蔵タンクに
排出されるとともに、純水供給装置から分離液供給パイ
プ19を通って供給され、分離槽7の分離液9の液高が
一定かつ混入するIPAの濃度が一定以下に維持され
る。
Next, the operation of the reproducing apparatus of this embodiment will be described. The IPA that has been displaced from water in the dehydration step of the previous step and adhered to the cleaning product is dissolved and mixed in the drying liquid 5 by immersing the cleaning product in the drying liquid 5 of the inner tank 5 of the cleaning tank 12. , And is removed from the cleaning object 5. The IPA-mixed dry liquid 5 overflowing from the upper part of the inner tank 2 and flowing into the outer tank 3 passes through the recovery pipe 6 and the hole 1 of the dry liquid discharge pipe 8.
It is released from 0 into the separated liquid 9. Since the separated liquid 9 has a higher compatibility with IPA than the dried liquid 5, while the dried liquid 5 passes through the separated liquid 9 and reaches the upper surface, the I in the dried liquid 5 is increased.
PA is dissolved in the separation liquid 9, and 5 layers of the regenerated dry liquid are accumulated on the separation liquid 9. The dry liquid 5 in the upper layer of the separation tank 7 is supplied from the bottom of the cleaning tank 1 into the inner tank 2 through the regenerant circulation pipe 11. On the other hand, the separation liquid 9 mixed with IPA is periodically discharged to the discharge storage tank through the separation liquid discharge pipe 20, and is also supplied from the pure water supply device through the separation liquid supply pipe 19 to separate the separation tank 7. The liquid height of the separated liquid 9 is constant and the concentration of the mixed IPA is maintained below a constant.

【0011】本実施例によれば、再生した乾燥液5中の
IPA濃度をガスクロマトグラフィーを使って分析した
結果、連続的に洗浄すると本実施例の再生装置を未使用
の場合には純度が徐々に低下した乾燥液を99%以上の
純度に保てることが確認された。
According to the present embodiment, the IPA concentration in the regenerated dry liquid 5 was analyzed by gas chromatography, and as a result, continuous washing revealed that the regenerator of this embodiment had a high purity when it was not used. It was confirmed that the gradually lowered dry liquid could be maintained at a purity of 99% or higher.

【0012】[0012]

【実施例2】図4は、本発明の実施例2の再生装置を示
す断面図である。洗浄槽1は内槽2と内槽3とからな
り、内槽2の中間部には網状の間仕切り板23が設けら
れている。洗浄槽1の内槽2と外槽3との隙間の底部に
は、乾燥液5の回収パイプ26が接続されている。この
回収パイプ26の他端は、バッファー槽27の上部側面
に接続されている。バッファー槽27の下部側面には、
バッファー槽27内の乾燥液5を内槽2内に供給する液
循環パイプ28が接続されており、この液循環パイプ2
8には、外槽3を貫通して内槽2の下部側面に接続され
ている。液循環パイプ28の先端は、乾燥液排出パイプ
29となり、内槽2の内部に引き込まれている。乾燥液
排出パイプ29には、前記実施例1と同様に多数の穴3
0が設けられている。乾燥液排出パイプ29の途中に
は。ポンプ12とフィルター13が設けられ、乾燥液5
を洗浄槽1→バッファー槽27→洗浄槽1の経路で循環
させている。
Second Embodiment FIG. 4 is a sectional view showing a reproducing apparatus according to a second embodiment of the present invention. The cleaning tank 1 is composed of an inner tank 2 and an inner tank 3, and a mesh-like partition plate 23 is provided at an intermediate portion of the inner tank 2. A recovery liquid recovery pipe 26 is connected to the bottom of the gap between the inner tank 2 and the outer tank 3 of the cleaning tank 1. The other end of the recovery pipe 26 is connected to the upper side surface of the buffer tank 27. On the lower side surface of the buffer tank 27,
A liquid circulation pipe 28 for supplying the dry liquid 5 in the buffer tank 27 into the inner tank 2 is connected.
8 is connected to the lower side surface of the inner tank 2 through the outer tank 3. The tip of the liquid circulation pipe 28 serves as a dry liquid discharge pipe 29, which is drawn into the inner tank 2. The drying liquid discharge pipe 29 has a large number of holes 3 as in the first embodiment.
0 is provided. In the middle of the dry liquid discharge pipe 29. A pump 12 and a filter 13 are provided, and the drying liquid 5
Is circulated in the route of washing tank 1 → buffer tank 27 → washing tank 1.

【0013】バッファー槽27には上蓋31が設けら
れ、上蓋31には、乾燥液5の液面感知用のフロートス
イッチ15と乾燥液5の新液槽16に連通した新液供給
パイプ17が取り付けられている。新液供給パイプ17
には、途中に弁18が設けられ、フロートスイッチ15
により乾燥液5の液面低下が感知されると弁18が開い
て、新液槽16から乾燥液5の新液がバッファー槽27
に供給されるようになっている。内槽2の底部には、外
槽3を貫通して分離液供給パイプ19と分離液排出パイ
プ20が接続されている。分離液供給パイプ19は、図
示しない純水供給装置に接続され、分離液排出パイプ2
0は、図示しない排出貯蔵タンクに接続されている。分
離供給パイプ19及び分離液排出パイプ20には、途中
にそれぞれ弁21及び弁22が設けられ、分離液9が供
給及び排出自在となっている。そして、内槽2内には、
分離液供給パイプ19を介して純水供給装置から供給さ
れた水が分離液9として仕切り板23の下まで溜められ
るようになっている。
The buffer tank 27 is provided with an upper lid 31, and the upper lid 31 is provided with a float switch 15 for detecting the liquid level of the dry liquid 5 and a new liquid supply pipe 17 communicating with a new liquid tank 16 of the dry liquid 5. Has been. New liquid supply pipe 17
A valve 18 is provided on the way to the float switch 15
When the decrease in the liquid level of the dry liquid 5 is detected by the valve 18, the valve 18 is opened, and the new liquid of the dry liquid 5 is transferred from the new liquid tank 16 to the buffer tank 27.
To be supplied to. A separation liquid supply pipe 19 and a separation liquid discharge pipe 20 are connected to the bottom of the inner tank 2 through the outer tank 3. The separated liquid supply pipe 19 is connected to a pure water supply device (not shown), and the separated liquid discharge pipe 2
0 is connected to a discharge storage tank (not shown). The separation supply pipe 19 and the separation liquid discharge pipe 20 are provided with valves 21 and 22 in the middle, respectively, so that the separation liquid 9 can be supplied and discharged freely. And in the inner tank 2,
The water supplied from the pure water supply device via the separated liquid supply pipe 19 is stored as the separated liquid 9 under the partition plate 23.

【0014】本実施例にあっては、前記実施例1と同様
に、内槽2の上部からオアーバーフローしたIPA混入
の乾燥液5は、回収パイプ26を通ってバッファー槽2
7に収容された後、ポンプ12により液循環パイプ28
を通って乾燥液排出パイプ29の穴30から分離液9に
放出される。乾燥液5が分離液9中を通ってその上面ま
で達する間に乾燥液5中のIPAが水に溶解し、再生さ
れた乾燥液5層が分離液9の上に溜まる。一方、IPA
の混入した分離液9は、分離液排出パイプ20を通って
定期的に排出貯蔵タンクに排出されるとともに、純水供
給装置から分離液供給パイプ19を通って供給され、内
槽2内の分離液9の液高が一定かつ混入するIPAの濃
度が一定以下に維持される。
In this embodiment, as in the case of Embodiment 1, the IPA-mixed dry liquid 5 which has been overflowed from the upper portion of the inner tank 2 passes through the recovery pipe 26 and the buffer tank 2
After being stored in 7, the liquid circulation pipe 28 is pumped by the pump 12.
Through which the separated liquid 9 is discharged from the hole 30 of the dry liquid discharge pipe 29. While the dry liquid 5 passes through the separation liquid 9 and reaches the upper surface thereof, IPA in the dry liquid 5 is dissolved in water, and the regenerated dry liquid 5 layer is accumulated on the separation liquid 9. On the other hand, IPA
The separated liquid 9 mixed with is periodically discharged to the discharge storage tank through the separated liquid discharge pipe 20, and is also supplied from the pure water supply device through the separated liquid supply pipe 19 for separation in the inner tank 2. The liquid height of the liquid 9 is constant and the concentration of the mixed IPA is maintained below a certain level.

【0015】本実施例によれば、洗浄槽1の内槽2内で
乾燥液5の再生が可能となり、実施例1の分離槽が不要
となる。また、再生した乾燥液中のIPA濃度をガスク
ロマトグラフィーを使って分析した結果、実施例1と同
様の効果があることが確認された。
According to this embodiment, the dry liquid 5 can be regenerated in the inner tank 2 of the cleaning tank 1, and the separation tank of the first embodiment is not necessary. In addition, as a result of analyzing the IPA concentration in the regenerated dried liquid using gas chromatography, it was confirmed that the same effect as in Example 1 was obtained.

【0016】[0016]

【発明の効果】以上、説明したように本発明によれば、
連続的に洗浄しても常時乾燥液を再生できるので乾燥液
の純度を一定に保ことができ、その結果洗浄物にシミや
むら等の外観不良を無くすことが可能となる。
As described above, according to the present invention,
Since the dried liquid can be constantly regenerated even after continuous washing, the purity of the dried liquid can be kept constant, and as a result, it is possible to eliminate appearance defects such as stains and unevenness on the washed product.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明に係る乾燥液の再生装置の実施例1を示
す断面図である。
FIG. 1 is a cross-sectional view showing a first embodiment of a drying liquid regenerating apparatus according to the present invention.

【図2】実施例1の再生装置における分離槽を示す斜視
図である。
FIG. 2 is a perspective view showing a separation tank in the regenerating apparatus of Example 1.

【図3】本発明の各実施例の乾燥液の再生装置を用いた
洗浄・乾燥工程を示すブロック線図である。
FIG. 3 is a block diagram showing a cleaning / drying process using the drying liquid regenerating apparatus of each example of the present invention.

【図4】本発明に係る乾燥液の再生装置の実施例2を示
す断面図である。
FIG. 4 is a cross-sectional view showing a second embodiment of the drying liquid regenerating apparatus according to the present invention.

【図5】従来の洗浄・乾燥工程等を示すブロック線図で
ある。
FIG. 5 is a block diagram showing a conventional cleaning / drying process and the like.

【符号の説明】[Explanation of symbols]

1 洗浄槽 2 内槽 3 外槽 5 乾燥液 6 26 回収パイプ 7 分離槽 9 分離液 11 再生液循環パイプ 12 ポンプ 28 液循環パイプ 1 Cleaning Tank 2 Inner Tank 3 Outer Tank 5 Dry Liquid 6 26 Recovery Pipe 7 Separation Tank 9 Separation Liquid 11 Regeneration Liquid Circulation Pipe 12 Pump 28 Liquid Circulation Pipe

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 非水系乾燥液を収容する洗浄槽と、前記
乾燥液との相溶性が低く脱水液との相溶性が高い分離液
を下部に収容し、乾燥液に溶解した脱水液を分離する分
離槽と、洗浄槽から分離槽の下部に洗浄液を導く配管
と、分離槽の上部から洗浄槽に乾燥液を導く配管と、乾
燥液を洗浄槽と分離槽との間で循環させるポンプとを有
することを特徴とする乾燥液の再生装置。
1. A washing tank containing a non-aqueous dry liquid, and a separated liquid having a low compatibility with the dry liquid and a high compatibility with the dehydrated liquid are contained in a lower portion, and the dehydrated liquid dissolved in the dried liquid is separated. A separation tank, a pipe for introducing the cleaning liquid from the cleaning tank to the lower part of the separation tank, a pipe for introducing the drying liquid from the upper part of the separation tank to the cleaning tank, and a pump for circulating the drying liquid between the cleaning tank and the separation tank. An apparatus for regenerating a dried liquid, comprising:
【請求項2】 非水系乾燥液を上部に収容し、前記乾燥
液との相溶性が低く脱水液との相溶性が高い分離液を下
部に収容して乾燥液に溶解した脱水液を分離する洗浄槽
と、洗浄槽の上部から排出した乾燥液を当該洗浄槽の下
部に導く配管と、乾燥液を洗浄槽の上部と洗浄槽の下部
との間で循環させるポンプとを有することを特徴とする
乾燥液の再生装置。
2. A non-aqueous dry liquid is contained in an upper part, and a separated liquid having a low compatibility with the dry liquid and a high compatibility with a dehydrated liquid is contained in the lower part to separate the dehydrated liquid dissolved in the dry liquid. A cleaning tank, a pipe for guiding the dry liquid discharged from the upper portion of the cleaning tank to the lower portion of the cleaning tank, and a pump for circulating the dry liquid between the upper portion of the cleaning tank and the lower portion of the cleaning tank. Drying liquid recycling device.
JP14354592A 1992-05-08 1992-05-08 Dry liquid regeneration equipment Expired - Fee Related JP3272400B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14354592A JP3272400B2 (en) 1992-05-08 1992-05-08 Dry liquid regeneration equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14354592A JP3272400B2 (en) 1992-05-08 1992-05-08 Dry liquid regeneration equipment

Publications (2)

Publication Number Publication Date
JPH05309205A true JPH05309205A (en) 1993-11-22
JP3272400B2 JP3272400B2 (en) 2002-04-08

Family

ID=15341244

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14354592A Expired - Fee Related JP3272400B2 (en) 1992-05-08 1992-05-08 Dry liquid regeneration equipment

Country Status (1)

Country Link
JP (1) JP3272400B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5647914A (en) * 1994-07-26 1997-07-15 Olympus Optical Co., Ltd. Nonaqueous solvent regenerating method for use in cleaning

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5647914A (en) * 1994-07-26 1997-07-15 Olympus Optical Co., Ltd. Nonaqueous solvent regenerating method for use in cleaning
WO2004091749A1 (en) * 1994-07-26 2004-10-28 Mitsuo Gotoh Method of regenerating nonaqueous solvent used for cleaning and apparatus therefor

Also Published As

Publication number Publication date
JP3272400B2 (en) 2002-04-08

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