JP2792705B2 - Solvent recovery equipment for dry cleaning equipment - Google Patents
Solvent recovery equipment for dry cleaning equipmentInfo
- Publication number
- JP2792705B2 JP2792705B2 JP2016074A JP1607490A JP2792705B2 JP 2792705 B2 JP2792705 B2 JP 2792705B2 JP 2016074 A JP2016074 A JP 2016074A JP 1607490 A JP1607490 A JP 1607490A JP 2792705 B2 JP2792705 B2 JP 2792705B2
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- solvent
- adsorber
- air
- 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 - Fee Related
Links
- 239000002904 solvent Substances 0.000 title claims description 64
- 238000011084 recovery Methods 0.000 title claims description 13
- 238000005108 dry cleaning Methods 0.000 title claims description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 58
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 22
- 238000001035 drying Methods 0.000 claims description 18
- 238000003795 desorption Methods 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 10
- 230000001877 deodorizing effect Effects 0.000 claims description 7
- 230000008929 regeneration Effects 0.000 claims description 3
- 238000011069 regeneration method Methods 0.000 claims description 3
- 238000011144 upstream manufacturing Methods 0.000 claims description 2
- 238000004332 deodorization Methods 0.000 description 7
- 238000001816 cooling Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- OKTJSMMVPCPJKN-NJFSPNSNSA-N Carbon-14 Chemical class [14C] OKTJSMMVPCPJKN-NJFSPNSNSA-N 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 4
- 238000001179 sorption measurement Methods 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- CYTYCFOTNPOANT-UHFFFAOYSA-N Perchloroethylene Chemical group ClC(Cl)=C(Cl)Cl CYTYCFOTNPOANT-UHFFFAOYSA-N 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
- 229950011008 tetrachloroethylene Drugs 0.000 description 2
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
Landscapes
- Accessory Of Washing/Drying Machine, Commercial Washing/Drying Machine, Other Washing/Drying Machine (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の溶剤ガス機外放出の防止と
コスト低減を図ることができるドライクリーニング装置
の溶剤回収装置に関するものである。Description: BACKGROUND OF THE INVENTION (Field of Industrial Application) The present invention relates to a solvent recovery device of a dry cleaning device capable of preventing the solvent from being released from a dry gas cleaner and reducing costs.
（従来の技術） 従来のドライクリーニング装置は第５図に示すように
構成されており、クリーニングの工程は洗浄工程、脱液
工程、乾燥工程、脱臭工程を順に行っている。(Prior Art) A conventional dry cleaning apparatus is configured as shown in FIG. 5, and a cleaning step includes a cleaning step, a liquid removing step, a drying step, and a deodorizing step in this order.
先ず洗浄工程では、被洗物01をパークロルエチレン、
1.1.1−トリクロルエタン、R11、R113等の揮発性の高い
溶剤に浸漬して汚れを落とす。更に脱液工程では、洗濯
ドラム02を高速回転させて溶剤を遠心分離させる。また
乾燥工程では、クリーニング装置内の空気を循環ファン
03により、水冷式クーラ04及びヒータ05を通過させて洗
濯ドラム02内へと循環させる。First, in the cleaning step, the object to be washed 01 is perchlorethylene,
1.1.1-Soak in highly volatile solvents such as trichloroethane, R11 and R113 to remove dirt. Further, in the liquid removing step, the washing drum 02 is rotated at a high speed to centrifuge the solvent. In the drying process, the air inside the cleaning device is circulated by a fan.
With 03, the water is passed through the water-cooled cooler 04 and the heater 05 and circulated into the washing drum 02.
即ち、ヒータ05で空気を昇温して、被洗物01に付着し
ている溶剤を蒸発させ、蒸発した溶剤ガスを水冷式クー
ラ04に導いて32〜35℃程度まで冷却する。そこで溶剤ガ
スは凝縮液化して回収されるが、空気に含まれる溶剤ガ
スは飽和濃度の関連で冷却温度が低いほどよく除去され
る。従って、例えば溶剤がパークロルエチレンの場合に
は冷却温度が35℃程度では空気に含まれる溶剤の濃度を
250g/m2以下とすることはできず、このままでは被洗物0
1に強い臭気が残る。そこで脱臭工程では、臭気を除去
し、また被洗物01を冷却するために、フレッシュエアダ
ンパ06を開いて外気を取り入れ、この外気を被洗物01と
接触させて溶剤ガス濃度を希釈させ、排気ダンパ07から
機外に排出させている。That is, the temperature of the air is raised by the heater 05 to evaporate the solvent adhering to the article 01 to be washed, and the evaporated solvent gas is guided to the water-cooled cooler 04 to be cooled to about 32 to 35 ° C. Thus, the solvent gas is condensed and liquefied and recovered. However, the solvent gas contained in the air is better removed as the cooling temperature is lower in relation to the saturation concentration. Therefore, for example, when the solvent is perchlorethylene, the concentration of the solvent contained in the air is reduced at a cooling temperature of about 35 ° C.
250 g / m 2 can not be less, Hiaraibutsu 0 in this state
Strong odor remains in 1. Therefore, in the deodorization step, in order to remove the odor and cool the object to be washed 01, the fresh air damper 06 is opened to take in the outside air, and the outside air is brought into contact with the object to be washed 01 to dilute the solvent gas concentration. The air is discharged outside from the exhaust damper 07.
この排気には希釈されたとはいえ、初期には数万ppm
に達する溶剤ガスの排出が行われ、大気汚染の問題が生
じるため、その対策及び溶剤回収による省資源を目的と
して、ダクト08を介して溶剤吸着槽09を設け、溶剤ガス
をこの槽09内に設けた活性炭槽010に吸着させてきれい
な空気のみを大気放出している。また前記溶剤吸着槽09
は、吸着した溶剤ガスで活性炭が飽和に達すると、活性
炭に蒸気配管011より水蒸気を吹き付けてこの溶剤を蒸
発させ、所謂脱着を行う。蒸発した溶剤ガスは水冷コン
デンサ012に導かれて凝縮液化し、水分離器013で回収溶
剤と水に分離されて回収される。また脱着工程に続いて
乾燥ファン014を作動させて活性炭層010を乾燥する乾燥
工程に入り、活性炭層010を再生して次の吸着工程に備
える。Although this exhaust gas was diluted, it was initially tens of thousands of ppm.
Solvent gas is discharged through the duct 08 through a duct 08 for the purpose of countermeasures and resource saving by solvent recovery. Activated carbon tank 010 provided adsorbs only clean air to the atmosphere. The solvent adsorption tank 09
When the activated carbon reaches saturation with the adsorbed solvent gas, the activated carbon is sprayed with steam from a steam pipe 011 to evaporate the solvent and perform so-called desorption. The evaporated solvent gas is guided to the water-cooled condenser 012 to be condensed and liquefied, and is separated and recovered by the water separator 013 into a recovered solvent and water. After the desorption step, the drying fan 014 is operated to start a drying step for drying the activated carbon layer 010, and the activated carbon layer 010 is regenerated to prepare for the next adsorption step.
（発明が解決しようとする課題） 前記第５図に示す従来の活性炭吸着の溶剤回収装置
は、溶剤脱着時及び乾燥して活性炭を再生させるため
に、独自の送風機、コンデンサ、水分離器を附属させて
いるため、コスト高となる問題があった。また脱臭工程
において、活性炭を通った後でも溶剤ガス濃度が零にな
らないまま機外に放出される問題もあり、更に活性炭に
吸収された溶剤を水蒸気を吹き込んで追い出したあと、
温風を吹き込んで活性炭の乾燥を行う。しかしこの時の
初期の排出空気（機外にそのまま放出される）に規制値
50PPM以上の濃度の溶剤ガスが排出されるが、排気口が
大気開放式ではこの高濃度ガスの排出は避けられなかっ
た。(Problem to be Solved by the Invention) The conventional activated carbon adsorption solvent recovery apparatus shown in FIG. 5 has an original blower, a condenser, and a water separator in order to regenerate activated carbon during solvent desorption and drying. Therefore, there was a problem that the cost was high. Also, in the deodorization process, even after passing through activated carbon, there is a problem that the solvent gas concentration is released to the outside without being reduced to zero, and after the solvent absorbed in the activated carbon is blown out by blowing steam,
The activated carbon is dried by blowing warm air. However, the regulated value for the initial exhaust air (discharged out of the machine as it is) at this time
Solvent gas with a concentration of 50 PPM or more is discharged, but if the exhaust port is open to the atmosphere, discharge of this high concentration gas is inevitable.
本発明は前記数来の課題を解決するために提案された
ものである。The present invention has been proposed to solve the above-mentioned problems.
（課題を解決するための手段） このため本発明は、蒸気配管を有する活性炭式溶剤吸
着器を備えると共に、処理槽に絞り弁を内蔵する吸出し
ダクトを介して主ダクトを連結し、同絞り弁に続いて同
主ダクト内にリントフィルタ、送風機、入口ダンパ、冷
却器、ヒータ、出口ダンパの順序で内蔵するドライクリ
ーニング装置において、前記吸着器の上部口とリントフ
ィルタの下流側を接続する第１配管と、同第１配管と前
記入口ダンパの下流側及び前記出口ダンパの下流側を夫
々接続する第２配管と第３配管、前記吸着器の下部口と
出口ダンパの上流側を接続する第４配管と、前記第１配
管と同第４配管とを接続する第５配管と、前記処理槽と
前記絞り弁を接続するバイパス管と、各配管を切換える
開閉弁とで閉回路を形成し、前記吸着器を介した衣料の
脱臭工程と活性炭の脱臭工程及び乾燥・再生工程で、ド
ライクリーニング装置の冷却器、ヒータ、送風機、水分
離器を共用できるものであり、また第２配管と第５配管
を削除して吸着器の下部口と入口ダンパの下流側を接続
する第６配管を設けてなるもので、これを課題解決のた
めの手段とするものである。(Means for Solving the Problems) Therefore, the present invention provides an activated carbon type solvent adsorber having a steam pipe, and connects a main duct to a treatment tank via a suction duct having a built-in throttle valve. Then, in a dry cleaning device built in the order of a lint filter, a blower, an inlet damper, a cooler, a heater, and an outlet damper in the same main duct, a first connecting the upper port of the adsorber and the downstream side of the lint filter. A pipe, a second pipe and a third pipe that respectively connect the first pipe and a downstream side of the inlet damper and a downstream side of the outlet damper, and a fourth pipe that connects a lower port of the adsorber and an upstream side of the outlet damper. Forming a closed circuit with a pipe, a fifth pipe connecting the first pipe and the fourth pipe, a bypass pipe connecting the processing tank and the throttle valve, and an on-off valve for switching each pipe; Via adsorber The cooler, heater, blower, and water separator of the dry cleaning device can be shared between the deodorizing process of the garment, the deodorizing process of the activated carbon, and the drying / regenerating process, and the second pipe and the fifth pipe are deleted. A sixth pipe connecting the lower port of the adsorber and the downstream side of the inlet damper is provided, and this is used as a means for solving the problem.
（作用） 活性炭よりの溶剤の回収（脱着工程）時に、水蒸気と
追い出された溶剤ガスをドライクリーナ本体の冷却装置
に導いてコンデンスさせ、凝縮により生じた液をドライ
クリーナ本体の水分離器に送る。また同様に活性炭の乾
燥工程において活性炭より出て来た湿った空気は、ドラ
イクリーナ本体に送られてドライクリーナの送風機、冷
却装置、水分離器、空気ヒータを経て乾燥され、この乾
いた温風が再び活性炭乾燥に使用される。更に脱臭工程
において、活性炭で溶剤ガスを除いた空気をそのままド
ライクリーナの処理槽へ送り、脱臭用として閉ループで
繰り返し使用することにより、活性炭で取りきれなかっ
た僅少の溶剤ガスでも機外に放出されることがなくな
る。また活性炭の乾燥工程においても、吸着器とドライ
クリーナを緊いだ閉ループで媒体空気を循環させるの
で、乾燥初期に生ずる濃い濃度の溶剤ガスが機外に排出
されるのを防止できる。(Action) During recovery (desorption step) of the solvent from the activated carbon, the vapor and the expelled solvent gas are led to the cooling device of the dry cleaner body to condense, and the liquid generated by the condensation is sent to the water separator of the dry cleaner body. . Similarly, the wet air coming out of the activated carbon in the activated carbon drying process is sent to the dry cleaner main body and dried through the dry cleaner's blower, cooling device, water separator, and air heater. Is again used for activated carbon drying. Furthermore, in the deodorization process, the air from which the solvent gas has been removed with activated carbon is directly sent to the treatment tank of the dry cleaner and used repeatedly in a closed loop for deodorization, so that even a small amount of solvent gas that could not be removed with activated carbon is released outside the machine. No more. Also, in the activated carbon drying step, the medium air is circulated in a closed loop in which the adsorber and the dry cleaner are tight, so that the solvent gas having a high concentration generated in the early stage of drying can be prevented from being discharged outside the apparatus.
（実施例） 以下本発明を図面の実施例について説明すると、第１
図〜第３図は本発明の第１実施例を示し、第４図は本発
明の第２実施例を示す。第１図において１はドライクリ
ーナの処理槽で、衣類の洗浄処理中は衣類を入れた処理
ドラムが中で回転するようになっている。また２は吸出
しダクトで、この中には絞り弁22が取付けられている。
３は溶剤道路で、ドライクリーナの洗浄、すすぎ工程に
おいては溶剤の溜り場所になっているが、脱臭、溶剤回
収工程においては、溶剤液は全部タンクに回収されて空
の状態である。(Embodiments) The present invention will be described below with reference to the embodiments in the drawings.
FIGS. 3 to 3 show a first embodiment of the present invention, and FIG. 4 shows a second embodiment of the present invention. In FIG. 1, reference numeral 1 denotes a processing tank of a dry cleaner, in which a processing drum containing clothes rotates inside during a washing process of the clothes. Reference numeral 2 denotes a suction duct, in which a throttle valve 22 is mounted.
Numeral 3 denotes a solvent road, which is a reservoir for the solvent in the washing and rinsing steps of the dry cleaner, but in the deodorizing and solvent collecting step, the solvent liquid is entirely collected in the tank and is empty.
本発明の要点とする脱臭、脱着、活性炭乾燥再生の工
程では、溶剤の逆流を防ぐためにストップ弁38は閉のま
まである。また４はバイパス管で、脱臭工程においては
ダクト２の中の絞り弁22が殆ど閉の位置にあり、溶剤ガ
スを含んだ空気は、大部分が通路３とこのバイパス管４
を流れて送風機６の入口に向かう。５はリントフィルタ
で、流れる空気中の糸屑を取除くものである。７は水冷
却器、８は冷媒冷却器で、凝縮液化効率を高める。９は
空気ヒータ、10はドライクリーナの主ダクト、11は水分
離器で、溶剤と水を比重差で分離する。12は水、溶剤用
配管、13は溶剤吸着器で、この中に活性炭14を内蔵す
る。15,16,17,18,19,20,21は空気配管、23,24はダクト1
0の出入口に取り付けられたダンパ、25,26,27,28,29,30
は空気配管15〜21の途中に置かれた空気用ストップ弁、
32は蒸気用ストップ弁、33は蒸気配管、34はベント配
管、35はベント配管34に取付けられたストップ弁（ドラ
イクリーナの内圧膨張時に活性炭経由で排出する為に使
用するが省略も可）、36は吸着器13から水分離器へ緊が
る排水管で、排水用ストップ弁37を取付けている。な
お、バイパス管４と絞り弁22は省略することもできる。In the deodorization, desorption, and activated carbon drying and regeneration steps, which are the main points of the present invention, the stop valve 38 is kept closed to prevent the backflow of the solvent. Reference numeral 4 denotes a bypass pipe, and in the deodorizing step, the throttle valve 22 in the duct 2 is almost at a closed position, and most of the air containing the solvent gas flows through the passage 3 and the bypass pipe 4.
To the inlet of the blower 6. A lint filter 5 removes lint from the flowing air. 7 is a water cooler, 8 is a refrigerant cooler, which increases the condensing and liquefaction efficiency. 9 is an air heater, 10 is a main duct of a dry cleaner, 11 is a water separator, which separates solvent and water with a specific gravity difference. 12 is a pipe for water and solvent, 13 is a solvent adsorber, in which activated carbon 14 is incorporated. 15, 16, 17, 18, 19, 20, 21 are air piping, 23, 24 are duct 1
Dampers mounted at doorway 0, 25, 26, 27, 28, 29, 30
Is a stop valve for air placed in the middle of the air piping 15-21,
32 is a stop valve for steam, 33 is a steam pipe, 34 is a vent pipe, 35 is a stop valve attached to the vent pipe 34 (used to discharge via activated carbon when the internal pressure of the dry cleaner expands, but can be omitted) Reference numeral 36 denotes a drain pipe which is tight from the adsorber 13 to the water separator, and has a drain stop valve 37 attached thereto. The bypass pipe 4 and the throttle valve 22 can be omitted.
ここで、空気配管16、19、20を第１配管、空気配管21
を第２配管、空気配管17を第３配管、空気配管15を第４
配管、空気配管18を第５配管と呼ぶことにする。Here, the air pipes 16, 19, and 20 are the first pipe and the air pipe 21
To the second pipe, the air pipe 17 to the third pipe, and the air pipe 15 to the fourth pipe.
The pipe and the air pipe 18 will be referred to as a fifth pipe.
次に作用を説明する。なお、ここでは先ず第１図で脱
臭工程における空気の流れと、その途中での処理につい
て説明する。さて処理槽１の中の回転するドラムの中の
衣類に付着していた溶剤ガスを奪った空気は、通路３、
バイパス管４、リントフィルタ５を通り、送風機６によ
り冷却器7,8に至り、若干の溶剤ガスがコンデンスする
（未だ溶剤ガスは空気中に残っている）。ダクト10の下
に溜まった溶剤の液は、水分離器11に流れ込む。また溶
剤ガスを含んだ空気は、熱くなっていないヒータ９を通
過し、空気配管15を通って吸着器13に至り、ここで溶剤
ガスの大部分が活性炭14に吸着される。そして無臭にま
できれいになった空気は、配管16,17を通って処理槽１
に入り、再度衣類から溶剤ガスを奪う。即ち、空気は閉
ループを循環するので、溶剤が大気中に放出されること
はない。この閉ループにおいて第１図の各ストップ弁の
動きは以下の通りである。即ち、空気用ストップ弁25,2
7、ダンパ23は開、ストップ弁26,28,29,30、ダンパ24は
閉、蒸気用ストップ弁32は閉。ベント用ストップ弁35は
開、排水用ストップ弁37は開、溶剤用ストップ弁38は閉
である。Next, the operation will be described. Here, first, the flow of air in the deodorization step and the processing in the middle thereof will be described with reference to FIG. By the way, the air which has removed the solvent gas attached to the clothes in the rotating drum in the processing tank 1 passes through the passage 3,
After passing through the bypass pipe 4 and the lint filter 5, the blower 6 reaches the coolers 7 and 8, and some solvent gas condenses (the solvent gas still remains in the air). The solvent liquid accumulated under the duct 10 flows into the water separator 11. The air containing the solvent gas passes through the heater 9 that is not heated, passes through the air pipe 15 and reaches the adsorber 13, where most of the solvent gas is adsorbed on the activated carbon 14. The air, which has been cleaned to an odorless level, passes through the pipes 16 and 17 and the treatment tank 1
Enter and take away solvent gas from clothing again. That is, since the air circulates through the closed loop, no solvent is released to the atmosphere. The operation of each stop valve in FIG. 1 in this closed loop is as follows. That is, the air stop valve 25, 2
7. Damper 23 is open, stop valves 26, 28, 29, 30 and damper 24 are closed, and steam stop valve 32 is closed. The vent stop valve 35 is open, the drain stop valve 37 is open, and the solvent stop valve 38 is closed.
次に第２図に脱着工程を説明する。第２図において蒸
気用ストップ弁32を開くと、配管33から100℃を超えた
蒸気が吸着器13に流れ込み、活性炭14に吸着した溶剤ガ
スを追い出し、配管15,18,19,21を通ってドライクリー
ナ本体のダクト10に流れ込む。ここで冷却器7,8によっ
て冷却されて凝縮し、ダクト10の下部から配管12を通っ
て水分離器11へ送られ溶剤は回収される。この工程にお
いては、送風機６と空気ヒータ９は使用しない。また各
ストップ弁の動きは以下の通りである。空気用ストップ
弁26,30は開、他は全て閉、ベント用ストップ弁35は
閉、排水用ストップ弁37、溶剤用ストップ弁38も閉であ
る。Next, the desorption process will be described with reference to FIG. In FIG. 2, when the stop valve 32 for steam is opened, the steam exceeding 100 ° C. flows from the pipe 33 into the adsorber 13 to drive out the solvent gas adsorbed on the activated carbon 14 and pass through the pipes 15, 18, 19, and 21. It flows into the duct 10 of the dry cleaner body. Here, it is cooled and condensed by the coolers 7 and 8, and is sent from the lower part of the duct 10 to the water separator 11 through the pipe 12 to recover the solvent. In this step, the blower 6 and the air heater 9 are not used. The movement of each stop valve is as follows. The air stop valves 26 and 30 are open, all others are closed, the vent stop valve 35 is closed, the drainage stop valve 37 and the solvent stop valve 38 are also closed.
次に第３図により活性炭乾燥再生工程につき説明す
る。第３図において送風機６により送られた空気は、冷
却器7,8により冷却され、水分は凝縮して乾いた空気が
エアーヒータ９により暖められ、この暖められた空気は
空気配管15を通って吸着器13に入り、脱着工程で蒸気に
より湿った活性炭14の水分を奪い、配管16,19,20を通っ
て送風機６の入口に達し、同送風機６よりダクト10に入
り、ここで空気中の水分と僅かに残っている溶剤ガスが
冷却器7,8により冷却され、凝縮して管路12により水分
離器11に送られて回収される。ここにおいても閉ループ
で活性炭の乾燥工程を、活性炭が完全に乾燥するまで続
ける。また各ストップ弁の動きは以下の通りである。即
ち、空気ストップ弁25,28,29、ダンパ23は開、ストップ
弁26,27,30、ダンパ24は閉、蒸気用ストップ弁32は閉、
ベント用ストップ弁35は開、排水用ストップ弁37は開、
溶剤用ストップ弁38は閉である。Next, the activated carbon drying and regeneration step will be described with reference to FIG. In FIG. 3, the air sent by the blower 6 is cooled by the coolers 7 and 8, the moisture is condensed and the dried air is heated by the air heater 9, and the warmed air passes through the air pipe 15. It enters the adsorber 13, deprives the activated carbon 14 moistened by steam in the desorption process, reaches the inlet of the blower 6 through the pipes 16, 19, 20 and enters the duct 10 from the blower 6, where it The water and a small amount of the solvent gas are cooled by the coolers 7 and 8, condensed, sent to the water separator 11 through the pipe 12, and collected. Here, the drying process of the activated carbon is continued in a closed loop until the activated carbon is completely dried. The movement of each stop valve is as follows. That is, the air stop valves 25, 28, 29, the damper 23 is open, the stop valves 26, 27, 30, the damper 24 is closed, the steam stop valve 32 is closed,
The vent stop valve 35 is open, the drain stop valve 37 is open,
The solvent stop valve 38 is closed.
次に第４図は第２実施例を示す。この実施例は第１実
施例における脱着時の蒸気の流れる配管、即ち吸着器13
からドライクリーナ本体まで専用の配管40を設けたもの
で、ストップ弁の数を減らすことができる。即ち、第１
図の配管18,20,21、空気用ストップ弁26,29,30を除き、
新たに第４図に示した如く配管40と、蒸気用ストップ弁
41を設けてなるものであるが、他の構成は第１実施例と
同じであり、作用効果においても差異はない。Next, FIG. 4 shows a second embodiment. This embodiment is different from the first embodiment in that the pipe through which steam flows during desorption, that is, the adsorber 13 is used.
A dedicated pipe 40 is provided from the to the dry cleaner main body, and the number of stop valves can be reduced. That is, the first
Except for piping 18, 20, 21 and air stop valves 26, 29, 30 in the figure,
A new pipe 40 and a steam stop valve as shown in FIG.
Although this embodiment is provided with 41, the other configuration is the same as that of the first embodiment, and there is no difference in the operation and effect.
（発明の効果） 以上詳細に説明した如く本発明は構成されているの
で、活性炭回収機に単独に回収機能、乾燥機能を持たせ
た場合と比べ、コンデンサ（冷却装置）、送風機、水分
離器のドライクリーナ本体の機能が共用できるので、コ
スト低減を図ることができる。また脱臭（吸着）工程に
おいて、溶剤ガスと空気の流れを閉ループにおいて処理
できるので、溶剤ガスが外気に出ない利点があり、更に
活性炭乾燥も閉ループで空気の処理ができるので、乾燥
の始めに起る高濃度ガスの初期破過による公害問題を防
ぐことができる。また従来の回収機で生じていた乾燥前
半の水蒸気の機外排出も無くなり、かつ水蒸気中に含ま
れた僅かな溶剤ガスも回収できる。更に閉ループで処理
するため、大口径の排気ダクトは不要となる。即ち、溶
剤回収に必要な機能がドライクリーナ本体の部品を共用
しているため、コストの低減を図ることができ、また脱
着後の乾燥を閉回路で行うため、乾燥初期の初期破過対
策ができ、脱臭工程も閉回路で実施するため、溶剤ガス
が外部に放出されることはない。(Effect of the Invention) As described in detail above, the present invention is configured, so that a condenser (cooling device), a blower, and a water separator are provided as compared with a case where the activated carbon recovering machine has a collecting function and a drying function independently. Since the function of the dry cleaner main body can be shared, the cost can be reduced. In the deodorization (adsorption) process, the flow of the solvent gas and the air can be processed in a closed loop, so that there is an advantage that the solvent gas does not come out to the outside air. Pollution problems caused by the initial breakthrough of high-concentration gas can be prevented. Further, the discharge of water vapor in the first half of drying, which has occurred in the conventional recovery machine, is eliminated, and a small amount of solvent gas contained in the water vapor can be recovered. Further, since the processing is performed in a closed loop, a large-diameter exhaust duct is not required. In other words, the functions required for solvent recovery share parts of the dry cleaner body, so that costs can be reduced, and drying after desorption is performed in a closed circuit. Since the deodorizing step is also performed in a closed circuit, the solvent gas is not released to the outside.
第１図，第２図及び第３図は夫々異なる工程の本発明の
実施例を示すドライクリーニング装置における溶剤回収
装置のシステム図、第４図は本発明の他の実施例を示す
溶剤回収装置のシステム図、第５図は従来の活性炭回収
装置付ドライクリーナのシステム図である。 図の主要部分の説明 １……処理槽 ６……送風機 ７……水冷却器 ８……冷媒冷却機 ９……空気ヒータ 11……水分離器 13……吸着器 14……活性炭 15,16,17,18,19,20,21……空気配管 23,24,25,26,27,28,29,30……空気用ストップ弁1, 2, and 3 are system diagrams of a solvent recovery apparatus in a dry cleaning apparatus showing an embodiment of the present invention in different steps, respectively, and FIG. 4 is a solvent recovery apparatus showing another embodiment of the present invention. FIG. 5 is a system diagram of a conventional dry cleaner with an activated carbon recovery device. Description of main parts in the figure 1 ... Treatment tank 6 ... Blower 7 ... Water cooler 8 ... Refrigerant cooler 9 ... Air heater 11 ... Water separator 13 ... Adsorber 14 ... Activated carbon 15,16 , 17,18,19,20,21 …… Air piping 23,24,25,26,27,28,29,30 …… Air stop valve
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6，ＤＢ名) D06F 43/08──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int.Cl. 6 , DB name) D06F 43/08
Claims (2)
えると共に、処理槽に絞り弁を内蔵する吸出しダクトを
介して主ダクトを連結し、同絞り弁に続いて同主ダクト
内にリントフィルタ、送風機、入口ダンパ、冷却器、ヒ
ータ、出口ダンパの順序で内蔵するドライクリーニング
装置において、前記吸着器の上部口とリントフィルタの
下流を接続する第１配管と、同第１配管と前記入口ダン
パの下流側及び前記出口ダンパの下流側を夫々接続する
第２配管と第３配管、前記吸着器の下部口と出口ダンパ
の上流側を接続する第４配管と、前記第１配管と同第４
配管とを接続する第５配管と、前記処理槽と前記絞り弁
を接続するバイパス管と、各配管を切換える開閉弁とで
閉回路を形成し、前記吸着器を介した衣料の脱臭工程と
活性炭の脱着工程及び乾燥・再生工程で、ドライクリー
ニング装置の冷却器、ヒータ、送風機、水分離器を共用
できることを特徴とするドライクリーニング装置の溶剤
回収装置。An activated carbon type solvent adsorber having a steam pipe, a main duct connected to a treatment tank via a suction duct having a built-in throttle valve, and a lint filter installed in the main duct following the throttle valve. A first pipe connecting an upper port of the adsorber and a downstream of a lint filter, a first pipe connecting the upper port of the adsorber and a downstream of a lint filter, and a blower, an inlet damper, a cooler, a heater, and an outlet damper. Second and third pipes respectively connecting the downstream side of the outlet and the downstream side of the outlet damper, a fourth pipe connecting the lower port of the adsorber and the upstream side of the outlet damper, and a fourth pipe connected to the first pipe.
A closed circuit is formed by a fifth pipe for connecting a pipe, a bypass pipe for connecting the processing tank and the throttle valve, and an on-off valve for switching each pipe, and a deodorizing step of the clothing through the adsorber and an activated carbon. A solvent recovery device for a dry cleaning device, wherein a cooler, a heater, a blower, and a water separator of the dry cleaning device can be shared in the desorption process and the drying / regeneration process.
の溶剤回収装置において、前記第２配管と第５配管を削
除して吸着器の下部口と入口ダンパの下流側を接続する
第６配管を設けたことを特徴とするドライクリーニング
装置の溶剤回収装置。2. A solvent recovery apparatus for a dry cleaning apparatus according to claim 1, wherein said second pipe and said fifth pipe are deleted and a sixth pipe connecting a lower port of said adsorber and a downstream side of said inlet damper is provided. A solvent recovery device for a dry cleaning device, which is provided.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2016074A JP2792705B2 (en) | 1990-01-29 | 1990-01-29 | Solvent recovery equipment for dry cleaning equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2016074A JP2792705B2 (en) | 1990-01-29 | 1990-01-29 | Solvent recovery equipment for dry cleaning equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03221099A JPH03221099A (en) | 1991-09-30 |
| JP2792705B2 true JP2792705B2 (en) | 1998-09-03 |
Family
ID=11906420
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2016074A Expired - Fee Related JP2792705B2 (en) | 1990-01-29 | 1990-01-29 | Solvent recovery equipment for dry cleaning equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2792705B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ITBO940260A1 (en) * | 1994-06-02 | 1995-12-02 | So Di Bo S P A | ACTIVATED CARBON SOLVENT PURIFIER FOR DRY CLEANING MACHINES WITH IMPROVED CONNECTION CIRCUIT TO THE MACHINE. |
| JP2007159691A (en) * | 2005-12-12 | 2007-06-28 | Tosen Machinery Corp | Method and apparatus for recovering solvent in washing machine |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62179497A (en) * | 1986-01-31 | 1987-08-06 | 富士車輌株式会社 | Solvent recovery method in dry cleaning |
| DE3609587C1 (en) * | 1986-03-21 | 1986-12-04 | BÖWE Reinigungstechnik GmbH, 8900 Augsburg | Device for the recovery of solvent gases |
-
1990
- 1990-01-29 JP JP2016074A patent/JP2792705B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03221099A (en) | 1991-09-30 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3883325A (en) | Method of and apparatus for the recovery of solvent gases from an air stream | |
| JPS63181795A (en) | Dry cleaning machiner for cloth | |
| JP2792705B2 (en) | Solvent recovery equipment for dry cleaning equipment | |
| JP3657425B2 (en) | Organic solvent recovery method and recovery device | |
| JPH0747109Y2 (en) | Solvent recovery device for dry cleaner | |
| JP2515329Y2 (en) | Solvent recovery device | |
| JP2617548B2 (en) | Dry cleaning method | |
| JP2552284Y2 (en) | Dry cleaner | |
| JPH0422811Y2 (en) | ||
| JPH0122633Y2 (en) | ||
| JPH0422810Y2 (en) | ||
| JP3021015B2 (en) | Dry cleaner | |
| JP2960989B2 (en) | Dry cleaning machine and method | |
| JP2749991B2 (en) | Dry cleaning method | |
| JP3082787B2 (en) | Dry cleaning machine | |
| JP2590729Y2 (en) | Activated carbon solvent recovery equipment with hot air desorption | |
| JP2971127B2 (en) | Dry cleaning method | |
| JP2744665B2 (en) | Solvent recovery equipment for dry cleaning equipment | |
| JP2813454B2 (en) | Dry cleaning method | |
| JP2948302B2 (en) | Dry cleaning machine | |
| JPH0639670Y2 (en) | Solvent recovery device | |
| JPH0425119Y2 (en) | ||
| JPS6142546Y2 (en) | ||
| JPS5818874Y2 (en) | dry cleaner | |
| JPH0141429Y2 (en) |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |