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JPS6357082B2 - - Google Patents
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JPS6357082B2 - - Google Patents

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Publication number
JPS6357082B2
JPS6357082B2 JP55076333A JP7633380A JPS6357082B2 JP S6357082 B2 JPS6357082 B2 JP S6357082B2 JP 55076333 A JP55076333 A JP 55076333A JP 7633380 A JP7633380 A JP 7633380A JP S6357082 B2 JPS6357082 B2 JP S6357082B2
Authority
JP
Japan
Prior art keywords
solvent
drum
dry cleaner
circulation path
recovery device
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
Application number
JP55076333A
Other languages
Japanese (ja)
Other versions
JPS571404A (en
Inventor
Kyomi Yamada
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 JP7633380A priority Critical patent/JPS571404A/en
Publication of JPS571404A publication Critical patent/JPS571404A/en
Publication of JPS6357082B2 publication Critical patent/JPS6357082B2/ja
Granted legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ドライクリーナにおける蒸留器内の
蒸留残渣から揮発性溶剤を回収する方法及び溶剤
回収装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method and a solvent recovery device for recovering volatile solvents from distillation residue in a still in a dry cleaner.

〔従来の技術と課題〕[Conventional technology and issues]

従来のドライクリーナにおける1サイクルのク
リーニング工程は、第2図に示す如く汚染溶剤入
口1より蒸留器2内に流入した汚染溶剤を、傍熱
弁3から加熱部4に供給する傍熱蒸気の大きな熱
量により傍熱蒸留して溶剤ガスをコンデンサ5に
導いて回収しているものである。このサイクルを
1日に10回〜20回繰返すと蒸留器2内に蒸留残渣
が蓄積する。この残渣は油状スラツジといわれる
もので界面活性剤、溶剤、軽油成分、有機酸エス
テル等が混合したものである。
As shown in FIG. 2, the one-cycle cleaning process in a conventional dry cleaner consists of a large amount of heat from indirectly heated steam that supplies contaminated solvent that has flowed into a distiller 2 from a contaminated solvent inlet 1 to a heating section 4 from an indirectly heated valve 3. In this case, the solvent gas is indirectly distilled and then introduced into the condenser 5 for recovery. If this cycle is repeated 10 to 20 times a day, distillation residue will accumulate in the distiller 2. This residue is called oily sludge, and is a mixture of surfactants, solvents, light oil components, organic acid esters, and the like.

一方溶剤中から微細なゴミその他の不純物を除
去するためフイルタ6を取付け、溶剤中に硅藻土
などの微粉末を投入するものであるが、不純物等
の蓄積により硅藻土が目詰りすると1日の最終サ
イクル後に上記蒸留器2内にバルブ7を開いて溶
剤とともに硅藻土を落下せしめる。この硅藻土ス
ラツジは水分、油分、界面活性剤、有機物等の揮
発成分70%と灰分30%の混合物である。しかして
油状スラツジとの混合物が傍熱蒸留に続いて直熱
弁8を開いて水蒸気と溶剤との共沸現象を利用し
て直熱蒸留を行つて溶剤を回収する。
On the other hand, a filter 6 is attached to remove fine dust and other impurities from the solvent, and fine powder such as diatomaceous earth is introduced into the solvent, but if the diatomaceous earth becomes clogged due to accumulation of impurities, After the last cycle of the day, the valve 7 is opened in the distiller 2 to allow diatomaceous earth to fall together with the solvent. This diatomaceous earth sludge is a mixture of 70% volatile components such as water, oil, surfactants, and organic matter, and 30% ash. After the mixture with the oily sludge undergoes indirect distillation, the direct heat valve 8 is opened to perform direct heat distillation using the azeotrope between water vapor and the solvent to recover the solvent.

次いで、蒸留器2の蓋(図示せず)を開いて蒸
留残渣をかき出すが、このとき該残渣中にはまだ
多量の溶剤が含まれ且つ蒸留器内に溶剤が拡散さ
れているため溶剤の損失が大きいとともに嫌臭を
発し作業者に苦痛を与え上記残渣のかき取り操作
を困難にしている。この溶剤損失量はドライクリ
ーナの種類により異なるが、1例をあげると処理
容量20Kg/ワツシヤの1,1,1のトリクロルエ
タン基において蒸留残渣中に含まれる溶剤約2.2
Kgと蒸留器内に拡散している溶剤約1.2Kgの計3.4
Kgが溶剤損失となる。
Next, the lid (not shown) of the distiller 2 is opened to scrape out the distillation residue, but at this time, the residue still contains a large amount of solvent and the solvent is diffused into the distiller, resulting in a loss of solvent. The residue is large and gives off an unpleasant odor, causing pain to workers and making it difficult to scrape off the residue. The amount of solvent loss varies depending on the type of dry cleaner, but to give an example, the amount of solvent contained in the distillation residue in a 1,1,1 trichloroethane group with a processing capacity of 20 kg/washer is approximately 2.2
A total of 3.4 kg and approximately 1.2 kg of the solvent diffused in the distiller.
Kg is the solvent loss.

また、大気中へ溶剤を放出するため大気汚染の
原因となり好ましくない。例えば1,1,1トリ
クロルエタンの労働安全衛生上の許容濃度は
200ppmに対して数万ppm以上の高濃度のものが
かき出し口から排出されていることになる。
In addition, since the solvent is released into the atmosphere, it causes air pollution, which is undesirable. For example, the permissible concentration for occupational safety and health of 1,1,1 trichloroethane is
This means that compared to 200 ppm, a high concentration of tens of thousands of ppm or more is being discharged from the scraping outlet.

なお、パークロルエチレン、R113を使用する
ドライクリーナにおいても同様である。
The same applies to dry cleaners that use perchlorethylene or R113.

本発明は上記事情に鑑みてなされたもので、蒸
留器内に拡散している溶剤ガス及び残渣中に含ま
れる溶剤を回収して溶剤損失量を著しく低減し得
るドライクリーナにおける蒸留器内の溶剤回収方
法及び溶剤回収装置を提供することを目的とす
る。
The present invention has been made in view of the above-mentioned circumstances, and it is possible to recover the solvent gas diffused in the distiller and the solvent contained in the residue, thereby significantly reducing the amount of solvent loss. The purpose of the present invention is to provide a recovery method and a solvent recovery device.

〔課題を解決するための手段〕 本願第1の発明は、ドライクリーナ本体のドラ
ム内に被洗物を入れドラムを回転させながら溶剤
を用いて洗濯する洗濯工程と、同洗濯工程後ドラ
ム内の使用済溶剤を蒸留器に導き溶剤分を蒸留回
収させる脱液工程と、同脱液工程後ドラムに接続
する循環路内に配設した送風機,ヒータ,コンデ
ンサを夫々作動させて被洗物に熱風を吹き付け同
被洗物から蒸発した溶剤ガスを該循環路内のコン
デンサに導き溶剤分を凝縮回収する乾燥工程と、
同乾燥工程に続いてドラム内の溶剤ガスを上記送
風機で溶剤回収装置に導き溶剤分を回収し、その
後新鮮空気をドラム内に導き同ドラム内空気を機
外に排気させる脱臭工程とを具備しうるようにし
たドライクリーナにおいて、蒸留器の蒸留室に蓄
積せる溶剤分を含有するスラツジを加熱し、気化
した溶剤ガスをコンデンサに導いて溶剤分を凝縮
回収し、その後該該蒸留室に新鮮空気を導入する
と共に上記ドライクリーナ本体の循環路に配設さ
れた送風機を作動させて残存溶剤ガスを該循環路
を経由して上記溶剤回収装置に導き溶剤分を回収
してなることを要旨とする。
[Means for Solving the Problems] The first invention of the present application includes a washing process in which the laundry is placed in a drum of a dry cleaner main body and washed using a solvent while rotating the drum, and a washing process in which the laundry in the drum is washed after the washing process. There is a deliquification process in which the used solvent is introduced into a distiller and the solvent is distilled and recovered, and after the deliquification process, the blower, heater, and condenser installed in the circulation path connected to the drum are operated to blow hot air onto the items to be washed. a drying step in which the solvent gas evaporated from the object to be washed is guided to a condenser in the circulation path and the solvent is condensed and recovered;
Following the drying step, the method includes a deodorizing step in which the solvent gas in the drum is guided to the solvent recovery device using the blower to recover the solvent, and then fresh air is introduced into the drum and the air in the drum is exhausted to the outside of the machine. In a wet dry cleaner, the sludge containing the solvent to be accumulated in the distillation chamber of the still is heated, the vaporized solvent gas is led to a condenser to condense and recover the solvent, and then fresh air is introduced into the distillation chamber. At the same time, a blower installed in the circulation path of the dry cleaner body is operated to guide the residual solvent gas through the circulation path to the solvent recovery device and recover the solvent. .

本願第2の発明は、ドライクリーナ本体のドラ
ム内に被洗物を入れドラムを回転させながら溶剤
を用いて洗濯する洗濯手段と、洗濯工程後ドラム
内の使用済溶剤を蒸留器に導き溶剤分を蒸留回収
させる脱液手段と、脱液工程後ドラムに接続する
循環路内に配設した送風機,ヒータ,コンデンサ
を夫々作動させて被洗物に熱風を吹き付け同被洗
物から蒸発した溶剤ガスを該循環路内のコンデン
サに導き溶剤分を凝縮回収する乾燥手段と、乾燥
工程に続いてドラム内の溶剤ガスを上記送風機で
溶剤回収装置に導き溶剤分を回収し、その後新鮮
空気をドラム内に導き同ドラム内空気を機外に排
気させる脱臭手段とを具備しうるようにしたドラ
イクリーナにおいて、蒸留器の蒸留室を溶剤回収
装置に連絡する上記ドライクリーナ本体の循環路
に配設された送風機の吸引側に臨んで開口する第
1ダクトを介して同循環路に接続すると共に、第
2ダクトを介してコンデンサに接続し、かつ該蒸
留室に逆止弁を介して新鮮空気取入口を設けてな
ることを要旨とする。
The second invention of the present application includes a washing means for placing the laundry in a drum of the main body of a dry cleaner and washing the laundry using a solvent while rotating the drum, and a method for guiding the used solvent in the drum to a distiller after the washing process and dissolving the solvent. After the deliquification process, a blower, a heater, and a condenser installed in the circulation path connected to the drum are operated to blow hot air onto the items to be washed, and the solvent gas evaporated from the items to be washed is removed. A drying means for guiding the solvent to a condenser in the circulation path and condensing and recovering the solvent, and following the drying process, the solvent gas in the drum is guided by the blower to the solvent recovery device to recover the solvent, and then fresh air is introduced into the drum. The dry cleaner is equipped with a deodorizing means for guiding the air inside the drum to the outside of the machine, and is arranged in the circulation path of the dry cleaner main body that connects the distillation chamber of the distiller to the solvent recovery device. It is connected to the circulation path through a first duct that opens facing the suction side of the blower, and is connected to the condenser through a second duct, and a fresh air intake is connected to the distillation chamber through a check valve. The main point is to establish the following.

〔作用〕[Effect]

本発明に係るドライクリーナにおける蒸留器内
の溶剤回収方法及び溶剤回収装置によれば、ドラ
ム内及び衣類に残存する溶剤ガスを送風機などに
よりドラム内から完全に排出することができ、溶
剤回収による利益が向上する。また、大気中に溶
剤を放出することがないため、大気汚染を防止し
環境衛生上の点でも好ましいものとなる。
According to the solvent recovery method and solvent recovery device in a distiller in a dry cleaner according to the present invention, the solvent gas remaining in the drum and on clothes can be completely discharged from the drum using a blower or the like, and benefits from solvent recovery can be obtained. will improve. In addition, since no solvent is released into the atmosphere, air pollution is prevented, which is preferable in terms of environmental hygiene.

〔実施例〕〔Example〕

以下、本発明の一実施例について第1図を参照
して説明する。ここで、第1図は本発明に係るド
ライクリーナにおける溶剤回収装置の一例を示す
説明図である。まず、この溶剤回収装置について
説明する。
Hereinafter, one embodiment of the present invention will be described with reference to FIG. Here, FIG. 1 is an explanatory diagram showing an example of a solvent recovery device in a dry cleaner according to the present invention. First, this solvent recovery device will be explained.

図中の11はドライクリーナ本体であり、該ド
ライクリーナ本体11のドラム12に被洗物が入
れられ溶剤により洗濯されるようになつている。
前記ドラム12には塵埃フイルタ13,送風機1
4,ヒータ15,水冷コンデンサ16及びダンパ
17を有した循環路18が接続されている。ここ
で、前記送風機14,ヒータ15,水冷コンデン
サ16を夫々作動させると、被洗物に熱風が吹付
けられ、被洗物から蒸発した溶剤ガスが循環路1
8内の水冷コンデンサ16に導かれ、溶剤分を凝
縮回収するようになつている。前記送風機14の
吸引側には、仕切弁19を介装した第1ダクト2
0を介して蒸留器21が接続されている。この蒸
留器21は、洗濯ドラム12内に残された使用済
溶剤を導いて溶剤分を回収する働きをする。前記
蒸留器21には、残留残渣22を加熱する加熱室
23が設けられている。前記蒸留器21には仕切
弁24を介して溶剤フイルタ25が接続され、該
溶剤フイルタ25は前記ドライクリーナ本体11
と接続されている。前記蒸留器21の蒸留室(図
示せず)には、第2ダクト26を介してコンデン
サ27が接続されている。前記蒸留器21には、
逆止弁28を介装した新鮮空気取入口29が設け
られている。前記蒸留器21の上部,溶剤フイル
タ25の底部には、夫々ポンプ30,ボタントラ
ツプ31を介装したダクトを介して前記ドラム1
2に接続されている。
Reference numeral 11 in the figure is a dry cleaner main body, and articles to be washed are placed in a drum 12 of the dry cleaner main body 11 and washed using a solvent.
The drum 12 is equipped with a dust filter 13 and a blower 1.
4, a circulation path 18 having a heater 15, a water-cooled condenser 16, and a damper 17 are connected. Here, when the blower 14, heater 15, and water-cooled condenser 16 are operated, hot air is blown onto the items to be washed, and the solvent gas evaporated from the items to be washed is transferred to the circulation path 1.
The solvent is guided to a water-cooled condenser 16 in the 8, and the solvent is condensed and recovered. On the suction side of the blower 14, there is a first duct 2 with a gate valve 19 interposed therein.
A distiller 21 is connected via 0. The distiller 21 functions to guide the used solvent left in the washing drum 12 and recover the solvent. The distiller 21 is provided with a heating chamber 23 for heating the residual residue 22. A solvent filter 25 is connected to the distiller 21 via a gate valve 24, and the solvent filter 25 is connected to the dry cleaner main body 11.
is connected to. A condenser 27 is connected to a distillation chamber (not shown) of the distiller 21 via a second duct 26. The distiller 21 includes:
A fresh air intake 29 with a check valve 28 interposed therein is provided. The drum 1 is connected to the top of the distiller 21 and the bottom of the solvent filter 25 through ducts equipped with a pump 30 and a button trap 31, respectively.
Connected to 2.

前記ドラム12の排出口12aには、第3ダク
ト32を介して冷凍回収装置33の入口部33a
が接続されている。一方、この冷凍回収装置33
の出口部33bは、第4ダクト34を介して前記
ドラム12に接続されている。ここで、前記冷凍
回収装置33は蓄冷式クーラ35を内蔵し、この
蓄冷式クーラ35は冷凍機36と冷凍回路37で
連結される蓄冷体を−20℃程度に冷却している。
また、上記冷凍回収装置33の上部室33cには
前述した入口部33aが設けられ、ここに取付け
られた前記第3ダクト32は制御弁38,39を
装着している。一方の制御弁37は蒸気入口部3
3aを開閉自在に制御するものであり、他方の制
御弁39は排気口39aを開閉して機外と第3ダ
クト32内とを連通、閉塞するものである。前記
冷凍回収装置33の下部室33dには上記出口部
33bが設けられ、ここに取付けた第4ダクト3
4は制御弁40,41が装着されている。ここ
で、一方の制御弁40は新鮮な空気取入口40a
を開閉している機外と第4ダクト34内とを連
通、閉塞するものである。上記下部室33には凝
縮液集合装置42が設けられ、水分離器43,溶
剤タンク44と接続している。
An inlet 33a of a frozen recovery device 33 is connected to the discharge port 12a of the drum 12 via a third duct 32.
is connected. On the other hand, this frozen recovery device 33
The outlet portion 33b of is connected to the drum 12 via a fourth duct 34. Here, the frozen recovery device 33 has a built-in regenerator cooler 35, and the regenerator 35 cools a regenerator connected to a refrigerator 36 through a refrigerating circuit 37 to about -20°C.
Further, the upper chamber 33c of the frozen recovery device 33 is provided with the aforementioned inlet portion 33a, and the third duct 32 attached thereto is equipped with control valves 38 and 39. One control valve 37 is connected to the steam inlet section 3
The other control valve 39 opens and closes the exhaust port 39a to communicate and close the outside of the machine and the inside of the third duct 32. The lower chamber 33d of the frozen recovery device 33 is provided with the outlet portion 33b, and the fourth duct 3 attached thereto
4 is equipped with control valves 40 and 41. Here, one control valve 40 is a fresh air intake port 40a.
The outside of the machine, which is opened and closed, and the inside of the fourth duct 34 are communicated and closed. A condensate collection device 42 is provided in the lower chamber 33 and connected to a water separator 43 and a solvent tank 44 .

こうした溶剤回収装置は、蒸留器21の蒸留室
を冷凍回収装置33に連絡するドライクリーナ本
体11の循環路18に配設された送風機14の吸
引側に第1ダクト20を介して接続すると共に、
第2ダクト20を介してコンデンサに接続し、か
つ該蒸留室に逆止弁28を介して新鮮空気取入口
29を設けた構造となつているため、ドラム12
内及び衣類に残存する溶剤ガスを送風機14など
によりドラム12内から完全に排出することがで
き、溶剤回収による利益が向上する。また、大気
中に溶剤を放出することがないため、大気汚染を
防止し環境衛生上の点でも好ましい。
Such a solvent recovery device connects the distillation chamber of the distiller 21 via the first duct 20 to the suction side of the blower 14 disposed in the circulation path 18 of the dry cleaner main body 11 that communicates with the freezing recovery device 33.
The drum 12 is connected to the condenser through the second duct 20, and the fresh air intake port 29 is provided in the distillation chamber through the check valve 28.
The solvent gas remaining inside the drum 12 and on the clothes can be completely discharged from the drum 12 by the blower 14 or the like, and the profits from solvent recovery are improved. Furthermore, since no solvent is released into the atmosphere, air pollution can be prevented, which is preferable in terms of environmental hygiene.

次に、上述した溶剤回収装置により1,1,1
トリクロルエタンを使用して蒸留器21内の溶剤
を回収する場合について説明する。
Next, 1,1,1
A case will be described in which the solvent in the distiller 21 is recovered using trichloroethane.

本発明方法では、洗濯ドラム12の排出口12
aより排出される溶剤ガスを第3ダクト32を経
て溶剤液とガス分とに凝縮分離する冷凍回収装置
33に導き、ここで凝縮した溶剤液を水分離器4
2に導いて水分と分離せしめて回収すると共に分
離したガス分は第4ダクト34を経て上記洗濯ド
ラム12内に戻す循環乾燥工程と、循環乾燥工程
後、冷凍回収装置33と上記第3ダクト32及び
第4ダクト34との連絡を遮断(制御弁38,3
9,40,41は2点鎖線の状態にする)して第
4ダクト34から洗濯ドラム12内に新鮮な空気
を供給し該空気を第3ダクト32を経て機外に排
気させる脱臭工程とにより、ドライクリーナ本体
11及び衣類に残存する溶剤を回収するものであ
る。
In the method of the present invention, the discharge port 12 of the washing drum 12
The solvent gas discharged from a is guided through the third duct 32 to a freezing recovery device 33 where it is condensed and separated into a solvent liquid and a gas component, and the condensed solvent liquid is passed through a water separator 4.
2, where the gas is separated from moisture and recovered, and the separated gas is returned to the washing drum 12 through the fourth duct 34, and after the circulation drying process, the freezing recovery device 33 and the third duct 32 and cut off communication with the fourth duct 34 (control valves 38, 3
9, 40, and 41 are indicated by two-dot chain lines), fresh air is supplied from the fourth duct 34 into the washing drum 12, and the air is exhausted outside the machine through the third duct 32. , to recover the solvent remaining in the dry cleaner main body 11 and clothes.

一方、所定のワツシヤ数(例えば15ワツシヤ/
日)に達し溶剤フイルタ24内のフイルタ圧力が
上昇すると仕切弁24を開き溶剤フイルタ25内
の溶剤と硅藻土を蒸留器21内に落下せしめ、従
来通りの所定蒸留工程を行つて可能な限りコンデ
ンサ27で溶剤ガスを凝縮回収する。
On the other hand, a predetermined number of washers (for example, 15 washers/
When the filter pressure in the solvent filter 24 increases, the gate valve 24 is opened and the solvent and diatomaceous earth in the solvent filter 25 are allowed to fall into the distiller 21, and the conventional prescribed distillation process is carried out as much as possible. A condenser 27 condenses and recovers the solvent gas.

次いで、ダンパ17を開き、制御弁38,40
が“開”、制御弁39,41が“閉”(新鮮空気取
入口41a及び排気口39aは閉じている)の状
態で、水冷コンデンサ15及び送風機14を作動
し、ヒータ15を停止し仕切弁24を開くと、蒸
留器21内に拡散している溶剤ガスが第1ダクト
20、塵埃フイルタ13、送風機14、水冷コン
デンサ15、第3ダクト32を経て蓄冷式クーラ
35に導かれ凝縮回収される。更に、この凝縮回
収による体積減少分が負圧となつて蒸留器21内
に逆止弁28を経て新鮮な空気が取入れられ、
次々に蒸留器21内の拡散溶剤ガスが蓄冷式クー
ラ35へ導かれると共に、蒸留残渣22中に含ま
れる溶剤が蒸留を続け蓄冷式クーラ35へ導かれ
凝縮回収される。
Next, the damper 17 is opened and the control valves 38, 40 are opened.
is "open" and the control valves 39 and 41 are "closed" (the fresh air intake port 41a and the exhaust port 39a are closed), the water-cooled condenser 15 and the blower 14 are operated, the heater 15 is stopped, and the gate valve is closed. 24 is opened, the solvent gas diffused in the distiller 21 is led to the regenerator cooler 35 via the first duct 20, dust filter 13, blower 14, water cooling condenser 15, and third duct 32, where it is condensed and recovered. . Furthermore, the volume reduction due to this condensation and recovery becomes negative pressure, and fresh air is taken into the distiller 21 via the check valve 28.
The diffused solvent gas in the distiller 21 is successively led to the regenerator cooler 35, and the solvent contained in the distillation residue 22 continues to be distilled and is led to the regenerator cooler 35 where it is condensed and recovered.

蒸留残渣22中の溶剤を回収したか否かを判断
するには、冷凍回収装置33の下部室33dから
洗濯ドラム21へ戻る空気温度(通常約−20℃)
をチエツクすることによつて行う。溶剤回収後蒸
留器21の取り出し蓋を開いて残渣をかき出せば
よい。
In order to judge whether or not the solvent in the distillation residue 22 has been recovered, the temperature of the air returning from the lower chamber 33d of the freezing recovery device 33 to the washing drum 21 (usually about -20°C)
This is done by checking. After recovering the solvent, the removal lid of the distiller 21 is opened and the residue is scraped out.

本発明方法によれば、蒸留器21の蒸留室に蓄
積せる溶剤分を含有するスラツジを加熱し、気化
した溶剤ガスをコンデンサ19に導いて溶剤分を
凝縮回収し、その後該該蒸留室に新鮮空気を導入
すると共に上記ドライクリーナ本体11の循環路
18に配設された送風機14を作動させて残存溶
剤ガスを該循環路18を経由して冷凍回収装置3
3に導き溶剤分を回収するため、ドラム12内及
び衣類に残存する溶剤ガスを送風機14などによ
りドラム12内から完全に排出することができ、
溶剤回収による利益が向上する。また、大気中に
溶剤を放出することがないため、大気汚染を防止
し環境衛生上の点でも好ましい。
According to the method of the present invention, the sludge containing the solvent to be accumulated in the distillation chamber of the distiller 21 is heated, the vaporized solvent gas is led to the condenser 19 to condense and recover the solvent, and then the sludge is freshly stored in the distillation chamber. At the same time as introducing air, the blower 14 disposed in the circulation path 18 of the dry cleaner main body 11 is operated, and the residual solvent gas is passed through the circulation path 18 to the freezing recovery device 3.
3 to recover the solvent, the solvent gas remaining in the drum 12 and on the clothes can be completely discharged from the drum 12 using a blower 14 or the like.
Increased profits from solvent recovery. Furthermore, since no solvent is released into the atmosphere, air pollution can be prevented, which is preferable in terms of environmental hygiene.

なお、上記実施例では、溶剤回収装置として冷
凍回収装置を用いた場合について述べたが、これ
に限らず、第3図に示す如く活性炭回収装置45
をドラム12の排出口12aに接続したものでも
よい。
In the above embodiment, the case where a frozen recovery device is used as the solvent recovery device is described, but the invention is not limited to this, and an activated carbon recovery device 45 as shown in FIG.
may be connected to the discharge port 12a of the drum 12.

また、上記実施例において、第4ダクト34か
らの洗濯ドラム15への空気流入口を、ヒータ1
4の前段部イに接続し、乾燥工程においてヒータ
14の熱により循環空気を加温して衣料に供給す
ることにより衣料から溶剤は追出され溶剤回収率
は向上する。
In the above embodiment, the air inlet from the fourth duct 34 to the washing drum 15 is connected to the heater 1.
In the drying process, the circulating air is heated by the heat of the heater 14 and supplied to the clothing, thereby expelling the solvent from the clothing and improving the solvent recovery rate.

〔発明の効果〕〔Effect of the invention〕

以上詳述した如く本発明によれば、蒸留器内に
拡散する溶剤及び残渣中の溶剤を効率よく回収し
うるため溶剤のロスが著しく低減し、溶剤回収に
よる利益が格段に向上するとともに、大気中に溶
剤を放出することを回避して大気汚染を防止し環
境衛生上極めて優れたドライクリーナにおける蒸
留器内の溶剤回収方法及び溶剤回収装置を提供で
きる。
As detailed above, according to the present invention, the solvent diffused in the distiller and the solvent in the residue can be efficiently recovered, so the loss of solvent is significantly reduced, the profits from solvent recovery are significantly improved, and the It is possible to provide a method and a solvent recovery device for recovering a solvent in a distiller in a dry cleaner, which prevents air pollution by avoiding the release of solvent into a dry cleaner, and is extremely superior in terms of environmental hygiene.

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

第1図は本発明に係る溶剤回収装置の説明図、
第2図は従来の溶剤回収装置の概略説明図、第3
図は本発明に係る溶剤回収装置のその他の例を示
すブロツク図である。 11……ドライクリーナ本体、12……ドラ
ム、13……塵埃フイルタ、14……送風機、1
5……ヒータ、16……水冷コンデンサ、18…
…循環路、20……第1ダクト、21……蒸留
器、22……蒸留残渣、25……溶剤フイルタ、
26……第2ダクト、28……逆止弁、32……
第3ダクト、33……冷凍回収装置、34……第
4ダクト、43……水分離器、44……溶剤タン
ク。
FIG. 1 is an explanatory diagram of a solvent recovery device according to the present invention,
Figure 2 is a schematic explanatory diagram of a conventional solvent recovery device;
The figure is a block diagram showing another example of the solvent recovery device according to the present invention. 11...Dry cleaner body, 12...Drum, 13...Dust filter, 14...Blower, 1
5...Heater, 16...Water-cooled condenser, 18...
... Circulation path, 20 ... First duct, 21 ... Distiller, 22 ... Distillation residue, 25 ... Solvent filter,
26...Second duct, 28...Check valve, 32...
Third duct, 33... Refrigeration recovery device, 34... Fourth duct, 43... Water separator, 44... Solvent tank.

Claims (1)

【特許請求の範囲】 1 ドライクリーナ本体のドラム内に被洗物を入
れドラムを回転させながら溶剤を用いて洗濯する
洗濯工程と、同洗濯工程後ドラム内の使用済溶剤
を蒸留器に導き溶剤分を蒸留回収させる脱液工程
と、同脱液工程後ドラムに接続する循環路内に配
設した送風機、ヒータ、コンデンサを夫々作動さ
せて被洗物に熱風を吹き付け同被洗物から蒸発し
た溶剤ガスを該循環路内のコンデンサに導き溶剤
分を凝縮回収する乾燥工程と、同乾燥工程に続い
てドラム内の溶剤ガスを上記送風機で溶剤回収装
置に導き溶剤分を回収し、その後新鮮空気をドラ
ム内に導き同ドラム内空気を機外に排気させる脱
臭工程とを具備しうるようにしたドライクリーナ
において、蒸留器の蒸留室に蓄積せる溶剤分を含
有するスラツジを加熱し、気化した溶剤ガスをコ
ンデンサに導いて溶剤分を凝縮回収し、その後該
該蒸留室に新鮮空気を導入すると共に上記ドライ
クリーナ本体の循環路に配設された送風機を作動
させて残存溶剤ガスを該循環路を経由して上記溶
剤回収装置に導き溶剤分を回収してなることを特
徴とするドライクリーナにおける蒸留器内の溶剤
回収方法。 2 ドライクリーナ本体のドラム内に被洗物を入
れドラムを回転させながら溶剤を用いて洗濯する
洗濯手段と、洗濯工程後ドラム内の使用済溶剤を
蒸留器に導き溶剤分を蒸留回収させる脱液手段
と、脱液工程後ドラムに接続する循環路内に配設
した送風機、ヒータ、コンデンサを夫々作動させ
て被洗物に熱風を吹き付け同被洗物から蒸発した
溶剤ガスを該循環路内のコンデンサに導き溶剤分
を凝縮回収する乾燥手段と、乾燥工程に続いてド
ラム内の溶剤ガスを上記送風機で溶剤回収装置に
導き溶剤分を回収し、その後新鮮空気をドラム内
に導き同ドラム内空気を機外に排気させる脱臭手
段とを具備しうるようにしたドライクリーナにお
いて、蒸留器の蒸留室を溶剤回収装置に連絡する
上記ドライクリーナ本体の循環路に配設された送
風機の吸引側に臨んで開口する第1ダクトを介し
て同循環路に接続すると共に、第2ダクトを介し
てコンデンサに接続し、かつ該蒸留室に逆止弁を
介して新鮮空気取入口を設けてなることを特徴と
するドライクリーナにおける蒸留器内の溶剤回収
装置。
[Claims] 1. A washing process in which the laundry is placed in the drum of the dry cleaner body and washed using a solvent while rotating the drum, and after the washing process, the used solvent in the drum is transferred to a distiller and the solvent is removed. There is a deliquification process in which the liquid is distilled and recovered, and after the deliquification process, a blower, a heater, and a condenser installed in the circulation path connected to the drum are activated to blow hot air onto the items to be washed, which evaporates from the items. There is a drying process in which the solvent gas is guided to the condenser in the circulation path and the solvent is condensed and recovered.Following the drying process, the solvent gas in the drum is guided by the blower to the solvent recovery device to recover the solvent, and then fresh air is introduced. The dry cleaner is equipped with a deodorizing process in which air is introduced into the drum and the air inside the drum is exhausted outside the machine.The sludge containing the solvent that is accumulated in the distillation chamber of the still is heated, and the vaporized solvent is removed. The gas is led to a condenser to condense and recover the solvent, and then fresh air is introduced into the distillation chamber, and a blower installed in the circulation path of the dry cleaner body is operated to remove the remaining solvent gas through the circulation path. A method for recovering a solvent in a distiller in a dry cleaner, characterized in that the solvent is introduced into the solvent recovery device via the solvent recovery device and the solvent is recovered. 2. A washing method in which the items to be washed are placed in the drum of the dry cleaner body and washed using a solvent while rotating the drum, and a deliquification method in which the used solvent in the drum is led to a distiller after the washing process and the solvent is distilled and recovered. After the deliquoring process, a blower, a heater, and a condenser installed in the circulation path connected to the drum are operated to blow hot air onto the items to be washed, and the solvent gas evaporated from the items to be washed is removed from the circulation path. A drying means that condenses and recovers the solvent gas that is guided to the condenser, and following the drying process, the solvent gas in the drum is guided to the solvent recovery device using the above-mentioned blower to recover the solvent gas, and then fresh air is introduced into the drum and the air inside the drum is removed. In a dry cleaner which can be equipped with a deodorizing means for exhausting water to the outside of the machine, the dry cleaner faces the suction side of a blower disposed in the circulation path of the dry cleaner main body that connects the distillation chamber of the distiller to the solvent recovery device. The distillation chamber is connected to the circulation path through a first duct that opens at , and is connected to the condenser through a second duct, and a fresh air intake is provided in the distillation chamber through a check valve. A solvent recovery device in a distiller in a dry cleaner.
JP7633380A 1980-06-06 1980-06-06 Method and apparatus for recovering solvent in still in dry cleaner Granted JPS571404A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7633380A JPS571404A (en) 1980-06-06 1980-06-06 Method and apparatus for recovering solvent in still in dry cleaner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7633380A JPS571404A (en) 1980-06-06 1980-06-06 Method and apparatus for recovering solvent in still in dry cleaner

Publications (2)

Publication Number Publication Date
JPS571404A JPS571404A (en) 1982-01-06
JPS6357082B2 true JPS6357082B2 (en) 1988-11-10

Family

ID=13602425

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7633380A Granted JPS571404A (en) 1980-06-06 1980-06-06 Method and apparatus for recovering solvent in still in dry cleaner

Country Status (1)

Country Link
JP (1) JPS571404A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112057886B (en) * 2020-09-09 2022-03-25 山东交通学院 On-site volatile solvent recovery device and recovery method

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54160565A (en) * 1978-06-09 1979-12-19 Okamura Corp Simple solvent recovery apparatus

Also Published As

Publication number Publication date
JPS571404A (en) 1982-01-06

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