JP2534606Y2 - Distillation residue treatment equipment - Google Patents

Distillation residue treatment equipment

Info

Publication number
JP2534606Y2
JP2534606Y2 JP1995008014U JP801495U JP2534606Y2 JP 2534606 Y2 JP2534606 Y2 JP 2534606Y2 JP 1995008014 U JP1995008014 U JP 1995008014U JP 801495 U JP801495 U JP 801495U JP 2534606 Y2 JP2534606 Y2 JP 2534606Y2
Authority
JP
Japan
Prior art keywords
distillation residue
solvent
container
distillation
activated carbon
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
JP1995008014U
Other languages
Japanese (ja)
Other versions
JPH08168U (en
Inventor
彰二 萩原
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP1995008014U priority Critical patent/JP2534606Y2/en
Publication of JPH08168U publication Critical patent/JPH08168U/en
Application granted granted Critical
Publication of JP2534606Y2 publication Critical patent/JP2534606Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】本考案はドライクリーニング装置
に利用する蒸留残渣処理装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a distillation residue processing apparatus used for a dry cleaning apparatus.

【0002】[0002]

【従来の技術】ドライクリーニングの工程における蒸留
の意味を明確にするため、ドライクリーニング装置の従
来の運転工程を要約して図2及び図3乃至図6に示す
と、図2は運転全工程を、図3〜図6は各工程の内容を
要約して示したものである。
2. Description of the Related Art In order to clarify the meaning of distillation in the process of dry cleaning, the conventional operation steps of a dry cleaning apparatus are summarized and shown in FIGS. 2 and 3 to 6. FIG. 3 to 6 summarize the contents of each step.

【0003】先ず図2において運転工程の概要を説明す
ると、ドライクリーニング装置に投入された衣料は、予
洗、高速遠心脱液、本洗、高速遠心脱液、乾燥及び脱臭
の工程を経て、クリーニングされて機外に取り出され
る。しかしこの場合の予洗に使用された溶剤は汚染の程
度が大きいため、蒸留器へ送られて蒸留して再使用され
る。なお、本洗に使用された溶剤は、蒸留されずにその
まま元のタンクに戻され、次回の予洗に使用されること
が多い。
First, the outline of the operation process will be described with reference to FIG. 2. Clothes put into a dry cleaning device are cleaned through pre-washing, high-speed centrifugal dewatering, main washing, high-speed centrifugal dewatering, drying and deodorizing processes. Out of the machine. However, the solvent used for pre-washing in this case has a high degree of contamination and is sent to a still to be distilled and reused. The solvent used for the main washing is returned to the original tank without being distilled, and is often used for the next prewash.

【0004】次に図3〜図6により従来のドライクリー
ニング装置における運転工程を説明すると、先ず図3は
予洗の場合で、衣料1を処理槽2内の回転ドラム3に投
入し、タンク4から溶剤を汲み上げポンプで循環しなが
ら洗浄する。
Next, the operation steps of the conventional dry cleaning apparatus will be described with reference to FIGS. 3 to 6. First, FIG. 3 shows a case of pre-washing, in which clothing 1 is put into a rotating drum 3 in a processing tank 2 and Wash the solvent while pumping and circulating it with a pump.

【0005】次に図4は排脱液の場合で、予洗後回転ド
ラム3を高速回転させて衣料を脱液すると共に、汚れた
溶剤をポンプ5で蒸留器6へ送る。蒸留器へ排液された
溶剤は、蒸気又は電気により加熱され、溶剤は蒸発して
冷却水7で冷却されるコンデンサ8で凝縮液化され、水
分離器9を経由して溶剤タンク10へ戻る。
Next, FIG. 4 shows a case of drainage, in which after the pre-washing, the rotating drum 3 is rotated at a high speed to drain the clothes, and the dirty solvent is sent to the still 6 by the pump 5. The solvent discharged to the still is heated by steam or electricity, and the solvent is evaporated and condensed and liquefied by a condenser 8 cooled by cooling water 7, and returns to a solvent tank 10 via a water separator 9.

【0006】次に図5は本洗の場合であり、再度溶剤を
タンク4から汲み上げ、さらにタンク10から補充し、
フィルタ11を通しながら洗浄する。またこの時洗剤1
2を投入する。洗浄後、溶剤はすべてタンク4へ戻る。
Next, FIG. 5 shows a case of the main washing, in which the solvent is again pumped from the tank 4 and further replenished from the tank 10,
Washing is performed while passing through the filter 11. Also at this time detergent 1
Input 2. After the washing, all the solvent returns to the tank 4.

【0007】次に図6は乾燥の場合で、ファン13が回
り系内に空気流を生じさせると、溶剤ガスは糸くずを捕
捉するリントフィルタ14を通り冷凍機又は水で冷却さ
れ、エアクーラ15で液化し回収される。空気は冷凍機
の排熱利用のプリヒータ16で暖められ、さらに図示し
ないサーモスタットの設定値までエアヒータ17で加熱
されて衣料に吹き当たり、溶剤を蒸発させる。また脱臭
では、ファン13の風量を落とし、またエアヒータ17
も切ってエアクーラ15での深冷によりガス濃度を下げ
る。
Next, FIG. 6 shows a case of drying. When the fan 13 generates an air flow in the surrounding system, the solvent gas passes through a lint filter 14 for catching lint, is cooled by a refrigerator or water, and is cooled by an air cooler 15. Liquefied and recovered. The air is warmed by a preheater 16 utilizing the exhaust heat of the refrigerator, and further heated by an air heater 17 to a set value of a thermostat (not shown) to blow against clothing to evaporate the solvent. In the deodorization, the air volume of the fan 13 is reduced,
The gas concentration is lowered by deep cooling in the air cooler 15.

【0008】[0008]

【考案が解決しようとする課題】前記図3〜図6におい
て、予洗に使用された溶剤は、蒸留器6へ送られて蒸留
されるが、蒸留末期には汚れ及び洗剤成分などが不揮発
分として液状、あるいは汚泥状で蒸留残渣として蒸留器
内に残る。従来はこの蒸留残渣を機外へ排出するため、
毎日1回以上図7に示す作業が必要であった。即ち、蒸
留器掃除口扉(図示せず)を開き、蒸留器6の底部20
の蒸留残渣21を、掻き出し棒22を用いて受皿23へ
掻き出す必要があった。受皿23に掻き出された蒸留残
渣は、産業廃棄物処理業者への処理を委託するために、
更に運搬に便利な容器26へ移す必要があった。なお、
前述の掻き出し棒22を用いて、受皿23へ蒸留残渣を
掻き出す際には、蒸留器内に残存する溶剤ガス24及び
水蒸気25が流出して作業環境を汚染し、異臭を発した
り、ひいてはドライクリーニング溶剤による大気汚染、
地下水汚染の原因の1つともなる可能性があった。
In FIG. 3 to FIG. 6, the solvent used for pre-washing is sent to the still 6 and distilled, but at the end of the distillation, dirt and detergent components are removed as non-volatile components. It remains in the still as a distillation residue in the form of a liquid or sludge. Conventionally, in order to discharge this distillation residue outside the machine,
The operation shown in FIG. 7 was required at least once a day. That is, the still opening door (not shown) of the still is opened, and the bottom 20 of the still 6 is opened.
It was necessary to scrape out the distillation residue 21 into the tray 23 using the scraping rod 22. The distillation residue scraped out in the saucer 23 is entrusted to an industrial waste disposal company for treatment.
Furthermore, it was necessary to transfer to the container 26 convenient for transportation. In addition,
When the distillation residue is scraped out to the tray 23 using the scraping rod 22 described above, the solvent gas 24 and water vapor 25 remaining in the still still flow out, contaminating the working environment, generating an unpleasant odor, and thus dry cleaning. Air pollution by solvents,
It could be one of the causes of groundwater pollution.

【0009】またドライクリーニング溶剤としてフッ素
系溶剤のフロンR113(CClF2 CCl2 F )を使用する
機械においては、オゾン層破壊を防止するための全世界
的フロン規制の中にあってフロンの消費量を低減させる
ことは必要不可欠のことであり、更に塩素系溶剤のテト
ラクロロエチレン(CCl2 ・ CCl2 )、あるいは1.1.1-ト
リクロロエタン(CH3CCl3 )を使用する機械において
は、大気汚染及び地下水汚染を防止するためにも、これ
らの溶剤消費量を可能な限り低減させることは、フロン
R113の場合と同様に必要不可欠のことである。従っ
てこのような観点からも、蒸留器掃除の際に掃除口から
溶剤ガスが機外に流出し、再び捕捉不可能な状態で、大
気に拡散するのを防ぐ必要が生じてきている。前記の如
く蒸留器からの蒸留残渣を排出する際に、蒸留器内に残
存する溶剤ガスを作業環境に拡散させることなく、蒸留
残渣のみを容器に回収すること、即ち閉鎖系で蒸留残渣
を回収することは必要不可欠のことであるが、従来は蒸
留残渣排出の際に蒸留器掃除口を開くため、溶剤ガスが
流出して異臭を放つなど、作業環境を汚染していた。
Further, in a machine using a fluorine-based solvent Freon R113 (CClF 2 CCl 2 F) as a dry-cleaning solvent, the consumption of Freon in the worldwide Freon regulations for preventing ozone layer destruction is considered. It is indispensable to reduce air pollution and air pollution and groundwater pollution in machines that use the chlorinated solvent tetrachloroethylene (CCl 2 · CCl 2 ) or 1.1.1-trichloroethane (CH 3 CCl 3 ). It is indispensable to reduce the consumption of these solvents as much as possible, as in the case of Freon R113, in order to prevent the above problem. Therefore, from such a viewpoint, it is necessary to prevent the solvent gas from flowing out of the apparatus through the cleaning port during cleaning of the still and diffusing into the atmosphere in a state in which the solvent gas cannot be captured again. When discharging the distillation residue from the distillation apparatus as described above, the solvent gas remaining in the distillation apparatus is not diffused into the working environment, and only the distillation residue is recovered in the container, that is, the distillation residue is recovered in a closed system. Although it is indispensable to do so, the work environment is conventionally polluted, such as the solvent gas flowing out and emitting an odor due to the opening of the distillery cleaner when discharging the distillation residue.

【0010】また蒸留残渣を受け入れる容器は、入手性
が容易であり、その後の処理を産業廃棄物処理業者へ委
託する際の取り扱いも容易なものであることが必要であ
るが、従来は満足できる蒸留残渣の処理手段がなかっ
た。一般に蒸留残渣排出作業が容易であることが、婦女
子作業者の増加と共に従来以上に必要となってきている
が、従来の蒸留器の掃除口を開いての掻き出し作業は、
異臭を放つため機械の取り扱い上最も嫌な作業であり、
また掃除口を開かずに蒸留器底部にある仕切弁を開いて
液状蒸留残渣を排出する場合でも、異臭の拡散を防止す
ることはできなかった。しかも従来は、蒸留器掃除の際
に蒸留器内に残存する溶剤ガスが掃除口などから機外に
流出し、高価な溶剤をも消失する欠点があった。本考案
は前記従来の課題を解決するために提案されたものであ
る。
[0010] Further, the container for receiving the distillation residue must be easily available and easy to handle when entrusting the subsequent treatment to an industrial waste disposal company, but it has been conventionally satisfactory. There was no means for treating the distillation residue. In general, it is becoming more necessary for the distillation residue discharge work to be easier than ever with the increase in women and women workers.
It is the most unpleasant work in handling the machine because it emits a bad smell,
Also, even when the gate valve at the bottom of the still is opened to discharge the liquid distillation residue without opening the cleaning port, the diffusion of the off-flavor cannot be prevented. In addition, conventionally, there has been a drawback that the solvent gas remaining in the distiller during cleaning of the distiller flows out of the apparatus through a cleaning port or the like, and the expensive solvent is also lost. The present invention has been proposed to solve the above-mentioned conventional problems.

【0011】[0011]

【課題を解決するための手段】このため本考案は、ドラ
イクリーニング装置において、蒸留器と、蒸留残渣を収
容する第1容器と、主として溶剤ガスを収容する第2容
器と、吸引装置とを備え、同蒸留器内の蒸留残渣を吸引
装置の吸込側に発生した負圧で前記第1容器に移送回収
すると共に、同吸引装置の吹出側から流出する溶剤ガス
を含む空気流を活性炭溶剤回収装置を通過させる回路を
設け、空気流中の溶剤ガスを活性炭に吸着させて回収す
るようにしてなるもので、これを課題解決のための手段
とするものである。
SUMMARY OF THE INVENTION Accordingly, the present invention provides a dry cleaning apparatus comprising a still, a first container for storing a distillation residue, a second container for mainly storing a solvent gas, and a suction device. Transferring and collecting the distillation residue in the distillation apparatus into the first container at a negative pressure generated on the suction side of the suction device, and collecting the air stream containing the solvent gas flowing out from the blowing side of the suction device into the activated carbon solvent recovery device. Is provided to allow the solvent gas in the air stream to be adsorbed on the activated carbon and recovered, and this is used as a means for solving the problem.

【0012】[0012]

【作用】既存の活性炭溶剤回収装置を通過した空気は、
活性炭層を通過することにより、基本的には溶剤成分を
含まない状態となり、公害上問題ないため直接大気に排
出する。また蒸留残渣用第1容器は、ドライクリーニン
グ用洗剤の空缶をそのまま使用することができ、数十回
分の残渣を受け入れることが可能であると共に、満杯と
なった容器をそのまま密栓して産業廃棄物処理業者へ渡
すことができる。
[Action] The air that has passed through the existing activated carbon solvent recovery device is
By passing through the activated carbon layer, it basically contains no solvent component, and is discharged directly to the atmosphere because there is no problem in terms of pollution. In addition, the first container for the distillation residue can use an empty can of detergent for dry cleaning as it is, can receive several tens of residues, and closes the full container as it is for industrial waste. Can be handed over to a material processing company.

【0013】[0013]

【実施例】以下本考案を図面の実施例について説明する
と、図1は本考案の実施例を示す。さて図1の実施例に
おいて、蒸留器6の底部に蒸留末期には蒸留残渣21が
存在する。ここで蒸留器6底部の仕切弁40を開き、吸
引装置31のモータ32を起動すると、インペラ33が
回転して吸込側の第2容器35に負圧を発生させ、アダ
プタ30を経由して第1容器25にも負圧を発生させ
る。なお、7は冷却水、8はコンデンサである。蒸留残
渣21は吸引されて第1容器25に移送されると共に、
インペラの高速回転により生じる空気流19は、アダプ
タ30経由で第1容器25内の溶剤ガスのみを第2容器
35へ移送する。なお、アダプタ30は洗剤空缶をその
まま第1容器25として使用するための器具であり、第
1容器25が残渣で満杯になった場合は、別の容器に付
け替えて使用する。また蒸留器の仕切弁42を開放し、
機外から空気を取り入れて蒸留残渣を第1容器25へ移
送し、吸引装置31から吹出る空気流を既存の活性炭溶
剤回収装置45を通過させることにより、空気流中の溶
剤ガスを活性炭45に吸着させて回収する。
FIG. 1 shows an embodiment of the present invention. In the embodiment of FIG. 1, a distillation residue 21 is present at the bottom of the still 6 at the end of distillation. Here, when the gate valve 40 at the bottom of the still 6 is opened and the motor 32 of the suction device 31 is started, the impeller 33 rotates to generate a negative pressure in the second container 35 on the suction side, and the second pressure is passed through the adapter 30. A negative pressure is also generated in one container 25. In addition, 7 is cooling water and 8 is a condenser. The distillation residue 21 is sucked and transferred to the first container 25,
The air flow 19 generated by the high-speed rotation of the impeller transfers only the solvent gas in the first container 25 to the second container 35 via the adapter 30. The adapter 30 is a tool for using the detergent empty can as it is as the first container 25. When the first container 25 is full of residues, it is replaced with another container for use. In addition, the gate valve 42 of the still is opened,
Air is taken in from outside the machine, the distillation residue is transferred to the first container 25, and the air flow blown out from the suction device 31 is passed through the existing activated carbon solvent recovery device 45, so that the solvent gas in the air flow is converted to the activated carbon 45. Collect by adsorption.

【0014】[0014]

【考案の効果】以上詳細に説明した如く、既存の活性炭
溶剤回収装置を通過した空気は、活性炭層を通過するこ
とにより、基本的には溶剤成分を含まない状態となり、
公害上問題ないため直接大気に排出する。また本考案で
は従来の蒸留残渣掻き出し作業に比較して、スイッチ1
つで殆どの残渣を1〜2分の短時間で排出できるため作
業が容易になり、排出後の残渣運搬などの取り扱いも大
幅に改善される。
As described in detail above, the air that has passed through the existing activated carbon solvent recovery device basically contains no solvent component by passing through the activated carbon layer,
Emitted directly to the atmosphere as there is no problem with pollution. In addition, in the present invention, compared with the conventional distillation residue scraping operation, the switch 1 is used.
In addition, since most of the residue can be discharged in a short time of 1 to 2 minutes, the work becomes easy, and handling such as transportation of the residue after the discharge is greatly improved.

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

【図1】本考案の実施例を示す蒸留残渣処理装置のフロ
ーシートである。
FIG. 1 is a flow sheet of a distillation residue treatment apparatus showing an embodiment of the present invention.

【図2】従来のドライクリーニング装置の運転工程を示
すブロック図である。
FIG. 2 is a block diagram showing operation steps of a conventional dry cleaning device.

【図3】従来のドライクリーニング装置の運転工程を詳
細に示す説明図である。
FIG. 3 is an explanatory diagram showing an operation process of a conventional dry cleaning device in detail.

【図4】従来のドライクリーニング装置の運転工程を詳
細に示す説明図である。
FIG. 4 is an explanatory diagram showing an operation process of a conventional dry cleaning device in detail.

【図5】従来のドライクリーニング装置の運転工程を詳
細に示す説明図である。
FIG. 5 is an explanatory diagram showing an operation process of a conventional dry cleaning device in detail.

【図6】従来のドライクリーニング装置の運転工程を詳
細に示す説明図である。
FIG. 6 is an explanatory diagram showing an operation process of a conventional dry cleaning device in detail.

【図7】従来の蒸留残渣掻き出し作業の説明図である。FIG. 7 is an explanatory view of a conventional distillation residue scraping operation.

【符号の説明】[Explanation of symbols]

6 蒸留器 7 冷却水 8 コンデンサ 10 凝縮液 19 空気流 21 蒸留残渣 25 第1容器 30 アダプタ 31 吸引装置 32 モータ 33 インペラ 34 フィルタ 35 第2容器 40,42 仕切弁 45 活性炭溶剤回収装置 6 Distiller 7 Cooling water 8 Condenser 10 Condensate 19 Air flow 21 Distillation residue 25 First container 30 Adapter 31 Suction device 32 Motor 33 Impeller 34 Filter 35 Second container 40, 42 Gate valve 45 Activated carbon solvent recovery device

Claims (1)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 ドライクリーニング装置において、蒸留
器と、蒸留残渣を収容する第1容器と、主として溶剤ガ
スを収容する第2容器と、吸引装置とを備え、同蒸留器
内の蒸留残渣を吸引装置の吸込側に発生した負圧で前記
第1容器に移送回収すると共に、同吸引装置の吹出側か
ら流出する溶剤ガスを含む空気流を活性炭溶剤回収装置
を通過させる回路を設け、空気流中の溶剤ガスを活性炭
に吸着させて回収することを特徴とする蒸留残渣処理装
置。
1. A dry cleaning apparatus, comprising: a distilling device, a first container for storing a distillation residue, a second container for mainly storing a solvent gas, and a suction device, and suctioning the distillation residue in the distillation device. A circuit is provided for transferring and recovering the first container with the negative pressure generated on the suction side of the device and passing the air flow containing the solvent gas flowing out from the discharge side of the suction device through the activated carbon solvent recovery device. A distillation residue treatment apparatus, wherein the solvent gas is recovered by adsorption on activated carbon.
JP1995008014U 1995-08-02 1995-08-02 Distillation residue treatment equipment Expired - Lifetime JP2534606Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1995008014U JP2534606Y2 (en) 1995-08-02 1995-08-02 Distillation residue treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1995008014U JP2534606Y2 (en) 1995-08-02 1995-08-02 Distillation residue treatment equipment

Publications (2)

Publication Number Publication Date
JPH08168U JPH08168U (en) 1996-02-02
JP2534606Y2 true JP2534606Y2 (en) 1997-05-07

Family

ID=18528299

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1995008014U Expired - Lifetime JP2534606Y2 (en) 1995-08-02 1995-08-02 Distillation residue treatment equipment

Country Status (1)

Country Link
JP (1) JP2534606Y2 (en)

Also Published As

Publication number Publication date
JPH08168U (en) 1996-02-02

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