JPH0710716Y2 - Solvent recovery device for dry cleaning device - Google Patents
Solvent recovery device for dry cleaning deviceInfo
- Publication number
- JPH0710716Y2 JPH0710716Y2 JP1989046795U JP4679589U JPH0710716Y2 JP H0710716 Y2 JPH0710716 Y2 JP H0710716Y2 JP 1989046795 U JP1989046795 U JP 1989046795U JP 4679589 U JP4679589 U JP 4679589U JP H0710716 Y2 JPH0710716 Y2 JP H0710716Y2
- Authority
- JP
- Japan
- Prior art keywords
- solvent
- activated carbon
- air
- solvent gas
- tank
- 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
Links
Description
【考案の詳細な説明】 〔産業上の利用分野〕 本考案はパークロルエチレン、1,1,1−トリクロルエタ
ン、R11,R113等の有機溶剤を使用するドライクリーニン
グ装置の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 solvent recovery device for a dry cleaning device using an organic solvent such as perchlorethylene, 1,1,1-trichloroethane, and R11, R113.
従来、ドライクリーニング装置は、第2図に示すように
構成され、クリーニングの工程は洗浄工程、脱液工程、
乾燥工程、脱臭工程を順におこなつている。Conventionally, a dry cleaning device is configured as shown in FIG. 2, and the cleaning process includes a cleaning process, a liquid removing process,
The drying process and the deodorizing process are performed in sequence.
洗浄工程では、被洗物1をパークロルエチレン、1,1,1
−トリクロルエタン、R11,R113等の揮発性を高い溶剤に
浸漬して汚れを落とす。さらに脱液工程では洗濯ドラム
2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アン3によ
り、水冷式クーラ4及びヒータ5を通過させて洗濯ドラ
ム2内へと循環させる。In the washing process, the item to be washed 1 is perchlorethylene, 1,1,1
-Immerse in a highly volatile solvent such as trichloroethane, R11 and R113 to remove dirt. Further, in the liquid removing step, the washing drum 2 is rotated at high speed to centrifuge the solvent. In the drying process, the air in the cleaning device is circulated into the washing drum 2 by the circulation fan 3 through the water-cooling cooler 4 and the heater 5.
すなわちヒータ5で空気を昇温して被洗物1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
4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。That is, the temperature of the air is raised by the heater 5 to evaporate the solvent adhering to the object to be washed 1, and the evaporated solvent gas is guided to the water-cooled cooler 4 to be cooled to about 32 to 35 ° C. Then, the solvent gas is condensed and liquefied and recovered, but the solvent gas contained in the air is more removed as the cooling temperature is lower due to the saturation concentration.
したがつて例えば溶剤がバ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25
0g/m3以下とすることはできず、このままでは被洗物1
に強い臭気が残る。Therefore, for example, when the solvent is perchlorethylene, the concentration of the solvent contained in the air is 25 when the cooling temperature is about 35 ° C.
It cannot be less than 0g / m 3, and if it is left as it is 1
A strong odor remains.
従つて脱臭工程では、臭気を除去し、又被洗物1を冷却
するために、フレツシユエアダンバ6を開いて外気を取
り入れ、これを被洗物1と接触させ、溶剤ガス濃度を希
釈させ、排気ダンパ7から機外に排出させる。Therefore, in the deodorizing step, in order to remove the odor and cool the article to be washed 1, the fresh air air damper 6 is opened to take in outside air, and this is brought into contact with the article to be washed 1 to dilute the solvent gas concentration. , Is discharged from the exhaust damper 7 to the outside of the machine.
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おこなわれ、大気汚染の問題が生
じる。この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8を介して溶剤吸着槽9を設け、溶剤ガ
スをこの槽9内に設けた活性炭槽10に吸着させてきれい
な空気のみを排気ダンパ17より大気放出している。Although this exhaust gas is diluted, solvent gas of tens of thousands ppm is discharged in the initial stage, which causes a problem of air pollution. For this reason, a solvent adsorption tank 9 is provided through the duct 8 for the purpose of countermeasures and resource saving by solvent recovery, and the solvent gas is adsorbed by the activated carbon tank 10 provided in the tank 9 so that only clean air is discharged from the exhaust damper 17. It is released into the atmosphere.
この溶剤吸着槽9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11より水蒸気を吹き付けて
この溶剤を蒸発させ、いわゆる脱着をおこなう。蒸発し
た溶剤ガスは水冷コンデンサ12に導かれ凝縮液化し、水
分離器13で回収溶剤と水に分離されて回収される。In this solvent adsorption tank 9, when the activated carbon reaches saturation with the adsorbed solvent gas, steam is sprayed onto the activated carbon from the steam pipe 11 to evaporate the solvent and perform so-called desorption. The evaporated solvent gas is guided to the water-cooled condenser 12, condensed and liquefied, and separated by the water separator 13 into the recovered solvent and water and recovered.
脱着工程に続いて乾燥フアン14を作動させて活性炭層10
を乾燥する乾燥工程に入り、活性炭層10を再生して次の
吸着工程に備える。Following the desorption process, the dry fan 14 is activated to activate the activated carbon layer 10
Then, the activated carbon layer 10 is regenerated to prepare for the next adsorption step.
前記の吸着槽内の活性炭を蒸気にて脱着後、活性炭を乾
燥フアンにて乾燥させる際、活性炭層内のコンデンサ寄
りの空間には脱着により活性炭から蒸発した溶剤ガスで
充満しており、また活性炭は蒸気にて加熱されていて溶
剤ガスの吸着能力がないため、活性炭の乾燥初期に乾燥
フアンから供給された大気には溶剤ガスが放出するいわ
ゆる初期破過により高濃度の溶剤ガスが大気に放出され
るおそれがある。After desorbing the activated carbon in the adsorption tank with steam and then drying the activated carbon with a drying fan, the space near the condenser in the activated carbon layer is filled with the solvent gas evaporated from the desorption due to the desorption. Is heated by steam and does not have the ability to adsorb solvent gas, so the solvent gas is released into the atmosphere supplied from the drying fan at the initial stage of drying the activated carbon, so a high concentration of solvent gas is released into the atmosphere by so-called initial breakthrough. May be
本考案は上記技術水準に鑑み、乾燥用空気に伴なわれる
溶剤蒸気を大気に排出させるおそれがないドライクリー
ニング装置の溶剤回収装置を提供しようとするものであ
る。In view of the above-mentioned state of the art, the present invention is to provide a solvent recovery device for a dry cleaning device that does not have the risk of discharging solvent vapor accompanying drying air to the atmosphere.
本考案は、ドライクリーニング装置と連通し、溶剤ガス
を活性炭によつて回収する活性炭吸着槽、該活性炭吸着
槽で清浄化した空気を排出する排気ダンパ、該活性炭吸
着槽に脱着用蒸気を供給する蒸気配管、該活性炭吸着槽
から排出される溶剤ガス含有蒸気を冷却するコンデン
サ、該コンデンサと連通する溶剤と水を分離する水分離
器及び脱着済み活性炭吸着槽に乾燥用空気を供給する乾
燥フアンによつて構成される溶剤回収装置において、上
記コンデンサと連通して溶剤ガス含有空気を吸引する吸
引ファン、該吸引ファンと吸引配管を介して連通して溶
剤ガス含有空気を貯えるエアタンク及び該エアタンクを
前記乾燥フアンと連通する排出配管を追設してなること
を特徴とするドライクリーニング装置の溶剤回収装置で
ある。The present invention is to communicate with a dry cleaning device, an activated carbon adsorption tank for collecting solvent gas by activated carbon, an exhaust damper for discharging the air cleaned in the activated carbon adsorption tank, and a desorption steam for the activated carbon adsorption tank. A steam pipe, a condenser for cooling the solvent gas-containing steam discharged from the activated carbon adsorption tank, a water separator for separating the solvent and water in communication with the condenser, and a drying fan for supplying drying air to the desorbed activated carbon adsorption tank. In the solvent recovery apparatus configured as described above, a suction fan that communicates with the condenser to suck the solvent gas-containing air, an air tank that communicates with the suction fan through a suction pipe to store the solvent gas-containing air, and the air tank are provided. A solvent recovery device for a dry cleaning device, wherein a discharge pipe communicating with a drying fan is additionally provided.
本考案装置によれば、活性炭の脱着後、乾燥工程の初期
に活性炭槽内に充満した溶剤ガスはフアンにて吸引さ
れ、吸引された溶剤ガスはエアタンクに一旦貯蔵され
る。活性炭槽内の溶剤ガスがなくなつたら乾燥フアンに
より活性炭を乾燥させはじめ、同時にエアタンク内に貯
蔵した溶剤ガス含有空気を乾燥フアンにより吸着槽に送
り込み、溶剤ガスを活性炭に吸着させる。According to the device of the present invention, after desorption of the activated carbon, the solvent gas filled in the activated carbon tank at the beginning of the drying process is sucked by the fan, and the sucked solvent gas is temporarily stored in the air tank. When the solvent gas in the activated carbon tank is exhausted, the activated carbon is dried with a drying fan, and at the same time, the solvent gas-containing air stored in the air tank is fed into the adsorption tank with the drying fan to adsorb the solvent gas to the activated carbon.
公害防止条例等により大気汚染に対する指導があり、例
えば神奈川県ではパークロルエチレンの排気ガス濃度50
ppm以下とある。従来乾燥の初期に数万ppmの溶剤ガスが
大気に放出されていたが、本考案装置によればこれが防
止できる。Guidance on air pollution is given by the Pollution Control Ordinance. For example, in Kanagawa prefecture, exhaust gas concentration of perchlorethylene 50
It is below ppm. Conventionally, tens of thousands of ppm of solvent gas was released to the atmosphere at the beginning of drying, but the device of the present invention can prevent this.
以下、本考案の一実施例を第1図によつて説明する。 An embodiment of the present invention will be described below with reference to FIG.
第1図において、溶剤回収装置内のコンデンサ12に吸引
配管22を設け、溶剤吸着槽9よりコンデンサ12を経由し
て吸引フアン20によつて溶剤吸着槽9内を吸引できるよ
うにし、吸引フアン20の排気側を同配管22によりエアタ
ンク21に接続する。エアタンク21は伸縮性の材料で製作
し、吸引した溶剤ガスを貯蔵できるようにすることが好
ましい。In FIG. 1, a suction pipe 22 is provided in the condenser 12 in the solvent recovery device so that the solvent adsorption tank 9 can be suctioned through the condenser 12 by the suction fan 20. The exhaust side of is connected to the air tank 21 through the same pipe 22. The air tank 21 is preferably made of a stretchable material so that it can store the sucked solvent gas.
エアタンク21の排気側に排出配管23を設け、乾燥フアン
14を作動した際、外気と共にエアタンク21内の溶剤ガス
を吸引排出できるようにする。Provide a discharge pipe 23 on the exhaust side of the air tank 21 to
When the valve 14 is activated, the solvent gas in the air tank 21 can be sucked and discharged together with the outside air.
図示せぬドライクリーニング装置の脱臭工程時にドライ
クリーニング装置から高濃度の溶剤ガスが排気され、ダ
クト8より溶剤吸着槽9に導かれる。高濃度の溶剤ガス
は活性炭層10に吸着され、溶剤ガスを含まない空気が排
気ダンパ17より大気に放出される。During the deodorizing process of a dry cleaning device (not shown), a high-concentration solvent gas is exhausted from the dry cleaning device and guided to the solvent adsorption tank 9 through the duct 8. The high-concentration solvent gas is adsorbed on the activated carbon layer 10, and the air containing no solvent gas is released from the exhaust damper 17 to the atmosphere.
この溶剤吸着槽9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11より水蒸気を吹き付けて
この溶剤を蒸発させ、脱着をおこなう。蒸発した溶剤ガ
スは水冷コンデンサ12に導かれ凝縮液化し、水分離器13
で回収溶剤と水に分離されて回収される。脱着工程終了
時、溶剤吸着槽9内のコンデンサ12寄りの空間及び活性
炭層内には脱着用の蒸気と溶剤ガスが充満している。又
活性炭層10内の活性炭も脱着のため、蒸気で加熱され溶
剤ガスの吸着能力がない。In the solvent adsorption tank 9, when the activated carbon reaches saturation with the adsorbed solvent gas, water vapor is sprayed from the steam pipe 11 to the activated carbon to evaporate the solvent and perform desorption. The evaporated solvent gas is guided to a water-cooled condenser 12, condensed and liquefied, and a water separator 13
It is separated into a solvent and water for recovery. At the end of the desorption process, the space near the condenser 12 in the solvent adsorption tank 9 and the activated carbon layer are filled with desorption vapor and solvent gas. Further, since the activated carbon in the activated carbon layer 10 is also desorbed, it is heated by steam and has no ability to adsorb solvent gas.
脱着終了後、溶剤吸着槽9内に充満した溶剤ガスを大気
に放出しないために、吸引フアン20を作動させ、排気ダ
ンパ17を開けて外気を取り入れながら溶剤吸着槽9内の
溶剤ガスがなくなるまで、あるいは活性炭10上部が吸着
能力を回復するまでコンデンサ12を経由して吸引フアン
20で吸引する。吸引フアン20より排気される溶剤ガスは
コンデンサ12を経由しているため、低温で低濃度になつ
ている。この低温で低濃度の溶剤ガスは吸引配管22より
エアタンク21に移送しエアタンク21に貯蔵れる。次いで
吸引フアン20を停止するとともに、エアタンク21の入口
側に設けた自動弁(図示せず)を閉じて乾燥フアン14を
直ちに作動させて活性炭層10を乾燥する乾燥工程に入
り、活性炭層10を再生する。After desorption, in order not to release the solvent gas filled in the solvent adsorption tank 9 to the atmosphere, the suction fan 20 is operated, the exhaust damper 17 is opened, and the solvent gas in the solvent adsorption tank 9 is exhausted while taking in the outside air. , Or the suction fan via the condenser 12 until the upper part of the activated carbon recovers the adsorption capacity.
Aspirate at 20. Since the solvent gas exhausted from the suction fan 20 passes through the condenser 12, it has a low concentration at a low temperature. This low-temperature, low-concentration solvent gas is transferred to the air tank 21 through the suction pipe 22 and stored in the air tank 21. Next, the suction fan 20 is stopped, an automatic valve (not shown) provided on the inlet side of the air tank 21 is closed, and the drying fan 14 is immediately activated to enter the drying step of drying the activated carbon layer 10. Reproduce.
この乾燥工程の初期には溶剤吸着槽9内に溶剤ガスがな
いため、あるいは活性炭10上部が吸着能力を回復してい
るので排気ダンパ17より高濃度の溶剤ガスが排出される
ことはなく乾燥される。又エアタンク21の排気側より接
続された排出配管23が乾燥フアン14の吸引側に設けてあ
るので、乾燥工程中にエアタンク21内に貯蔵した溶剤ガ
スは吸引され、活性炭層10に吸着し、エアタンク21は収
縮し次の工程に備える。この乾燥工程終了後、活性炭層
10は再生され次の吸着工程に備える。Since there is no solvent gas in the solvent adsorption tank 9 at the beginning of this drying process, or because the upper part of the activated carbon 10 has recovered its adsorption capacity, the exhaust damper 17 does not discharge high-concentration solvent gas and it is dried. It Further, since the discharge pipe 23 connected from the exhaust side of the air tank 21 is provided on the suction side of the drying fan 14, the solvent gas stored in the air tank 21 during the drying process is sucked and adsorbed on the activated carbon layer 10, 21 shrinks and prepares for the next step. After this drying process, activated carbon layer
10 is regenerated to prepare for the next adsorption step.
なお前記配管23に自動弁(図示せず)を設けて乾燥工程
の末期のみ自動弁を開ければ、より効率良く溶剤ガスが
活性炭層10に吸着する事が出来る。またコンデンサ12と
吸引フアン20の間には脱着中に閉じる自動弁(図示せ
ず)を設けるのが実用的である。活性炭層10の乾燥は、
フアン14に設けた吸気ダンパ(図示せず)を開にしてフ
アン14を作動させ大気を取り入れることにより実施され
る。If an automatic valve (not shown) is provided in the pipe 23 and the automatic valve is opened only at the end of the drying process, the solvent gas can be more efficiently adsorbed to the activated carbon layer 10. Further, it is practical to provide an automatic valve (not shown) between the condenser 12 and the suction fan 20 which is closed during the attachment / detachment. Drying the activated carbon layer 10
This is performed by opening an intake damper (not shown) provided in the fan 14 and operating the fan 14 to take in the atmosphere.
活性炭の脱着後、溶剤吸着層内に充満した溶剤ガスと蒸
気をコンデンサ経由フアンにより吸引し、溶剤吸着層内
の溶剤ガスがなくなつたら乾燥工程に入るため、初期破
過による大気汚染がない。After desorption of the activated carbon, the solvent gas and vapor filled in the solvent adsorption layer are sucked by the fan through the condenser, and when the solvent gas in the solvent adsorption layer is exhausted, the drying process starts, so there is no air pollution due to initial breakthrough.
またフアンにより吸引した溶剤ガスは一旦エアタンクに
貯蔵し、貯蔵した溶剤ガスは乾燥工程中又は乾燥工程末
期に活性炭層に吸着され大気に溶剤ガスを放出すること
がない。Further, the solvent gas sucked by the fan is once stored in the air tank, and the stored solvent gas is not adsorbed to the activated carbon layer during the drying process or at the end of the drying process and is not released to the atmosphere.
第1図は、本考案の1実施例に係る溶剤回収装置の概略
図、第2図は従来の溶剤回収装置の一態様の概略図であ
る。 1……被洗物、2……洗濯ドラム、3……循環フアン、
4……水冷式クーラ、5……ヒータ、6……フレツシユ
エアダンパ、7……排気ダンパ、8……ダクト、9……
溶剤吸着槽、10……活性炭槽、11……蒸気配管、12……
水冷コンデンサ、13……水分離器、14……乾燥フアン、
17……排気ダンパ、20……フアン、21……エアタンク、
22……吸引配管、23……排出配管FIG. 1 is a schematic view of a solvent recovery apparatus according to an embodiment of the present invention, and FIG. 2 is a schematic view of one mode of a conventional solvent recovery apparatus. 1 ... Washed item, 2 ... Washing drum, 3 ... Circulating fan,
4 ... Water-cooled cooler, 5 ... Heater, 6 ... Fresh air damper, 7 ... Exhaust damper, 8 ... Duct, 9 ...
Solvent adsorption tank, 10 …… Activated carbon tank, 11 …… Steam piping, 12 ……
Water-cooled condenser, 13 ... water separator, 14 ... drying fan,
17 …… Exhaust damper, 20 …… Juan, 21 …… Air tank,
22 …… Suction piping, 23 …… Discharge piping
Claims (1)
スを活性炭によって回収する活性炭吸着槽、該活性炭吸
着槽で清浄化した空気を排出する排気ダンパ、該活性炭
吸着槽に脱着用蒸気を供給する蒸気配管、該活性炭吸着
槽から排出される溶剤ガス含有蒸気を冷却するコンデン
サ、該コンデンサと連通する溶剤と水を分離する水分離
器及び脱着済み活性炭吸着槽に乾燥用空気を供給する乾
燥ファンによって構成される溶剤回収装置において、上
記コンデンサと連通して溶剤ガス含有空気を吸引する吸
引ファン、該吸引ファンと吸引配管を介して連通して溶
剤ガス含有空気を貯えるエアタンク及び該エアタンクを
前記乾燥ファンと連通する排出配管を追設してなること
を特徴とするドライクリーニング装置の溶剤回収装置。1. An activated carbon adsorption tank which communicates with a dry cleaning device to collect solvent gas by activated carbon, an exhaust damper which discharges air cleaned in the activated carbon adsorption tank, and a steam which supplies desorption steam to the activated carbon adsorption tank. Consists of a pipe, a condenser for cooling the solvent gas-containing vapor discharged from the activated carbon adsorption tank, a water separator for separating the solvent and water communicating with the condenser, and a drying fan for supplying drying air to the desorbed activated carbon adsorption tank. In the solvent recovery apparatus described above, a suction fan that communicates with the condenser to suck the solvent gas-containing air, an air tank that communicates with the suction fan via a suction pipe to store the solvent gas-containing air, and the air tank with the drying fan. A solvent recovery device for a dry cleaning device, characterized in that a communicating discharge pipe is additionally provided.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1989046795U JPH0710716Y2 (en) | 1989-04-24 | 1989-04-24 | Solvent recovery device for dry cleaning device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1989046795U JPH0710716Y2 (en) | 1989-04-24 | 1989-04-24 | Solvent recovery device for dry cleaning device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02138696U JPH02138696U (en) | 1990-11-20 |
JPH0710716Y2 true JPH0710716Y2 (en) | 1995-03-15 |
Family
ID=31562179
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1989046795U Expired - Lifetime JPH0710716Y2 (en) | 1989-04-24 | 1989-04-24 | Solvent recovery device for dry cleaning device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0710716Y2 (en) |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5990790U (en) * | 1982-12-10 | 1984-06-20 | 三菱重工業株式会社 | Dry cleaner solvent recovery equipment |
-
1989
- 1989-04-24 JP JP1989046795U patent/JPH0710716Y2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH02138696U (en) | 1990-11-20 |
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