JPH0222680B2 - - Google Patents
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- Publication number
- JPH0222680B2 JPH0222680B2 JP57133247A JP13324782A JPH0222680B2 JP H0222680 B2 JPH0222680 B2 JP H0222680B2 JP 57133247 A JP57133247 A JP 57133247A JP 13324782 A JP13324782 A JP 13324782A JP H0222680 B2 JPH0222680 B2 JP H0222680B2
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- Prior art keywords
- control valve
- pipe
- water
- valve
- air
- Prior art date
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Description
【発明の詳細な説明】
本発明はパークロルエチレン、1,1,1―ト
リクロルエタン、1,1,2―トリクロロ―1,
2,2―トリフルオロエタンR113、トリクロロ
モノフルオロメタンR11などの有機溶剤を使用す
るドライクリーニング装置に関し、特に溶剤温度
上昇の防止を図つたドライクリーニング装置にお
ける溶剤温度上昇防止方法及び装置に関するもの
である。Detailed Description of the Invention The present invention relates to perchlorethylene, 1,1,1-trichloroethane, 1,1,2-trichloro-1,
This invention relates to dry cleaning equipment that uses organic solvents such as 2,2-trifluoroethane R113 and trichloromonofluoromethane R11, and in particular to a method and device for preventing a rise in solvent temperature in a dry cleaning equipment that aims to prevent a rise in solvent temperature. .
従来のドライクリーニング装置の概略を第1図
に示すが、この第1図を用いて従来のドライクリ
ーニング工程を概説する(以下、パークロルエチ
レンを例にして説明する)。まずドア1から衣料
2を投入し、ドア1を閉じて運転を開始すると、
一般には次の順序で工程が進行する。 A conventional dry cleaning apparatus is schematically shown in FIG. 1, and the conventional dry cleaning process will be explained using FIG. 1 (hereinafter, perchlorethylene will be explained as an example). First, put clothing 2 into door 1, close door 1, and start operation.
Generally, the steps proceed in the following order.
溶剤タンク3から溶剤4をバルブ5を介して
ポンプ6で汲み揚げ、バルブ7、フイルタ8か
ら成る経路、またはバルブ9から成る経路によ
つて処理槽10に溶剤4を必要量送り込む。 The solvent 4 is pumped up from the solvent tank 3 through the valve 5 by the pump 6, and the required amount of the solvent 4 is sent into the processing tank 10 through the path consisting of the valve 7 and the filter 8 or the path consisting of the valve 9.
処理ドラム11をゆつくり回し、溶剤4を処
理槽10、ボタントラツプ12、バルブ13、
ポンプ6を経て、バルブ7、フイルタ8からな
る回路、またはバルブ9から成る回路で循環し
て衣料2を洗浄する。 Gently rotate the processing drum 11 and pour the solvent 4 into the processing tank 10, button trap 12, valve 13,
The clothes 2 are washed by circulating through a pump 6 and a circuit consisting of a valve 7 and a filter 8 or a circuit consisting of a valve 9.
処理槽10、ボタントラツプ12、バルブ1
3、ポンプ6、バルブ14、蒸留器15の経路
で排液し、つづいて処理ドラム11が高速回転
して、衣料2中の溶剤4を遠心分離し同様に排
液する。 Processing tank 10, button trap 12, valve 1
3, the liquid is drained through the path of the pump 6, the valve 14, and the distiller 15, and then the processing drum 11 rotates at high speed to centrifugally separate the solvent 4 in the clothing 2 and drain it in the same way.
前記,の工程を繰り返えす。 Repeat the steps above.
処理槽10、ボタントラツプ12、バルブ1
3、バルブ5の経路で溶剤タンク3に排液し、
つづいて処理ドラム11が高速回転して衣料2
中の溶剤4を遠心分離し排液する。 Processing tank 10, button trap 12, valve 1
3. Drain the liquid into the solvent tank 3 through the route of the valve 5,
Subsequently, the processing drum 11 rotates at high speed to remove the clothing 2.
The solvent 4 inside is centrifuged and drained.
再び処理ドラム11をゆつくり回し、フアン
16、エアクーラ17、エアヒータ18から成
るリカバリエアダクト19と処理槽10の間を
矢印20の向きでエアを循環し、衣料2を乾燥
する。衣料2から蒸発した溶剤ガスは、エアク
ーラ17で凝縮し、回収経路21を経て水分離
器22に入り、溶剤配管23を通つてクリンタ
ンク24に入る。 The processing drum 11 is slowly rotated again, air is circulated in the direction of the arrow 20 between the recovery air duct 19 consisting of the fan 16, the air cooler 17, and the air heater 18 and the processing tank 10, and the clothes 2 are dried. The solvent gas evaporated from the clothing 2 is condensed in the air cooler 17, enters the water separator 22 through the recovery path 21, and enters the clean tank 24 through the solvent pipe 23.
乾燥が終了すると、ダンパ25,26が破線
の如く開き、ダンパ25から新鮮な空気をとり
入れ、ダンパ26からエアクーラ17では回収
できない未凝縮溶剤ガスを排気し、衣料2中の
溶剤臭を脱臭する。 When the drying is completed, the dampers 25 and 26 open as shown by the broken line, fresh air is taken in from the damper 25, and uncondensed solvent gas that cannot be recovered by the air cooler 17 is exhausted from the damper 26, thereby deodorizing the solvent odor in the clothing 2.
以上の〜の1サイクルは第2図の如く区分
される。 One cycle of the above steps is divided as shown in FIG.
なお、第1図中30はエアヒータ18に接続し
てエアクーラ17を通過したエアを加熱する水蒸
気配管、31は蒸留器15で蒸発した溶剤ガスを
凝縮液化する冷却水配管、32は蒸留器15に排
液された溶剤を加熱して蒸留する蒸気配管、33
は冷却水配管、34は乾燥工程に冷却水出口温度
を検知して必要な冷却水を供給している制水弁、
35は蒸気弁を示す。 In FIG. 1, 30 is a steam pipe connected to the air heater 18 to heat the air that has passed through the air cooler 17, 31 is a cooling water pipe that condenses and liquefies the solvent gas evaporated in the distiller 15, and 32 is a water vapor pipe connected to the distiller 15. Steam piping for heating and distilling the drained solvent, 33
34 is a cooling water pipe, and 34 is a water control valve that detects the cooling water outlet temperature and supplies the necessary cooling water to the drying process.
35 indicates a steam valve.
さて前記の工程で蒸留器15に入つた溶剤4
は、蒸発してコンデンサ27で凝縮回収され、水
分離器22、溶剤配管23を通つてクリーンタン
ク24に入り、オーバーフロー付仕切板28から
溶剤タンク3に戻る。また水分離器22で分離し
た水は、水配管29によつて系外へ排出する。 Now, the solvent 4 that entered the distiller 15 in the above step
is evaporated, condensed and recovered in the condenser 27, enters the clean tank 24 through the water separator 22 and solvent piping 23, and returns to the solvent tank 3 through the overflow partition plate 28. Further, the water separated by the water separator 22 is discharged to the outside of the system through a water pipe 29.
しかしながら第1図の装置で第2図のサイクル
によりパークロルエチレンの液温が上昇すると、
衣料の縮み、色泣き等の衣料に対する悪影響が増
加する。なお、この場合の溶剤温度を上昇させる
要因としては、下記の3点が考えられる。 However, when the liquid temperature of perchlorethylene rises in the cycle shown in Fig. 2 in the apparatus shown in Fig. 1,
Negative effects on clothing, such as shrinkage and discoloration, increase. In addition, the following three points can be considered as factors for increasing the solvent temperature in this case.
(a) 蒸留回収液がコンデンサ27の能力、冷却水
不足等により溶剤の温度が上昇する。(a) The temperature of the solvent in the distilled recovered liquid increases due to the capacity of the condenser 27, lack of cooling water, etc.
(b) 乾燥工程に於ける乾燥温度(55℃〜60℃)
によつて、処理槽10及び処理ドラム11等が
昇温されるが、この装置顕熱が1サイクル中に
放熱できず、次のサイクルで洗浄液が処理槽1
0に流入すると、前記顕熱により洗浄液は昇温
される。これの繰り返しにより溶剤温度は順次
上昇して行くことになる。(b) Drying temperature in the drying process (55℃~60℃)
, the temperature of the processing tank 10, processing drum 11, etc. is raised, but the sensible heat of this device cannot be dissipated during one cycle, and the cleaning liquid is heated to the processing tank 1 in the next cycle.
0, the temperature of the cleaning liquid is raised by the sensible heat. By repeating this process, the solvent temperature will gradually rise.
(c) ポンプ6による液循環により溶剤の温度が上
昇する。(c) The temperature of the solvent increases due to liquid circulation by the pump 6.
さて前記(a)〜(c)の要因のうち、(a)は適正なコン
デンサの選択、冷却水量の増加で対処可能であ
り、(c)は上昇幅が僅かなので無視できるのに対
し、(b)は溶剤温度上昇の最大要因であるが、その
対策としての簡便な方法はなかつた。 Now, among the factors (a) to (c) above, (a) can be dealt with by selecting an appropriate capacitor and increasing the amount of cooling water, and (c) can be ignored because the increase is small, whereas ( b) is the biggest cause of the increase in solvent temperature, but there is no simple method to deal with it.
本発明は溶剤温度の上昇を防止して、前記従来
の衣料事故等の不具合を解消することを目的と
し、処理ドラムからフアン、エアクーラ及びエア
ヒータを経て同処理ドラムに帰還するループを有
するドライクリーニング装置において、乾燥工程
では前記エアクーラに冷却水を流す冷却配管上に
設けられた小流量制水弁を作動させて溶剤ガスを
凝縮回収した後、次の冷却工程ではエアヒータの
熱源を遮断し、冷却水配管における前記制水弁の
入口側から分岐し、同制水弁の出口側に合流する
バイパス配管上に設けられ、同制水弁より大口径
の大流量バイパス弁を作動させた状態で、空気流
を前記ループを循環させることにより溶剤温度の
上昇を防止するようにしたドライクリーニング装
置における溶剤温度の上昇防止方法を提供せんと
するものである。 The present invention aims to prevent the increase in solvent temperature and eliminate the above-mentioned conventional problems such as clothing accidents.The present invention is a dry cleaning device having a loop from the processing drum to the processing drum via a fan, an air cooler, and an air heater. In the drying process, a small flow control valve installed on the cooling pipe that flows cooling water to the air cooler is operated to condense and recover the solvent gas, and in the next cooling process, the heat source of the air heater is shut off and the cooling water is When a high-flow bypass valve with a larger diameter than the water control valve is operated, it is installed on a bypass pipe that branches from the inlet side of the water control valve and merges with the outlet side of the water control valve. It is an object of the present invention to provide a method for preventing an increase in solvent temperature in a dry cleaning apparatus, which prevents an increase in solvent temperature by circulating a flow through the loop.
また本発明はフアン、エアクーラ及びエアヒー
タからなるリカバリエアダクトと処理ドラムとの
間をエアを循環させるドライクリーニング装置に
おいて、前記エアクーラに冷却水を流す冷却水配
管上に乾燥工程用制水弁を設けると共に、同冷却
水配管における同制水弁の入口側から分岐し、同
制水弁の出口側に合流するバイパス配管を前記冷
却水配管と並列に設け、同バイパス配管上に前記
制水弁より大口径の冷却工程用バイパス弁を設け
たドライクリーニング装置における溶剤温度の上
昇防止装置を提供せんとするものである。 The present invention also provides a dry cleaning device that circulates air between a recovery air duct consisting of a fan, an air cooler, and an air heater, and a processing drum, in which a water control valve for the drying process is provided on a cooling water pipe that flows cooling water to the air cooler. , a bypass pipe is installed in parallel with the cooling water pipe that branches from the inlet side of the water control valve in the cooling water pipe and joins to the outlet side of the water control valve, and a bypass pipe larger than the water control valve is installed on the bypass pipe. It is an object of the present invention to provide a device for preventing a rise in solvent temperature in a dry cleaning apparatus equipped with a bypass valve for a cooling process.
以下本発明の実施例を図面について説明する
と、第4図は本発明装置の実施例を示し、第1図
における要部の改良構造を示す。ここで第4図に
おける第1図との相違点のみ説明すると、33は
エアクーラ17に冷却水を流す冷却水配管で、同
配管33上には乾燥工程用制水弁34を設けると
共に、同冷却水配管33における同制水弁34の
入口側から分岐し、同制水弁34の出口側に合流
するバイパス配管を前記冷却水配管33と並列に
設け、同バイパス配管上に前記制水弁34に比較
して大口径の冷却工程のみ開となる自動開閉弁
(バイパス弁)36を設けてなるものである。 Embodiments of the present invention will be described below with reference to the drawings. FIG. 4 shows an embodiment of the apparatus of the present invention, and shows an improved structure of the main parts in FIG. 1. To explain only the differences between FIG. 4 and FIG. 1, reference numeral 33 is a cooling water pipe that flows cooling water to the air cooler 17. A water control valve 34 for the drying process is provided on the pipe 33, and a water control valve 34 for the drying process is provided on the pipe 33. A bypass pipe that branches from the inlet side of the water control valve 34 in the water pipe 33 and merges with the outlet side of the water control valve 34 is provided in parallel with the cooling water pipe 33, and the water control valve 34 is installed on the bypass pipe. An automatic opening/closing valve (bypass valve) 36 is provided which is opened only during the cooling process with a large diameter compared to the above.
次に本発明方法と従来方法との相違点について
説明すると、予洗工程から乾燥工程までは同
様であるので、ここではそれらの説明は省略し、
本発明の実施例を示す第3図の,工程のみ説
明する。 Next, to explain the differences between the method of the present invention and the conventional method, the steps from the pre-washing step to the drying step are the same, so their explanation will be omitted here.
Only the steps in FIG. 3 showing an embodiment of the present invention will be explained.
冷却工程
乾燥工程が終了すると、エアヒータ18の熱
源である水蒸気配管30の蒸気弁35を閉とし、
自動開閉弁36を開とすることにより、エアクー
ラ17に大流量の冷却水を通して、空気流をフア
ン16→エアクーラ17→エアヒータ18→処理
ドラム11(衣料2)→フアン16と循環させる
ことにより、処理槽10、処理ドラム11等の装
置顕熱を奪うとともに、衣料2も冷却する。Cooling process When the drying process is finished, the steam valve 35 of the steam pipe 30, which is the heat source of the air heater 18, is closed.
By opening the automatic opening/closing valve 36, a large flow of cooling water is passed through the air cooler 17, and the air flow is circulated from the fan 16 → air cooler 17 → air heater 18 → processing drum 11 (clothing 2) → fan 16. Sensible heat from devices such as the tank 10 and the processing drum 11 is removed, and the clothing 2 is also cooled.
脱臭工程
第2図の脱臭工程と同様であるが、冷却工程
で既に衣料2は冷却されているため、時間的に
は第2図の脱臭工程よりも短縮できる。以上詳
細に説明した如く本発明は構成されており、乾燥
工程と脱臭工程の間に冷却工程を設けるこ
とにより、装置顕熱を冷却水温(エアクーラの出
口水温は通常約30℃)のプラス5℃〜10℃程度ま
で低下することが可能となり、溶剤温度の上昇は
防止されて、衣料の縮み、色泣き等の衣料事故を
解消することができる。また衣料自身を充分に冷
却できるので、衣料の皺の発生を減少させて仕上
を楽にすることができる。Deodorizing process This is the same as the deodorizing process shown in FIG. 2, but since the clothing 2 has already been cooled in the cooling process, the time can be shorter than that of the deodorizing process shown in FIG. The present invention is constructed as described in detail above, and by providing a cooling process between the drying process and the deodorizing process, the sensible heat of the device is reduced by 5 degrees Celsius above the cooling water temperature (the air cooler outlet water temperature is usually about 30 degrees Celsius). It is possible to lower the temperature to about 10°C, preventing the solvent temperature from rising and eliminating clothing accidents such as shrinkage and discoloration of clothing. In addition, since the clothing itself can be sufficiently cooled, the occurrence of wrinkles in the clothing can be reduced and the finishing process can be made easier.
また本発明は、エアクーラの冷却水配管と並設
してバイパス配管を設け、同冷却水配管上には乾
燥工程用制水弁を、バイパス配管上には同制水弁
より大口径の冷却工程用バイパス弁を設けたの
で、冷却工程では装置顕熱を要望の温度まで十分
に低下させることが可能である。しかも本発明
は、従来装置に単にバイパス弁を有するバイパス
配管を並設しただけの極めて簡単な構造であるた
め、装置のコストを余り上げることなく目的を達
成することができる等の効果を奏するものであ
る。 In addition, the present invention provides a bypass pipe in parallel with the cooling water pipe of the air cooler, a water control valve for the drying process on the cooling water pipe, and a water control valve for the cooling process with a larger diameter than the water control valve on the bypass pipe. Since the bypass valve is provided, it is possible to sufficiently reduce the sensible heat of the device to the desired temperature in the cooling process. Moreover, since the present invention has an extremely simple structure in which bypass piping having a bypass valve is simply installed in parallel to the conventional device, it is possible to achieve the objective without significantly increasing the cost of the device. It is.
第1図は従来の一般的なドライクリーニング装
置の正面断面図、第2図は従来のドライクリーニ
ング工程を示す説明図、第3図は本発明の実施例
を示すドライクリーニング工程の説明図、第4図
は本発明装置の実施例を示し、第1図の要部の改
良構造を示す正面断面図である。
図の主要部分の説明、2……衣料、11……処
理ドラム、16……フアン、17……エアクー
ラ、18……エアヒータ、33……冷却水配管、
34……制水弁、36……自動開閉弁(バイパス
弁)。
FIG. 1 is a front sectional view of a conventional general dry cleaning apparatus, FIG. 2 is an explanatory diagram showing a conventional dry cleaning process, and FIG. 3 is an explanatory diagram of a dry cleaning process showing an embodiment of the present invention. FIG. 4 shows an embodiment of the device of the present invention, and is a front sectional view showing an improved structure of the main part of FIG. 1. Explanation of the main parts of the diagram, 2...Clothing, 11...Processing drum, 16...Fan, 17...Air cooler, 18...Air heater, 33...Cooling water piping,
34... Water control valve, 36... Automatic opening/closing valve (bypass valve).
Claims (1)
ヒータを経て同処理ドラムに帰還するループを有
するドライクリーニング装置の溶剤温度上昇防止
方法において、乾燥工程では前記エアクーラに冷
却水を流す冷却配管上に設けられた小流量制水弁
を作動させて溶剤ガスを凝縮回収した後、次の冷
却工程ではエアヒータの熱源を遮断し、冷却水配
管における前記制水弁の入口側から分岐し、同制
水弁の出口側に合流するバイパス配管上に設けら
れ、同制水弁より大口径の大流量バイパス弁を作
動させた状態で空気流を前記ループを循環させる
ことにより、溶剤温度の上昇を防止することを特
徴とするドライクリーニング装置の溶剤温度上昇
防止方法。 2 フアン、エアクーラ及びエアヒータからなる
リカバリエアダクトと処理ドラムとの間をエアを
循環させるドライクリーニング装置において、前
記エアクーラに冷却水を流す冷却水配管上に乾燥
工程用制水弁を設けると共に、同冷却水配管にお
ける同制水弁の入口側から分岐し、同制水弁の出
口側に合流するバイパス配管を前記冷却水配管と
並列に設け、同バイパス配管上に前記制水弁より
大口径の冷却工程用バイパス弁を設けたことを特
徴とするドライクリーニング装置の溶剤温度上昇
防止装置。[Scope of Claims] 1. In a method for preventing a rise in solvent temperature in a dry cleaning apparatus having a loop returning from a processing drum to the processing drum via a fan, an air cooler, and an air heater, in the drying process, a method for preventing a rise in solvent temperature on a cooling pipe that flows cooling water to the air cooler is provided. After condensing and recovering the solvent gas by activating the small flow water control valve installed at A high-flow bypass valve with a larger diameter than the water control valve is installed on the bypass piping that joins the outlet side of the water valve, and the air flow is circulated through the loop to prevent a rise in solvent temperature. A method for preventing a rise in solvent temperature in dry cleaning equipment. 2. In a dry cleaning device that circulates air between a recovery air duct consisting of a fan, an air cooler, and an air heater, and a processing drum, a water control valve for the drying process is provided on the cooling water pipe that flows cooling water to the air cooler, and A bypass pipe that branches from the inlet side of the water control valve in the water pipe and merges with the outlet side of the water control valve is provided in parallel with the cooling water pipe, and a cooling pipe with a diameter larger than that of the water control valve is installed on the bypass pipe. A solvent temperature rise prevention device for dry cleaning equipment, characterized by being equipped with a process bypass valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13324782A JPS5922598A (en) | 1982-07-30 | 1982-07-30 | Method and apparatus for preventing rising in solvent temperature in dry cleaning apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13324782A JPS5922598A (en) | 1982-07-30 | 1982-07-30 | Method and apparatus for preventing rising in solvent temperature in dry cleaning apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5922598A JPS5922598A (en) | 1984-02-04 |
| JPH0222680B2 true JPH0222680B2 (en) | 1990-05-21 |
Family
ID=15100141
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13324782A Granted JPS5922598A (en) | 1982-07-30 | 1982-07-30 | Method and apparatus for preventing rising in solvent temperature in dry cleaning apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5922598A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2590729Y2 (en) * | 1993-03-12 | 1999-02-17 | 三菱重工業株式会社 | Activated carbon solvent recovery equipment with hot air desorption |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS55133989U (en) * | 1979-03-15 | 1980-09-22 |
-
1982
- 1982-07-30 JP JP13324782A patent/JPS5922598A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5922598A (en) | 1984-02-04 |
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