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JP3333308B2 - Vacuum degreasing cleaning apparatus and its vacuum degreasing cleaning method - Google Patents
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JP3333308B2 - Vacuum degreasing cleaning apparatus and its vacuum degreasing cleaning method - Google Patents

Vacuum degreasing cleaning apparatus and its vacuum degreasing cleaning method

Info

Publication number
JP3333308B2
JP3333308B2 JP06452194A JP6452194A JP3333308B2 JP 3333308 B2 JP3333308 B2 JP 3333308B2 JP 06452194 A JP06452194 A JP 06452194A JP 6452194 A JP6452194 A JP 6452194A JP 3333308 B2 JP3333308 B2 JP 3333308B2
Authority
JP
Japan
Prior art keywords
cleaning
drying chamber
washing
drying
vacuum
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
Application number
JP06452194A
Other languages
Japanese (ja)
Other versions
JPH07243074A (en
Inventor
丈夫 加藤
稔 小田
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.)
Ulvac Inc
Original Assignee
Ulvac Inc
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 Ulvac Inc filed Critical Ulvac Inc
Priority to JP06452194A priority Critical patent/JP3333308B2/en
Publication of JPH07243074A publication Critical patent/JPH07243074A/en
Application granted granted Critical
Publication of JP3333308B2 publication Critical patent/JP3333308B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Cleaning By Liquid Or Steam (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)

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、半導体装置や精密機器
等の工業製品を洗浄剤によって真空系で脱脂洗浄する装
置及びその方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus and a method for degrease and cleaning industrial products such as semiconductor devices and precision equipment in a vacuum system using a cleaning agent.

【0002】[0002]

【従来の技術及びその問題点】この種の工業製品を真空
脱脂洗浄するための、第1従来例としての真空脱脂洗浄
装置20の配管系統図を図5に示した。この装置20は
二室型と称されるものであり、タンクT内に隔壁Aによ
り乾燥室21と洗浄室22とが上下に画成され、隔壁A
の開口Aaを真空シール可能に仕切弁24が設けられて
いる。乾燥室21の一側壁部に形成した開口Taを介し
て被洗浄物Wを出し入れし得るように扉23が設けら
れ、乾燥室21はバルブ9を介して真空排気装置として
のトラップ15と真空ポンプ16とが接続されている。
なお、扉23の外部には、被洗浄物Wの装填装置29が
設けられている。又、洗浄室22には洗浄剤Sが収容さ
れ、バルブ25、26を介して洗浄剤Sを再生させるた
めの蒸留再生装置64が接続されている。すなわち、洗
浄剤Sは洗浄室22の底部からバルブ25のラインを経
て蒸留再生装置64へ送り込まれ、油脂分を分離され再
生された洗浄剤Sはバルブ26のラインを経て洗浄室2
2の上部へ戻されるようになっている。更には、受け入
れた被洗浄物Wを乾燥室21から洗浄室22へ降ろして
洗浄剤Sに液浴させ、次いで乾燥室21へ引き上げるた
めの昇降台28を備えた昇降装置27が乾燥室21内を
主体にして設けられており、図示されていないが乾燥室
21には系内へN2 ガスを送り込むためのN2 ガス配管
が配設されている。
2. Description of the Related Art FIG. 5 shows a piping system diagram of a vacuum degreasing / cleaning apparatus 20 as a first conventional example for vacuum degreasing cleaning of this kind of industrial product. This apparatus 20 is of a so-called two-chamber type. A drying chamber 21 and a cleaning chamber 22 are vertically defined by a partition A in a tank T, and the partition A
A gate valve 24 is provided so that the opening Aa can be vacuum-sealed. Through an opening Ta formed on one side wall of the drying chamber 21 door 23 so as to out the object to be cleaned W is provided, the drying chamber 21 traps 15 of a vacuum exhaust device via the valve 9 and the vacuum pump 16 are connected.
Note that, outside the door 23, a loading device 29 for the article W to be cleaned is provided. Further, the cleaning agent 22 is accommodated in the cleaning chamber 22, and a distillation regeneration device 64 for regenerating the cleaning agent S is connected via valves 25 and 26. That is, the cleaning agent S is sent from the bottom of the cleaning chamber 22 to the distillation / regeneration device 64 through the line of the valve 25, and the regenerated cleaning agent S from which the oils and fats are separated is passed through the line of the valve 26.
2 to be returned to the top. Further, the lifting / lowering device 27 provided with a lifting / lowering table 28 for lowering the received article W to be washed from the drying chamber 21 to the cleaning chamber 22 so as to bathe the cleaning agent S in the cleaning chamber 21 , and then moving the cleaning object S into the drying chamber 21 . The drying room is provided mainly with
The N 21 is provided with an N 2 gas pipe for sending N 2 gas into the system.

【0003】この第1従来例の作用を説明するに、先ず
全バルブは閉の状態にあり、洗浄室22内はN2 ガス雰
囲気にあるものとする。扉23を開として、装填装置2
9によって被洗浄物Wを乾燥室21へ押し込み、昇降装
置27の昇降台28へ載置して扉23を密閉する。そし
て、図示しないN2 ガス配管からのN2 ガスで乾燥室2
1内の空気を置換してから、仕切弁24を開とし、被洗
浄物Wを昇降装置27によって洗浄室22内へ下降さ
せ、洗浄剤Sに液浴させる。所定時間後、乾燥室21
引き上げて仕切弁24を閉とする。
To explain the operation of the first conventional example, first, it is assumed that all valves are in a closed state, and the inside of the cleaning chamber 22 is in an N 2 gas atmosphere. With the door 23 opened, the loading device 2
The cleaning object W is pushed into the drying chamber 21 by 9 and placed on the elevating table 28 of the elevating device 27 to seal the door 23. The drying chamber with N 2 gas from the N 2 gas pipe (not shown) 2
After the air in 1 is replaced, the gate valve 24 is opened, and the object to be cleaned W is lowered into the cleaning chamber 22 by the elevating device 27, so that the cleaning agent S is bathed with the liquid. After a predetermined time, it is lifted to the drying chamber 21 and the gate valve 24 is closed.

【0004】次いで、バルブ9を開とし、真空ポンプ1
6によって乾燥室21内を真空排気し、被洗浄物Wに付
着している洗浄剤Sを真空乾燥する。所定時間後にバル
ブ9を閉とし、乾燥室21内へN2 ガスを導入して大気
圧としてから、扉23を開とし、被洗浄物Wを取り出
す。このようにして真空脱脂洗浄の1サイクルが完了す
るが、以後このサイクルが繰り返される。
Then, the valve 9 is opened, and the vacuum pump 1
The inside of the drying chamber 21 is evacuated by 6 to vacuum-dry the cleaning agent S adhering to the object W to be cleaned. After a predetermined time, the valve 9 is closed, N 2 gas is introduced into the drying chamber 21 to make it atmospheric pressure, the door 23 is opened, and the article W to be cleaned is taken out. Thus, one cycle of vacuum degreasing and washing is completed, and this cycle is thereafter repeated.

【0005】この間、必要であれば、洗浄剤Sの再生を
行なう。すなわち、バルブ25、26を開とし、蒸留再
生装置64に付属する送液ポンプによって、洗浄剤Sを
洗浄室22から蒸留再生装置64へ送り込み、再生され
た洗浄剤Sは蒸留再生装置64に付属する送液ポンプに
よって洗浄室22へ戻される。なお、洗浄剤Sには通常
は消防法上の第3石油類に該当する炭化水素系のものが
使用される。
During this time, if necessary, the cleaning agent S is regenerated. That is, the valves 25 and 26 are opened, and the cleaning agent S is sent from the cleaning chamber 22 to the distillation regeneration device 64 by the liquid pump attached to the distillation regeneration device 64, and the regenerated cleaning agent S is attached to the distillation regeneration device 64. The liquid is returned to the cleaning chamber 22 by the liquid sending pump. Note that, as the cleaning agent S, a hydrocarbon-based cleaning agent corresponding to the third petroleum based on the Fire Service Law is usually used.

【0006】この二室型の真空脱脂洗浄装置20は液浴
方式で脱脂効率が高いほか、洗浄剤Sを加温すると真空
脱脂洗浄サイクルが短縮されて20分間程度になり、従
来の各種真空脱脂洗浄装置の中では最短の真空脱脂洗浄
サイクルを与える。又、洗浄室22内の洗浄剤Sは常に
大気に触れることがないように操作されるので、引火、
爆発に対する安全性も高い。
The two-chamber vacuum degreasing / cleaning apparatus 20 has a high degreasing efficiency in a liquid bath system. In addition, when the cleaning agent S is heated, the vacuum degreasing / cleaning cycle is shortened to about 20 minutes. Provide the shortest vacuum degreasing cleaning cycle in the cleaning equipment. Further, since the cleaning agent S in the cleaning chamber 22 is operated so as not to always contact the atmosphere, the
High safety against explosion.

【0007】しかし、この装置20は二室型であること
による欠点もある。すなわち、真空シールされる大型の
仕切弁24や昇降装置27が全体の装置コストを大巾に
上昇させている。
However, this device 20 has a drawback due to its two-chamber type. In other words, the large gate valve 24 and the elevating device 27 which are vacuum-sealed greatly increase the overall device cost.

【0008】次に第2従来例として、一室型と称される
真空脱脂洗浄装置30を説明する。図6はこの装置30
の配管系統図であり、洗浄剤Sを収容するタンクT’内
の洗浄乾燥室31は蓋32によって密閉され、被洗浄物
Wは洗浄乾燥室31内の架台33の上に載置される。洗
浄乾燥室31の上部には、バルブ9を介してトラップ1
5と、これに続く真空ポンプ16が接続されており、図
示しないがN2 ガス配管も配設されている。更には、洗
浄乾燥室31には、バルブ35、36を介して、洗浄剤
Sの受器34が接続されている。これは、洗浄乾燥室
内で真空乾燥が行なわれる間、洗浄剤Sを一時的に貯
留待避させ、次に洗浄乾燥室31内で脱脂洗浄が行なわ
れる時には、受器34から洗浄剤Sを再び洗浄乾燥室
へ戻すためにある。又、受器34にはバルブ37を介
して蒸留再生装置64が接続され、受器34中の洗浄剤
Sはバルブ37のラインを経て蒸留再生装置64へ送り
込まれ、再生された洗浄剤Sはバルブ38のラインを経
て洗浄乾燥室31へ戻されるようになっている。
Next, as a second conventional example, a vacuum degreasing cleaning device 30 called a one-chamber type will be described. FIG.
The washing / drying chamber 31 in the tank T ′ containing the cleaning agent S is sealed by a lid 32, and the article W to be washed is placed on a gantry 33 in the washing / drying chamber 31 . In the upper part of the washing / drying chamber 31 , the trap 1 is connected via a valve 9.
5 and a vacuum pump 16 subsequent thereto are connected, and an N 2 gas pipe (not shown) is also provided. Further, a receiver 34 for the cleaning agent S is connected to the cleaning / drying chamber 31 via valves 35 and 36. This is the washing and drying room 3
The cleaning agent S is temporarily stored and evacuated while vacuum drying is performed in the cleaning chamber 1, and then, when degreasing is performed in the cleaning and drying chamber 31 , the cleaning agent S is again transferred from the receiver 34 to the cleaning and drying chamber 3.
There is to return to 1 . Further, a distillation regenerating device 64 is connected to the receiver 34 via a valve 37, and the cleaning agent S in the receiver 34 is sent to the distillation regenerating device 64 via the valve 37 line, and the regenerated cleaning agent S is The cleaning and drying chamber 31 is returned via the valve 38 line.

【0009】この第2従来例の装置30は次のように作
用する。なお、全てのバルブは閉の状態にあり、洗浄乾
燥室31内の洗浄剤Sは受器34に貯留されているもの
とする。蓋32を開けて被洗浄物Wを洗浄乾燥室31
の架台33に載置し、蓋32で密閉する。そして、洗浄
乾燥室31内の空気を図示しないN2 ガス配管からのN
2 ガスで置換する。次に、バルブ36を開とし、受器3
4に付属する送液ポンプによって洗浄剤Sを受器34か
ら洗浄乾燥室31へ戻して、被洗浄物Wを液浴させる。
図6はその液浴状態を示している。所定時間後、バルブ
35を開とし、受器34に付属する送液ポンプによって
洗浄乾燥室31内の洗浄剤Sを受器34へ移し、バルブ
35、36を閉とする。
The device 30 of the second conventional example operates as follows. It is assumed that all the valves are in a closed state, and the cleaning agent S in the cleaning and drying chamber 31 is stored in the receiver 34. The lid 32 is opened, and the object to be cleaned W is placed on the gantry 33 in the cleaning / drying chamber 31 . Then, the air in the cleaning / drying chamber 31 is converted into N 2 gas from an N 2 gas pipe (not shown).
Replace with 2 gases. Next, the valve 36 is opened and the receiver 3
The cleaning agent S is returned from the receiver 34 to the cleaning / drying chamber 31 by the liquid feed pump attached to 4, and the object W to be cleaned is bathed.
FIG. 6 shows the liquid bath state. After a predetermined time, the valve 35 is opened, the cleaning agent S in the cleaning / drying chamber 31 is transferred to the receiver 34 by the liquid feed pump attached to the receiver 34, and the valves 35 and 36 are closed.

【0010】次いで、バルブ9を開とし、真空ポンプ1
6によって洗浄乾燥室31を真空排気して被洗浄物Wに
付着している洗浄剤Sを真空乾燥する。乾燥が終了すれ
ばバルブ9を閉とし、洗浄乾燥室31へN2 ガスを導入
して大気圧としてから、蓋32を開け被洗浄物Wを取り
出して、真空脱脂洗浄の1サイクルが完了する。そし
て、このサイクルが繰り返される。
Next, the valve 9 is opened, and the vacuum pump 1
6, the cleaning / drying chamber 31 is evacuated to vacuum and the cleaning agent S adhering to the object to be cleaned W is vacuum dried. When the drying is completed, the valve 9 is closed, N 2 gas is introduced into the cleaning / drying chamber 31 to bring the pressure to the atmospheric pressure, the lid 32 is opened, the object W to be cleaned is taken out, and one cycle of vacuum degreasing cleaning is completed. Then, this cycle is repeated.

【0011】この間、洗浄剤Sが油脂分で汚れて来れ
ば、洗浄剤Sの再生が行なわれる。すなわち、バルブ3
7を開とし、蒸留再生装置64に付属する送液ポンプに
よって受器34中の洗浄剤Sを蒸留再生装置64へ送り
込み、再生された洗浄剤Sはバルブ38を開とし、同じ
く蒸留再生装置64に付属する送液ポンプによって洗浄
乾燥室31へ戻した後、バルブ37、38は閉とされ
る。
During this time, if the cleaning agent S becomes contaminated with oils and fats, the cleaning agent S is regenerated. That is, the valve 3
7 is opened, and the cleaning agent S in the receiver 34 is sent to the distillation and regeneration unit 64 by the liquid feed pump attached to the distillation and regeneration unit 64, and the regenerated cleaning agent S is opened by the valve 38. After returning to the washing / drying chamber 31 by the liquid feed pump attached to the valve, the valves 37 and 38 are closed.

【0012】この第2従来例の一室型の真空脱脂洗浄装
置30は、第1従来例のような仕切弁12、昇降装置2
7を持たないので、装置コストは大巾に低下するが、洗
浄乾燥室31において脱脂洗浄と真空乾燥とを行なう故
に、洗浄剤Sを洗浄乾燥室31と受器34との間で往復
させており、これに時間を要して洗浄乾燥室31に遊び
が生じ、脱脂洗浄サイクルの時間は第1従来例のほぼ2
倍となっている。従って、第2従来例の処理能力当りの
装置コストは、第1従来例の場合と較べて、それ程低下
していない。
The one-chamber vacuum degreasing / cleaning apparatus 30 of the second conventional example comprises a gate valve 12 and a lifting / lowering apparatus 2 as in the first conventional example.
7, the apparatus cost is greatly reduced. However, since degreasing and vacuum drying are performed in the cleaning / drying chamber 31 , the cleaning agent S is reciprocated between the cleaning / drying chamber 31 and the receiver 34. As a result, play takes place in the cleaning / drying chamber 31 because of the time required, and the time of the degreasing cleaning cycle is about 2 times that of the first conventional example.
Doubled. Therefore, the apparatus cost per processing capacity of the second conventional example is not so much lower than that of the first conventional example.

【0013】[0013]

【発明が解決しようとする問題点】本発明は上述の問題
に鑑みてなされ、装置コストが低く、かつ二室型真空脱
脂洗浄装置と同等以上の処理能力を有する真空脱脂洗浄
装置及びその真空脱脂洗浄方法を提供することを目的と
する。
DISCLOSURE OF THE INVENTION The present invention has been made in view of the above-mentioned problems, and has a low apparatus cost and a vacuum degreasing / cleaning apparatus having a processing capacity equal to or higher than that of a two-chamber vacuum degreasing / cleaning apparatus, and a vacuum degreasing apparatus therefor. It is intended to provide a cleaning method.

【0014】以上の目的は、被洗浄物を収容するための
対を構成する洗浄乾燥室と、該洗浄乾燥室に接続される
共通の真空排気装置と、バイパスラインを内蔵する洗浄
剤の蒸留再生装置とからなり、洗浄乾燥室と真空排気装
置とは真空排気路で接続され、洗浄乾燥室と蒸留再生装
置とは洗浄乾燥室から蒸留再生装置に至る回収洗浄剤路
と、蒸留再生装置から洗浄乾燥室に至る再生洗浄剤路と
によって接続されており、洗浄剤を対の一方の洗浄乾燥
室から他方の洗浄乾燥室へ移替える場合には、一方の洗
浄乾燥室から回収洗浄剤路および蒸留再生装置に内蔵さ
れるバイパスラインを経て他方の洗浄乾燥室に至る再生
洗浄剤路が移替路とされることを特徴とする真空脱脂洗
浄装置、によって達成される。
[0014] The above object is to accommodate an object to be cleaned.
A washing / drying chamber forming a pair and connected to the washing / drying chamber
Cleaning with a common vacuum pump and built-in bypass line
Cleaning and drying room and vacuum exhaust system.
Is connected to the cleaning and drying chamber and the distillation and regeneration equipment.
Is the recovery cleaning agent path from the cleaning and drying room to the distillation regeneration device.
And the regenerating cleaning agent path from the distillation regenerator to the cleaning drying room
Connected and dried by one side of the cleaning agent
When transferring from one room to the other washing and drying room,
It is installed in the recovery cleaning agent channel and distillation regeneration device from the cleaning and drying room.
Regeneration through the bypass line to the other washing and drying room
This is achieved by a vacuum degreasing / cleaning apparatus characterized in that the cleaning agent path is a transfer path .

【0015】又、以上の目的は、被洗浄物を収容するた
めの対を構成する洗浄乾燥室と、該洗浄乾燥室に接続さ
れる共通の真空排気装置と、バイパスラインを内蔵する
洗浄剤の蒸留再生装置とからなり、洗浄乾燥室と真空排
気装置とは真空排気路で接続され、洗浄乾燥室と蒸留再
生装置とは洗浄乾燥室から蒸留再生装置に至る回収洗浄
剤路と、蒸留再生装置から洗浄乾燥室に至る再生洗浄剤
路とによって接続されており、洗浄剤を対の一方の洗浄
乾燥室から他方の洗浄乾燥室へ移替える場合には、一方
の洗浄乾燥室から回収洗浄剤路および蒸留再生装置に内
蔵されるバイパスラインを経て他方の洗浄乾燥室に至る
再生洗浄剤路が移替路とされる真空脱脂洗浄装置を使用
して、被洗浄物を洗浄剤によって脱脂洗浄し、次いで被
洗浄物に付着する洗浄剤を真空乾燥するに際し、一方の
洗浄乾燥室が脱脂洗浄の工程にある時は、他方の洗浄乾
燥室は真空乾燥の工程にあるようにすることを特徴とす
る真空脱脂洗浄方法、によって達成される。
[0015] Further, the above object is to accommodate the object to be cleaned.
And a washing / drying chamber forming a pair.
Built-in common vacuum pumping device and bypass line
It consists of a cleaning agent distillation and regeneration unit.
The vacuum system is connected to the vacuum system by a vacuum exhaust path.
The raw equipment is the recovery and washing from the washing and drying room to the distillation and regeneration unit.
Recycled cleaning agent from the agent path and distillation / regeneration unit to the washing / drying room
The cleaning agent is connected by one of the two
When transferring from the drying room to the other washing and drying room,
From the washing / drying chamber of the
To the other washing and drying room via the bypass line
The object to be cleaned is degreased and cleaned with a cleaning agent using a vacuum degreasing cleaning device in which the regenerated cleaning agent path is a transfer path , and then, when the cleaning agent attached to the object to be cleaned is vacuum-dried, one of the <br> When the cleaning / drying chamber is in the degreasing cleaning step, the other cleaning / drying chamber is in the vacuum drying step.

【0016】[0016]

【作用】対の一方の洗浄乾燥室が脱脂洗浄の工程にある
時は、他方の洗浄乾燥室はは真空乾燥の工程にあるよう
にしているので、処理能力は従来の一室型真空脱脂洗浄
装置のほぼ2倍、すなわち従来の二室型真空脱脂洗浄装
置と同等以上の処理が可能であり、かつ真空排気装置及
び蒸留再生装置を共有させているので、装置コストは大
巾には増大しない。又、洗浄剤を圧力差で移替えるの
で、運転コストを節減することができ、更には常に再生
された洗浄剤での脱脂洗浄が可能である。
When one of the cleaning / drying chambers is in the degreasing / cleaning step, the other cleaning / drying chamber is in the vacuum drying step. The processing can be performed almost twice as much as the apparatus, that is, the same processing as or more than the conventional two-chamber vacuum degreasing / cleaning apparatus, and the apparatus costs are not greatly increased because the vacuum exhaust apparatus and the distillation regeneration apparatus are shared. . Further, since the cleaning agent is transferred by the pressure difference, the operation cost can be reduced, and further, the degreasing cleaning with the regenerated cleaning agent is always possible.

【0017】[0017]

【実施例】以下、本発明の実施例による真空脱脂洗浄装
置について、図面を参照して説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, a vacuum degreasing and cleaning apparatus according to an embodiment of the present invention will be described with reference to the drawings.

【0018】図1は第1実施例による真空脱脂洗浄装置
10Aの配管系統図である。本実施例の装置10Aは、
真空排気装置としてのトラップ61、真空ポンプ62、
及び蒸留再生装置64を共有して、第1洗浄乾燥室41
を画成するタンクT1 と第2洗浄乾燥室51を画成する
タンクT2 とが対峙して設けられている。
FIG. 1 is a piping diagram of a vacuum degreasing / cleaning apparatus 10A according to a first embodiment. The device 10A of the present embodiment includes:
A trap 61 as a vacuum exhaust device, a vacuum pump 62,
And the first regenerating and drying chamber 41 by sharing the
A tank T 1 defining a tank T 2 defining a second washing and drying chamber 51 is provided to face each other.

【0019】すなわち、第1洗浄乾燥室41はシーリン
グ材43を介して蓋42によって密閉され、同じく第2
洗浄乾燥室51はシーリング材53を介して蓋52によ
って密閉される。そして、第1洗浄乾燥室41はバルブ
1を介し、又、第2洗浄乾燥室51はバルブ2を介し
て、共有するトラップ61と、これに続く真空ポンプ6
2とに接続されて排気路とされている。更には第1洗浄
乾燥室41の底部がバルブ3、チーズ66、フィルタ6
3、バルブ5、蒸留再生装置64に内蔵されるバイパス
ライン64'(破線で示す)、バルブ8を経て第2洗浄乾
燥室51と接続されて洗浄剤Sの移替路とされ、第2洗
浄乾燥室51の底部はバルブ4、チーズ66、フィルタ
63、バルブ5、蒸留再生装置64に内蔵されるバイパ
スライン64'、バルブ7を経て第1洗浄乾燥室41
接続されて洗浄剤Sのもう一方の移替路とされる。
That is, the first cleaning / drying chamber 41 is sealed by the lid 42 via the sealing material 43,
The washing / drying chamber 51 is closed by a lid 52 via a sealing material 53. The first cleaning / drying chamber 41 is connected via a valve 1, and the second cleaning / drying chamber 51 is connected via a valve 2 to a common trap 61 and a vacuum pump 6
2 and an exhaust path. Further, the bottom of the first washing / drying chamber 41 is provided with the valve 3, the cheese 66, and the filter 6.
3, a valve 5, a bypass line 64 '(shown by a broken line) incorporated in the distillation regeneration device 64, and a valve 8 connected to the second cleaning / drying chamber 51 to serve as a transfer path for the cleaning agent S. The bottom of the drying chamber 51 is connected to the first cleaning / drying chamber 41 via the valve 4, the cheese 66, the filter 63, the valve 5, the bypass line 64 ′ built in the distillation regeneration device 64, and the valve 7 for cleaning. This is the other transfer path for the agent S.

【0020】又更には、第1洗浄乾燥室41の底部から
バルブ3、チーズ66、フィルタ63、バルブ5、蒸留
再生装置64、又は、第2洗浄乾燥室51の底部からバ
ルブ4、チーズ66、フィルタ63、バルブ5、蒸留再
生装置64に至るラインはそれぞれの回収洗浄剤回路と
されている。この蒸留再生装置64はバルブ7を介して
第1洗浄乾燥室41と接続され、又、バルブ8を介して
第2洗浄乾燥室51と接続されて、それぞれへの再生洗
浄剤路とされている。なお、図示していないが、第1洗
浄乾燥室41、第2洗浄乾燥室51の上部には、それぞ
れN2 ガス配管が配設されている。
Further, from the bottom of the first washing and drying chamber 41 , the valve 3, the cheese 66, the filter 63, the valve 5, the distillation regenerating device 64, or the bottom of the second washing and drying chamber 51 , the valve 4, the cheese 66, The lines leading to the filter 63, the valve 5, and the distillation regeneration device 64 are each a collection cleaning agent circuit. The distillation / regeneration device 64 is connected to the first cleaning / drying chamber 41 via the valve 7 and to the second cleaning / drying chamber 51 via the valve 8 to provide a regenerating cleaning agent path to each. . Although not shown, N 2 gas pipes are provided above the first cleaning / drying chamber 41 and the second cleaning / drying chamber 51 , respectively.

【0021】本実施例による真空脱脂洗浄装置10Aは
以上のように構成されるが、次にその作用を説明する。
The vacuum degreasing / cleaning apparatus 10A according to the present embodiment is constructed as described above. Next, the operation thereof will be described.

【0022】本実施例の装置10Aは、第1洗浄乾燥室
41と第2洗浄乾燥室51に関し、一方が被洗浄物Wを
洗浄剤Sに液浴させての脱脂洗浄の工程にある時は、他
方は被洗浄物Wに付着する洗浄剤Sを乾燥させる真空乾
燥の工程にあるように作動され、洗浄剤Sは交互に脱脂
洗浄工程となる第1洗浄乾燥室41と第2洗浄乾燥室
との間を往復される。
The apparatus 10A of the present embodiment includes a first cleaning and drying chamber.
Regarding 41 and the second cleaning / drying chamber 51 , when one of them is in a degreasing cleaning step in which the cleaning object S is bathed in the cleaning agent S, the other is for drying the cleaning agent S attached to the cleaning object W. is actuated to be in the process of vacuum drying, detergent S is the first washing and drying chamber 41 which is a degreasing cleaning step alternately second washing and drying chamber 5
It is reciprocated between 1 .

【0023】すなわち、図1を参照して、第1洗浄乾燥
41内にはこれから脱脂洗浄される被洗浄物W2 が収
容されて、シーリング材43を介し蓋42で密閉され、
かつ既に真空排気して減圧にされているものとし、第2
洗浄乾燥室51内では、被洗浄物W1 が洗浄剤Sに液浴
されて脱脂洗浄工程は完了しているものとする。又、真
空ポンプ62は常時運転されており、全バルブは閉の状
態にあるものとする。
That is, referring to FIG. 1, an object to be cleaned W 2 to be degreased and cleaned is accommodated in a first cleaning and drying chamber 41 , and is sealed with a lid 42 via a sealing material 43.
It is assumed that the pressure has already been reduced by evacuation,
The cleaning and drying chamber 51, it is assumed that the object to be cleaned W 1 is degreasing step is a liquid bath in the detergent S is completed. Further, it is assumed that the vacuum pump 62 is constantly operated and all valves are in a closed state.

【0024】バルブ4、5、7を開とすることにより、
第2洗浄乾燥室51内の洗浄剤Sは圧力差によってチー
ズ66、フィルタ63、蒸留再生装置64に内蔵される
バイパスライン64'を通って第1洗浄乾燥室41内へ
移る。この時、洗浄剤Sに固形分が含まれるならば、こ
れはフィルタ63によって瀘別される。この洗浄剤Sの
移替え後、バルブ4、5、7を閉とすると共に、バルブ
2を開として、第2洗浄乾燥室51を真空ポンプ62と
繋ぐ。これらの操作によって、第1洗浄乾燥室41では
被洗浄物W2 の脱脂洗浄が開始され、第2洗浄乾燥室
51では被洗浄物W1 に付着している洗浄剤Sの真空
乾燥が開始される。
By opening valves 4, 5, and 7,
The cleaning agent S in the second cleaning / drying chamber 51 moves into the first cleaning / drying chamber 41 through the cheese 66, the filter 63, and the bypass line 64 ′ built in the distillation / regeneration device 64 due to the pressure difference. At this time, if the solid content is contained in the cleaning agent S, this is filtered out by the filter 63. After the transfer of the cleaning agent S, the valves 4, 5, and 7 are closed and the valve 2 is opened to connect the second cleaning and drying chamber 51 to the vacuum pump 62. With these operations, the degreasing cleaning of the object to be cleaned W2 is started in the first cleaning / drying chamber 41 , and the second cleaning / drying chamber is started.
At 51 , the vacuum drying of the cleaning agent S attached to the article to be cleaned W1 is started.

【0025】所定時間の経過後、第2洗浄乾燥室51
方はバルブ2を閉とし、図示しないN2 ガス配管からN
2 ガスを導入して大気圧としてから、蓋52を開けて被
洗浄物W1 を取り出す。続いて、次の被洗浄物W3 を収
容し(図示されていない)、シーリング材53を介し
て、蓋52によって密閉する。次いで、第2洗浄乾燥室
51内の空気をN2 ガスで置換した後、バルブ2を開と
して、真空ポンプ16によって第2洗浄乾燥室51を真
空排気し、減圧にしてバルブ2を閉とする。一方、第1
洗浄乾燥室41の方では、この間に被洗浄物W2 の脱脂
洗浄が完了する。
After a lapse of a predetermined time, the valve 2 is closed in the second cleaning / drying chamber 51 and N 2 gas piping (not shown) is connected to the N 2 gas pipe.
After the atmospheric pressure by introducing two gases, taking out the article to be cleaned W 1 opens the lid 52. Then, to accommodate the next object to be cleaned W 3 (not shown), via the sealing material 53 is sealed by a lid 52. Next, the second washing and drying room
After replacing the air in 51 with N 2 gas, the valve 2 is opened, the second cleaning / drying chamber 51 is evacuated by the vacuum pump 16, the pressure is reduced, and the valve 2 is closed. Meanwhile, the first
It was washing and drying chamber 41, degreasing of the object to be cleaned W 2 is completed during this time.

【0026】この状態は、当初において被洗浄物W2
収容して真空減圧下にあった第1洗浄乾燥室41は脱脂
洗浄の完了状態にあり、被洗浄物W1 の脱脂洗浄を完了
していた第2洗浄乾燥室51は被洗浄物W3 を収容して
真空減圧下にあり、丁度、洗浄乾燥室4151とが当
初の工程を入れ替えた状態である。以降、このような操
作が繰り返される。
[0026] This state is the first washing and drying chamber 41 was under vacuum reduced pressure and accommodates the cleaning object W 2 at the beginning is in complete state of degreasing, to complete the degreasing of the object to be cleaned W 1 the second washing and drying chamber 51 has been located under vacuum reduced pressure to accommodate the object to be cleaned W 3, just a state in which the washing and drying chamber 41 and 51 is replaced with the original process. Thereafter, such an operation is repeated.

【0027】上記の真空脱脂洗浄が繰り返されて、洗浄
剤Sが汚れて来ると、それに含まれる油脂分を蒸留再生
装置64によって除去するべく、洗浄剤Sの再生が行な
われる。すなわち、図1によって説明すれば、真空脱脂
洗浄を中断して、第1洗浄乾燥室41は被洗浄物Wn
収容せずに減圧とされ、第2洗浄乾燥室51は被洗浄物
m の脱脂洗浄が完了しているものとする。
When the cleaning agent S is contaminated by repeating the above vacuum degreasing cleaning, the cleaning agent S is regenerated in order to remove the oils and fats contained in the cleaning agent S by means of the distillation and regeneration device 64. That is, if explained by Figure 1, to interrupt the vacuum degreasing, first washing and drying chamber 41 is a vacuum without accommodating the object to be cleaned W n, the second washing and drying chamber 51 to be washed W m Degreasing cleaning has been completed.

【0028】第2洗浄乾燥室51内の洗浄剤Sは上記で
説明したように圧力差によって第1洗浄乾燥室41へ移
され、第2洗浄乾燥室51では、被洗浄物Wm の真空乾
燥、取り出し、続いて被洗浄物Wn の収容が通常の操作
通り行なわれるが、減圧のみ行なわれない。
The detergent S of the second washing and drying chamber 51 is transferred to the first washing and drying chamber 41 by a pressure difference as described above, the second washing and drying chamber 51, the vacuum drying of the object to be cleaned W m , taken out, followed by accommodating the object to be cleaned W n is is carried out normal operations as not performed under reduced pressure only.

【0029】第1洗浄乾燥室41へ移替えられた洗浄剤
Sはバルブ3、バルブ5を開とし、蒸留再生装置64に
付属する送液ポンプによって蒸留再生装置64へ送り込
まれる。蒸留再生装置64で油脂分が除かれ再生された
洗浄剤Sは、バルブ8を開とし、蒸留再生装置64に付
属する送液ポンプによって、第2洗浄乾燥室51へ送ら
れて、既に収容されている被洗浄物Wn の脱脂洗浄に使
用される。空になった第1洗浄乾燥室41は次の被洗浄
物Wo が収容され減圧とされて、真空脱脂洗浄の再開に
備えられる。
The cleaning agent S transferred to the first cleaning / drying chamber 41 is sent to the distillation and regeneration unit 64 by opening the valve 3 and the valve 5 and using a liquid feed pump attached to the distillation and regeneration unit 64. The cleaning agent S whose fats and oils have been removed and regenerated by the distillation regeneration device 64 is opened to the valve 8, sent to the second cleaning and drying chamber 51 by the liquid feed pump attached to the distillation regeneration device 64, and is already stored. used in degreasing of the object to be cleaned W n are. The first cleaning / drying chamber 41 that has been emptied contains the next object Wo to be cleaned and is depressurized to prepare for the resumption of vacuum degreasing cleaning.

【0030】洗浄剤Sの再生は上述のように真空脱脂洗
浄プロセスの途中に行なうほかに、真空脱脂洗浄プロセ
スの終了後に、被洗浄物Wのない状態でプロセスとは別
に蒸留再生のみを行なってもよい。
The regeneration of the cleaning agent S is performed in the middle of the vacuum degreasing cleaning process as described above, and after the completion of the vacuum degreasing cleaning process, only the distillation regeneration is performed separately from the process without the object W to be cleaned. Is also good.

【0031】上記の再生は洗浄剤Sが汚れた時点で、そ
の再生のために蒸留再生装置64を間欠的に運転する再
生方法であるが、蒸留再生装置64を連続的に運転し、
常に再生された洗浄剤Sで脱脂洗浄することも可能であ
る。
The above-mentioned regeneration is a regeneration method in which the distillation regeneration device 64 is operated intermittently for the regeneration when the cleaning agent S becomes contaminated.
It is also possible to perform degreasing cleaning with the regenerated cleaning agent S at all times.

【0032】すなわち、図2は図1と同じく本実施例の
装置10Aの配管系統図であるが、図2に示すように、
第2洗浄乾燥室51が脱脂洗浄工程にある時に、バルブ
4、バルブ5、バルブ8を開とし、洗浄剤Sを第2洗浄
乾燥室51と蒸留再生装置64との間で矢印Mで示すよ
うに循環させ再生させる方法である。こうすることによ
って、第2洗浄乾燥室51には常に再生された洗浄剤S
が供給されるので脱脂洗浄効率が向上する。次に第1洗
浄乾燥室41が脱脂洗浄工程となった時は、洗浄剤S
は、勿論、第1洗浄乾燥室41と蒸留再生装置64との
間を矢印Nのように循環される。なお、これらの循環を
させながら被洗浄物Wのない状態で蒸留再生のみを行な
ってもよい。
That is, FIG. 2 is a piping system diagram of the apparatus 10A of the present embodiment as in FIG. 1, but as shown in FIG.
When the second cleaning / drying chamber 51 is in the degreasing cleaning step, the valve 4, the valve 5, and the valve 8 are opened, and the detergent S is supplied between the second cleaning / drying chamber 51 and the distillation regeneration device 64 as indicated by an arrow M. It is a method of circulating and reproducing. By doing so, the regenerated cleaning agent S is always stored in the second cleaning and drying chamber 51.
Is supplied, so that the degreasing and cleaning efficiency is improved. Next, when the first cleaning / drying chamber 41 enters the degreasing cleaning step, the cleaning agent S
Is naturally circulated between the first washing / drying chamber 41 and the distillation / regeneration device 64 as shown by the arrow N. In addition, only the distillation regeneration may be performed in the state where there is no cleaning object W while circulating these.

【0033】以上の実施例では2室の洗浄乾燥室が同じ
形状であることを想定しているが、例えば図3の斜視図
に示すように、一方の洗浄乾燥室41’を円筒体、他方
の洗浄乾燥室51’を直方体とし、両者をほぼ同一の容
積とすれば、形状の異なる被洗浄物の真空脱脂洗浄が可
能となる。
In the above embodiment, it is assumed that the two washing and drying chambers have the same shape. For example, as shown in the perspective view of FIG. If the washing and drying chamber 51 ′ is formed in a rectangular parallelepiped and has substantially the same volume, the objects to be washed having different shapes can be vacuum-degreased and cleaned.

【0034】又、真空ポンプ62と蒸留再生装置64の
能力が大きい場合には、洗浄乾燥室を4室以上の洗浄乾
燥室部からなるものとすることができる。図4はこのよ
うな第2実施例を示すが、洗浄乾燥室がn対の洗浄乾燥
からなる真空脱脂洗浄装置10Bの配管系統図であ
る。すなわち、洗浄乾燥室は、第1グループのn個の洗
浄乾燥室部11、G12、G13、・・・G1nと、第2グル
ープのn個の洗浄乾燥室部21、G22、G23、・・・G
2nとのn対からなっており、それらの中で例えばG 11
21 とは対を構成している。そして、第1グループの洗
浄乾燥室が脱脂洗浄の工程にある時は、第2グループ
の洗浄乾燥室は真空乾燥の工程にあるように作動され
る。洗浄乾燥室と、トラップ61、真空ポンプ62
とはそれぞれのバルブ1’又は2’を介して接続されて
排気路とされる。第1グループの洗浄乾燥室11、G
12、G13、・・・G1nの底部は、それぞれのバルブ
3’、チーズ66、フィルタ63、バルブ5、蒸留再生
装置64に内蔵されるバイパスライン64'を経て第2
グループの洗浄乾燥室21、G22、G23、・・・G2n
と接続されて洗浄剤Sの移替路とされ、第2グループの
洗浄乾燥室21、G22、G23、・・・G2nの底部は、
それぞれのバルブ4、チーズ66、フィルタ63、バル
ブ5、蒸留再生装置64に内蔵されるバイパスライン
4'を経て第1グループの洗浄乾燥室11、G12、G
13、・・・G1nと接続されて洗浄剤Sのもう一方の移替
路とされる。なお、バルブ1’、2’、3’又は4’は
第1実施例におけるバルブ1、2、3又は4と対応す
る。又更には、第1グループの洗浄乾燥室11
12、G13、・・・G1nの底部から、それぞれのバルブ
3’、チーズ66、フィルタ63、バルブ5、蒸留再生
装置64、又は第2グループの洗浄乾燥室21
22、G23、・・・G2nの底部から、それぞれのバルブ
4’、チーズ66、フィルタ63、バルブ5、蒸留再生
装置64に至るラインはそれぞれの回収洗浄剤路とされ
ている。この蒸留再生装置64と各洗浄乾燥室の上部
とを結ぶラインはそれぞれの再生洗浄路である。
[0034] Further, when the ability of the vacuum pump 62 and the distillation reproducing apparatus 64 is large, the washing and drying chamber 4 or more rooms cleaning dry
It can be composed of a drying chamber . Figure 4 shows such a second embodiment, the washing and drying chamber is a piping diagram of a vacuum degreasing cleaning apparatus 10B consisting of washing and drying chamber of the n pairs. That is, the washing / drying chamber has n washings in the first group.
Kiyoshi drying chamber G 11, G 12, G 13 , ··· G 1n and, n pieces of the washing and drying chamber G 21 of the second group, G 22, G 23, ··· G
Has become the n pairs of 2n, for example, G 11 is within them
Constitute a pair and G 21. When the washing and drying chamber of the first group is in the process of degreasing cleaning, washing and drying chamber of the second group is actuated to be in the process of vacuum drying. Each washing and drying chamber, the trap 61, a vacuum pump 62
Are connected via respective valves 1 'or 2' to form an exhaust path. Washing and drying chamber of the first group G 11, G
12, G 13, the bottom of the · · · G 1n, each valve 3 second through ', cheese 66, filter 63, valve 5, the distillation reproducing apparatus 64 bypass line 64 which is incorporated in'
Washing and drying chamber G 21 groups, G 22, G 23, ··· G 2n
Is the transfer Kawaro of connected detergent S and, washing and drying chamber of the second group G 21, G 22, G 23 , the bottom of the · · · G 2n is
Each valve 4, cheese 66, filter 63, valve 5, and bypass line 6 built in the distillation regeneration device 64
The first group of cleaning and drying chamber G 11 through the 4 ', G 12, G
13 ,... G 1n are connected to the other transfer path of the cleaning agent S. The valves 1 ', 2', 3 'or 4' correspond to the valves 1, 2, 3 or 4 in the first embodiment. Furthermore, the washing / drying chamber section G 11 of the first group,
From the bottom of G 12 , G 13 ,... G 1n , the respective valves 3 ′, cheese 66, filter 63, valve 5, distillation regeneration device 64, or washing and drying chamber part G 21 of the second group,
Lines from the bottom of G 22 , G 23 ,... G 2n to each valve 4 ′, cheese 66, filter 63, valve 5, and distillation / regeneration device 64 form respective recovery cleaning agent paths. The lines connecting the distillation regeneration device 64 and the upper part of each washing / drying chamber section are respective regeneration cleaning agent passages.

【0035】以上、本発明の各実施例について説明した
が、勿論、本発明はこれらによって限定されることな
く、本発明の技術的思想に基づいて種々の変形が可能で
ある。
Although the embodiments of the present invention have been described above, the present invention is, of course, not limited thereto, and various modifications can be made based on the technical concept of the present invention.

【0036】例えば以上の実施例においては、脱脂洗浄
中にある洗浄剤Sの加温装置を設けていないが、各洗浄
乾燥室の周囲に加熱スチームの配管を巻装して、洗浄剤
Sを加温するようにしてもよい。
For example, in the above-described embodiment, the heating device for the cleaning agent S during the degreasing cleaning is not provided. However, a heating steam pipe is wound around each cleaning and drying chamber to supply the cleaning agent S. You may make it heat.

【0037】又、以上の実施例において、例えば第1洗
浄乾燥室41から蒸留再生装置64への回収洗浄剤路に
よる洗浄剤Sの移送に際し、第1洗浄乾燥室41と蒸留
再生装置64との間に別に均圧ラインを設けて移送をス
ムースにすることは好ましく、これとは別の方法とし
て、第1洗浄乾燥室41へN2 ガスを送り込むことも洗
浄剤Sの移送を容易にする。
In the above embodiment, for example, when the cleaning agent S is transferred from the first cleaning / drying chamber 41 to the distillation / regeneration apparatus 64 through the recovered cleaning agent path, the first cleaning / drying chamber 41 and the distillation / regeneration apparatus 64 are connected to each other. It is preferable to provide a pressure equalizing line separately to make the transfer smoother. Alternatively, sending N 2 gas to the first cleaning / drying chamber 41 also facilitates the transfer of the cleaning agent S.

【0038】又、以上の実施例においては2室を対とす
る洗浄乾燥室としたが、脱脂洗浄工程と真空乾燥工程と
の所要時間が均等でない場合には、長時間の工程を2室
で分担し、短時間の工程を1室で行なうような3室をユ
ニットとする構成にしてもよい。
In the above embodiment, two washing / drying chambers are used as a pair. However, if the time required for the degreasing cleaning step and the time required for the vacuum drying step are not equal, a long time step is carried out in two chambers. A configuration may be adopted in which three units are shared, in which the sharing and the short process are performed in one room.

【0039】[0039]

【発明の効果】従来の一室型真空脱脂洗浄装置における
と同様な洗浄乾燥室を対として設けて一方の洗浄乾燥室
を脱脂洗浄に、他方の洗浄乾燥室を真空乾燥に使用する
ので、洗浄乾燥室に遊びを生ずることなく、従来の一室
型と較べてほぼ2倍の処理能力となり、かつ真空排気装
置と蒸留再生装置とは共有させているので、装置コスト
はそれ程増大しない。従って、処理能力当りの装置コス
トは大巾に低下する。
EFFECT OF THE INVENTION degreasing one of the washing and drying chamber <br/> provided as pairs similar washing and drying chamber as in the conventional room vacuum degreasing cleaning apparatus, used in vacuum drying of the other washing and drying chamber As a result, there is no play in the washing / drying chamber, the processing capacity is almost twice that of the conventional single-chamber type, and the vacuum exhaust unit and the distillation regeneration unit are shared, so that the equipment cost increases significantly. do not do. Therefore, the equipment cost per processing capacity is greatly reduced.

【0040】又、脱脂洗浄工程にある洗浄乾燥室と、真
空乾燥工程にある洗浄乾燥室との間で洗浄剤を移替えて
使用するので、別な洗浄剤タンクや配管を必要としな
い。更には、その移替えを圧力差で行なうので、運転コ
ストを節減し得る。
Further, since the cleaning agent is transferred and used between the cleaning / drying chamber in the degreasing cleaning step and the cleaning / drying chamber in the vacuum drying step, no separate cleaning agent tank or piping is required. Furthermore, since the transfer is performed with a pressure difference, the operating cost can be reduced.

【0041】又、洗浄乾燥室を異なる形状の対として、
異なる形状の被洗浄物を真空脱脂洗浄し得る。
Further, the washing and drying chambers are formed as pairs of different shapes,
Objects of different shapes can be vacuum degreased and cleaned.

【0042】又、被洗浄物の脱脂洗浄と、洗浄剤の再生
とを同時に行なって、常に再生された洗浄剤で脱脂洗浄
できるので、脱脂洗浄効率を向上させることができる。
Further, the degreasing and cleaning of the object to be cleaned and the regeneration of the cleaning agent are simultaneously performed, and the degreasing and cleaning can be performed with the regenerated cleaning agent at all times, so that the degreasing and cleaning efficiency can be improved.

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

【図1】本発明の第1実施例による真空脱脂洗浄装置の
配管系統図である。
FIG. 1 is a piping diagram of a vacuum degreasing / cleaning apparatus according to a first embodiment of the present invention.

【図2】図1と同じ図であるが、被洗浄物の脱脂洗浄と
洗浄剤の再生とを同時に行なう真空脱脂洗浄方法におけ
る、洗浄剤の流れを示す。
FIG. 2 is the same view as FIG. 1, but shows a flow of a cleaning agent in a vacuum degreasing cleaning method for simultaneously performing degreasing and cleaning of an object to be cleaned and regeneration of the cleaning agent.

【図3】洗浄乾燥室の他例を示す斜視図である。FIG. 3 is a perspective view showing another example of the cleaning and drying chamber.

【図4】第2実施例でn対の洗浄乾燥室からなる真空脱
脂洗浄装置の配管系統図である。
FIG. 4 is a piping system diagram of a vacuum degreasing / cleaning apparatus including n pairs of cleaning / drying chambers in a second embodiment.

【図5】第1従来例による真空脱脂洗浄装置の配管系統
図である。
FIG. 5 is a piping diagram of a vacuum degreasing and cleaning apparatus according to a first conventional example.

【図6】第2従来例による真空脱脂洗浄装置の配管系統
図である。
FIG. 6 is a piping diagram of a vacuum degreasing / cleaning apparatus according to a second conventional example.

【符号の説明】41 第1洗浄乾燥室51 第2洗浄乾燥室 61 トラップ 62 真空ポンプ 63 フィルタ 64 蒸留再生装置 S 洗浄剤 W 被洗浄物[Description of Signs] 41 First Washing / Drying Room 51 Second Washing / Drying Room 61 Trap 62 Vacuum Pump 63 Filter 64 Distillation / Regeneration Apparatus S Cleaning Agent W Cleaning Object

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C23G 5/04 B08B 3/08 C23G 5/00 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) C23G 5/04 B08B 3/08 C23G 5/00

Claims (9)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 被洗浄物を収容するための対を構成する
洗浄乾燥室と、該洗浄乾燥室に接続される共通の真空排
気装置と、バイパスラインを内蔵する洗浄剤の蒸留再生
装置とからなり、 前記洗浄乾燥室と前記真空排気装置とは真空排気路で接
続され、 前記洗浄乾燥室と前記蒸留再生装置とは前記洗浄乾燥室
から前記蒸留再生装置に至る回収洗浄剤路と、前記蒸留
再生装置から前記洗浄乾燥室に至る再生洗浄剤路とによ
って接続されており、 前記洗浄剤を前記対の一方の前記洗浄乾燥室から他方の
前記洗浄乾燥室へ移替える場合には、前記一方の洗浄乾
燥室から前記回収洗浄剤路および前記蒸留再生装置に内
蔵された前記バイパスラインを経て前記他方の洗浄乾燥
室に至る前記再生洗浄剤路が移替路とされる ことを特徴
とする真空脱脂洗浄装置。
A pair for accommodating an object to be cleaned is provided.
A washing and drying chamber and a common vacuum exhaust connected to the washing and drying chamber
Regeneration of cleaning agent with built-in gas and bypass line
The cleaning and drying chamber and the vacuum exhaust device are connected by a vacuum exhaust path.
The washing / drying chamber and the distillation / regeneration apparatus are connected to the washing / drying chamber.
A recovery cleaning agent path from the distillation and regeneration apparatus to the distillation and regeneration apparatus;
A regenerating cleaning agent path from the regenerating device to the cleaning / drying chamber.
The cleaning agent is supplied from one of the washing and drying chambers of the pair to the other.
When transferring to the washing and drying room, the one of the washing and drying
From the drying chamber to the recovery cleaning agent passage and the distillation regeneration device.
Washing and drying of the other through the stored bypass line
The reclaimed cleaning agent path leading to the chamber is a transfer path .
【請求項2】 前記対を構成する洗浄乾燥室がほぼ同一
容積で異なった形状とされている請求項1に記載の真空
脱脂洗浄装置。
2. The washing and drying chambers constituting the pair are substantially the same.
2. The vacuum of claim 1, wherein the vacuum is shaped differently.
Degreasing cleaning equipment.
【請求項3】 前記対の一方の洗浄乾燥室が複数の洗浄
乾燥室部からなり、前記他方の洗浄乾燥室の同数の洗浄
乾燥室部がそれぞれ対となるように形成されており、か
つ前記一方の洗浄乾燥室を構成する前記複数の洗浄乾燥
室部と前記他方の洗浄乾燥室を構成する前記同数の洗浄
乾燥室部が前記共通の真空排気装置と前記バイパスライ
ンを内蔵する洗浄剤の蒸留再生装置に接続されている請
求項1に記載の真空脱脂乾燥装置。
3. The cleaning and drying chamber of one of the pair includes a plurality of cleaning and drying chambers.
The same number of washings in the other washing and drying chamber
The drying chambers are formed so as to be paired with each other.
The plurality of washing and drying constituting the one washing and drying chamber
The same number of washings constituting a chamber and the other washing and drying chamber
A drying chamber is provided with the common evacuation device and the bypass line.
The contractor connected to the distillation and regeneration device
The vacuum degreasing and drying apparatus according to claim 1.
【請求項4】 被洗浄物を収容するための対を構成する
洗浄乾燥室と、該洗浄乾燥室に接続される共通の真空排
気装置と、バイパスラインを内蔵する洗浄剤の蒸留再生
装置とからなり、前記洗浄乾燥室と前記真空排気装置と
は真空排気路で接続され、前記洗浄乾燥室と前記蒸留再
生装置とは前記洗浄乾燥室から前記蒸留再生装置に至る
回収洗浄剤路と、前記蒸留再生装置から前記洗浄乾燥室
に至る再生洗浄剤路とによって接続されており、前記洗
浄剤を前記対の一方の前記洗浄乾燥室から他方の前記洗
浄乾燥室へ移替える場合には、前記一方の洗浄乾燥室か
ら前記回収洗浄剤路および前記蒸留再生装置に内蔵され
たバイパスラインを経て 前記他方の洗浄乾燥室に至る前
記再生洗浄剤路が移替路とされる真空脱脂洗浄装置を使
用して、 前記被洗浄物を前記洗浄剤によって脱脂洗浄し、次いで
前記被洗浄物に付着する前記洗浄剤を真空乾燥するに際
し、前記一方の洗浄乾燥室が脱脂洗浄の工程にある時
は、前記他方の洗浄乾燥室は真空乾燥の工程にあるよう
にすることを特徴とする真空脱脂洗浄方法。
4. A pair for accommodating an object to be cleaned is provided.
A washing and drying chamber and a common vacuum exhaust connected to the washing and drying chamber
Regeneration of cleaning agent with built-in gas and bypass line
The cleaning and drying chamber and the evacuation device
Are connected by a vacuum exhaust path, and the washing and drying chamber and the distillation
The raw equipment is from the washing and drying chamber to the distillation and regeneration unit
A recovery cleaning agent passage, and the cleaning and drying chamber
Connected to the regenerating cleaning agent path leading to
Cleaning agent from one of the washing and drying chambers of the pair
When transferring to a cleaning / drying room, use
Built into the recovered cleaning agent path and the distillation regeneration device.
Before reaching the other washing and drying room via the bypass line
Using a vacuum degreasing cleaning device in which the regenerated cleaning agent path is a transfer path, the object to be cleaned is degreased and washed with the cleaning agent, and then the cleaning agent attached to the object to be cleaned is vacuum dried. Wherein the one cleaning and drying chamber is in a degreasing cleaning step, and the other cleaning and drying chamber is in a vacuum drying step.
【請求項5】 前記対を構成する洗浄乾燥室がほぼ同一
容積で異なった形状とされている真空脱脂洗浄装置を使
用して、 前記被洗浄物を前記洗浄剤によって脱脂洗浄し、次いで
前記被洗浄物に付着する前記洗浄剤を真空乾燥するに際
し、前記一方の洗浄乾燥室が脱脂洗浄の工程にある時
は、前記他方の洗浄乾燥室は真空乾燥の工程にあるよう
にする請求項4に記載の真空脱脂洗浄方法。
5. The washing and drying chambers constituting the pair are substantially the same.
Use vacuum degreasing and cleaning equipment that has different shapes in volume.
In use, the object to be cleaned is degreased and washed with the cleaning agent, and then
When vacuum-drying the cleaning agent attached to the object to be cleaned,
And when the one of the cleaning and drying chambers is in a degreasing cleaning process.
The other washing and drying chamber is in a vacuum drying process.
The vacuum degreasing method according to claim 4, wherein
【請求項6】 前記対の一方の洗浄乾燥室が複数の洗浄
乾燥室部からなり、前記他方の洗浄乾燥室の同数の洗浄
乾燥室部がそれぞれ対を形成するように設けられてお
り、かつ前記一方の洗浄乾燥室を構成する前記複数の洗
浄乾燥室部と前記他方の洗浄乾燥室を構成する前記同数
の洗浄乾燥室部が前記共通の真空排気装置と前記バイパ
スラインを内蔵する洗浄剤の蒸留再生装置に接続されて
いる真空脱脂乾燥装置を使用して、 前記被洗浄物を前記洗浄剤によって脱脂洗浄し、次いで
前記被洗浄物に付着する前記洗浄剤を真空乾燥するに際
し、前記一方の洗浄乾燥室が脱脂洗浄の工程にある時
は、前記他方の洗浄乾燥室は真空乾燥の工程にあるよう
にする請求項4に記載の真空脱脂洗浄方法。
6. The cleaning and drying chamber of one of the pair includes a plurality of cleaning and drying chambers.
The same number of washings in the other washing and drying chamber
The drying chambers are provided so as to form a pair.
And the plurality of washings constituting the one washing and drying chamber.
The same number constituting the cleaning and drying chamber and the other cleaning and drying chamber
The washing and drying chamber is provided with the common vacuum exhaust device and the bypass.
Connected to a cleaning and distillation apparatus with built-in sling
Using a vacuum degreasing and drying apparatus, the object to be cleaned is degreased and cleaned with the cleaning agent, and then
When vacuum-drying the cleaning agent attached to the object to be cleaned,
And when the one of the cleaning and drying chambers is in a degreasing cleaning process.
The other washing and drying chamber is in a vacuum drying process.
The vacuum degreasing method according to claim 4, wherein
【請求項7】 前記脱脂洗浄の工程を完了した前記一方
の洗浄乾燥室から、次に脱脂洗浄の工程に入る前記他方
の洗浄乾燥室へ前記移替路によって前記洗浄剤の移替え
を行なう請求項4に記載の真空脱脂洗浄方法。
7. The one which has completed the degreasing and washing step.
From the washing and drying chamber of the other, and then enter the degreasing washing process
Transfer of the cleaning agent to the washing and drying room by the transfer path
The vacuum degreasing cleaning method according to claim 4, wherein the cleaning is performed.
【請求項8】 前記洗浄剤の移替えが、前記一方の洗浄
乾燥室を常圧とし、前記他方の洗浄乾燥室を減圧とする
圧力差によって行なわれる請求項5に記載の真空脱脂洗
浄方法。
8. The method according to claim 8 , wherein the transfer of the cleaning agent is performed by the cleaning of the one side.
The drying chamber is at normal pressure, and the other washing and drying chamber is at reduced pressure.
The vacuum degreasing according to claim 5, which is performed by a pressure difference.
Purification method.
【請求項9】 何れかの前記洗浄乾燥室が脱脂洗浄の工
程にある時に、前記 洗浄乾燥室から前記回収洗浄剤路、
前記蒸留再生装置、および前記再生洗浄剤路を経て前記
蒸留再生装置へ戻すように洗浄剤を連続的に循環させ
て、前記被洗浄物の脱脂洗浄と前記洗浄剤の再生とを同
時に行なう請求項4に記載の真空脱脂洗浄方法。
9. The cleaning and drying chamber according to claim 1 , wherein the cleaning and drying chamber is a degreasing cleaning step.
When it is in the process, the recovered cleaning agent path from the cleaning and drying chamber;
The distillation and regeneration apparatus, and
Continuous circulation of detergent to return to distillation regeneration unit
The degreasing and cleaning of the object to be cleaned and the regeneration of the cleaning agent are performed at the same time.
The vacuum degreasing method according to claim 4, which is performed at any time.
JP06452194A 1994-03-07 1994-03-07 Vacuum degreasing cleaning apparatus and its vacuum degreasing cleaning method Expired - Lifetime JP3333308B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06452194A JP3333308B2 (en) 1994-03-07 1994-03-07 Vacuum degreasing cleaning apparatus and its vacuum degreasing cleaning method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06452194A JP3333308B2 (en) 1994-03-07 1994-03-07 Vacuum degreasing cleaning apparatus and its vacuum degreasing cleaning method

Publications (2)

Publication Number Publication Date
JPH07243074A JPH07243074A (en) 1995-09-19
JP3333308B2 true JP3333308B2 (en) 2002-10-15

Family

ID=13260613

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Link
JP (1) JP3333308B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000153243A (en) * 1998-11-17 2000-06-06 Japan Field Kk Cleaning device sealing method
JP5111091B2 (en) * 2007-12-18 2012-12-26 サクラ精機株式会社 In-line cleaning device

Also Published As

Publication number Publication date
JPH07243074A (en) 1995-09-19

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