JPS62721Y2 - - Google Patents
Info
- Publication number
- JPS62721Y2 JPS62721Y2 JP1981065892U JP6589281U JPS62721Y2 JP S62721 Y2 JPS62721 Y2 JP S62721Y2 JP 1981065892 U JP1981065892 U JP 1981065892U JP 6589281 U JP6589281 U JP 6589281U JP S62721 Y2 JPS62721 Y2 JP S62721Y2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- solvent
- distiller
- valve
- temperature controller
- 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
Links
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Investigating Or Analyzing Materials Using Thermal Means (AREA)
Description
【考案の詳細な説明】
本考案はパークロルエチレン、1.1.1トリクロ
ルエタン、R113などの有機溶剤を使用するドラ
イクリーニング機械等の異常を検知する蒸留器に
関するものである。[Detailed description of the invention] The present invention relates to a distiller that detects abnormalities in dry cleaning machines and the like that use organic solvents such as perchlorethylene, 1.1.1 trichloroethane, and R113.
ここで第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。先ずドア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。 Here, a conventional dry cleaning process will be outlined using FIG. First, the clothing 2 is put in through the door 1, and the door 1 is closed to 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、バルブ7、フイルタ8、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,
Clothes 2 are washed by circulation through a circuit consisting of pump 6, valve 7, filter 8, or valve 9.
処理槽11、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 11, 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 the liquid is drained in the same way.
項、項の工程をくりかえす。 Repeat the steps in section and section.
処理槽11、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 11, 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.
次いで再び処理ドラム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。また衣料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。 Next, slowly rotate the processing drum 11 again,
Fan 16, air cooler 17, air heater 18
A recovery air duct 19 and a treatment tank 10 consisting of
Air is circulated between the two in the direction of the arrow 20 to dry the clothing 2. Further, the solvent gas evaporated from the clothing 2 is condensed in the air cooler 17 and collected in the recovery path 21.
It enters the water separator 22 through the solvent pipe 23 and enters the clean tank 24.
乾燥が終了すると、ダンパ25および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からはエアクーラ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 drying is completed, the dampers 25 and 26 open as shown by the broken lines, 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. .
項の工程で蒸留器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を通つてクリンタンク
24に入り、オーバフロー付仕切板28から溶
剤タンク3に戻る。なお、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。 The solvent 4 that entered the distiller 15 in the step of section 1.
It evaporates and is condensed and recovered in the condenser 27, enters the clean tank 24 through the water separator 22 and the solvent pipe 23, and returns to the solvent tank 3 through the overflow partition plate 28. Note that the water separated by the water separator 22 is discharged to the outside of the system through a water pipe 29.
次に本考案で対象とする従来の蒸留器について
第2図及び第3図で詳細に説明する。蒸留器の加
熱方式としては、電気ヒータで加熱した熱媒油方
式によるもの、および飽和蒸気によるものが従来
からよく知られているが、ここでは一般的な飽和
蒸気によるものを第2図に示す。 Next, a conventional distillation device to which the present invention is applied will be explained in detail with reference to FIGS. 2 and 3. The heating methods for distillers have long been well known, such as heating oil heated by an electric heater and using saturated steam. .
第2図において1サイクルのクリーニング工程
中に、汚染溶剤入口30より蒸留器15に流入し
た汚染溶剤を、蒸気弁31から加熱部32へ供給
する蒸気の熱量により加熱して蒸発させ、溶剤ガ
スをコンデンサ27に導き、冷却回収する方式を
取つている。そして汚染溶剤中に何らかの理由で
水分または界面活性剤が多量に混入すると、突沸
現象を起こし、瞬間的に多量の気泡が発生して第
3図に示す如く蒸留器15内に充満し、接続管3
3を通じコンデンサ27に汚染溶剤の気泡が到達
する。 In FIG. 2, during one cycle of cleaning process, the contaminated solvent flowing into the distiller 15 from the contaminated solvent inlet 30 is heated and evaporated by the heat of the steam supplied from the steam valve 31 to the heating section 32, and the solvent gas is released. A system is adopted in which it is guided to a condenser 27 and cooled and recovered. If a large amount of water or surfactant gets mixed into the contaminated solvent for some reason, a bumping phenomenon occurs, and a large amount of bubbles are instantaneously generated, filling the distiller 15 as shown in Figure 3, and connecting pipes. 3
Contaminant solvent bubbles reach the condenser 27 through 3.
さらに放置すれば、水分離器を通り、溶剤タン
ク内をも汚染する事態となり、各部機能をまひさ
せて復帰に多大の時間を要するトラブルとなる。
従つて気泡が発生した場合には、作業者が直ちに
蒸気弁31を止めてトラブルの拡大を防止してい
るが、異常現象は突発的に発生するものであり、
作業者が異常発生に気付くのがおくれ、しばしば
溶剤タンク内の溶剤まで汚染する不具合が発生し
ているのが実状である。 If left unattended further, the solvent will pass through the water separator and contaminate the inside of the solvent tank, resulting in trouble that paralyzes the functions of various parts and requires a great deal of time to recover.
Therefore, when bubbles occur, the operator immediately stops the steam valve 31 to prevent the problem from spreading; however, abnormal phenomena occur suddenly.
The reality is that workers are slow to notice the occurrence of an abnormality, often resulting in problems that even the solvent in the solvent tank becomes contaminated.
なお、第2図及び第3図で冷却管34、冷却水
入口35、同出口36によつて冷却され、凝縮回
収された溶剤は、溶剤回収管37を通り、水分離
器22を経て溶剤タンク3に回収される。なお4
7は蒸気ドレーン排出管、39は蒸留中の汚染溶
剤38の突沸現象によつて発生した汚染溶剤の泡
である。 In addition, in FIGS. 2 and 3, the solvent cooled by the cooling pipe 34, the cooling water inlet 35, and the cooling water outlet 36 and condensed and recovered passes through the solvent recovery pipe 37, passes through the water separator 22, and is transferred to the solvent tank. It will be collected on 3rd. Note 4
7 is a steam drain discharge pipe, and 39 is a bubble of contaminated solvent generated by the bumping phenomenon of contaminated solvent 38 during distillation.
本考案は前記従来の欠点を解消するために提案
されたもので、ドライクリーニング装置の溶剤回
収を行なうための蒸留器において、蒸留室内に臨
んで設けられた所定温度の雰囲気を保つシーズヒ
ータと熱電対等の温度検出端、及び温度調節計よ
りなる泡検知装置を備え、前記温度検出端は溶剤
蒸発温度より高い温度に保持されており、発泡し
た泡が触れてこの温度が急低下した場合、この温
度の急低下を前記温度調節計で検知することによ
り、発泡状態を検知するようにしたものであり、
異常発泡(ボイルオーバと云う)によるトラブル
を防止することができる蒸留器を提供せんとする
ものである。 The present invention was proposed in order to eliminate the above-mentioned drawbacks of the conventional methods.In a distiller for recovering solvents in dry cleaning equipment, a sheathed heater and a thermoelectric generator are installed facing into the distillation chamber to maintain an atmosphere at a predetermined temperature. A bubble detection device consisting of an equal temperature detection end and a temperature controller is provided. The bubbling state is detected by detecting a sudden drop in temperature with the temperature controller,
It is an object of the present invention to provide a distiller that can prevent troubles caused by abnormal foaming (referred to as boilover).
以下図面の実施例について本考案を説明する
と、本考案の実施例を示す蒸留器を第4図に示
す。第4図の装置は蒸留器15の上部空間に設置
された発泡検知センサ40、同センサの温度を設
定値に調節する温度調節計44、同温度調節計の
急激な温度変化信号を受けて蒸気弁31を閉じる
指示計45から構成されている。 The present invention will be described below with reference to the embodiments shown in the drawings. FIG. 4 shows a distiller showing an embodiment of the present invention. The device shown in FIG. 4 includes a foaming detection sensor 40 installed in the upper space of the distiller 15, a temperature controller 44 that adjusts the temperature of the sensor to a set value, and a temperature controller 44 that controls the temperature of the distiller 15. It consists of an indicator 45 that closes the valve 31.
発泡検知センサ40の1例を第5図に示すと、
耐腐蝕性に優れた材料(例えばステンレス鋼)で
製作された外筒46内に、シーズヒータ41、熱
電対等の温度検出端42が熱伝導度のよい粉体4
3(例えば金属粉)で保持されている。なお、第
4図において27はコンデンサ、30は汚染溶剤
投入口、32は加熱部、33は接続管、38は蒸
留中の汚染溶剤である。 An example of the foam detection sensor 40 is shown in FIG.
A sheathed heater 41 and a temperature detection end 42 such as a thermocouple are placed in a powder 4 with good thermal conductivity in an outer cylinder 46 made of a material with excellent corrosion resistance (for example, stainless steel).
3 (for example, metal powder). In FIG. 4, 27 is a condenser, 30 is a contaminated solvent inlet, 32 is a heating section, 33 is a connecting pipe, and 38 is a contaminated solvent during distillation.
次に作用を説明すると、洗浄工程で汚染された
汚染溶剤は、汚染溶剤投入口30より蒸留器15
に投入され、蒸気弁31から加熱部32へ供給す
る蒸気の大きな熱量により蒸発し、接続管33を
通じてコンデンサ27で凝縮回収される。蒸留器
内溶剤および溶剤ガス温度は大気圧下でその溶剤
の沸点温度、例えば溶剤にパークロルエチレンを
使用した場合は、121℃となる。 Next, to explain the operation, the contaminated solvent contaminated in the cleaning process is transferred to the distiller 15 from the contaminated solvent inlet 30.
It is evaporated by the large amount of heat of the steam supplied from the steam valve 31 to the heating section 32, and is condensed and recovered by the condenser 27 through the connecting pipe 33. The temperature of the solvent and solvent gas in the distiller is the boiling point temperature of the solvent under atmospheric pressure, for example, 121° C. when perchlorethylene is used as the solvent.
一方発泡検知センサ40は、シーズヒータ4
1、温度検出端42、温度調節計44により、溶
剤温度より約20℃高い温度、溶剤にパークロルエ
チレンを使用の場合は140℃に保持されている。 On the other hand, the foaming detection sensor 40 is connected to the sheathed heater 4
1. The temperature detection end 42 and temperature controller 44 maintain the temperature at about 20°C higher than the solvent temperature, or 140°C when perchlorethylene is used as the solvent.
ここで何らかの理由で発泡現象が起きた場合、
泡が蒸留器15内を次第に上昇して発泡検知セン
サ40に接触するまで上昇すると、発泡検知セン
サ40は泡の温度、パークロルエチレンの場合は
121℃まで温度調節計44の調節能力に抗して急
速に冷却される。この発泡検知センサ40の温度
の急低下を、温度調節計44で検知して指示計4
5を作動させ、蒸気弁31を閉じて蒸気の供給を
断つ。なお、蒸気弁31の閉にかえ、溶剤投入口
30を短時間開にして、冷い溶剤を蒸留器15内
に導入するようにしてもよい。また要すれば両者
の併用でもよく、発泡現象をブザー等で作業者に
知らせてもよい。 If bubbling occurs for some reason,
When the bubbles gradually rise in the distiller 15 until they come into contact with the bubble detection sensor 40, the bubble detection sensor 40 detects the temperature of the bubbles, and in the case of perchlorethylene.
It is rapidly cooled down to 121° C. against the control ability of the temperature controller 44. This sudden drop in temperature of the foaming detection sensor 40 is detected by the temperature controller 44 and the indicator 4
5 and closes the steam valve 31 to cut off the steam supply. Note that instead of closing the steam valve 31, the solvent inlet 30 may be opened for a short time to introduce cold solvent into the distiller 15. Moreover, if necessary, both may be used in combination, and the foaming phenomenon may be notified to the operator by a buzzer or the like.
以上詳細に説明した如く本考案は構成されてお
り、蒸留器内で発泡現象を検知して蒸気供給を断
つため、加熱源を失つてそれ以上の発泡は起ら
ず、泡は蒸留器内にとどまつて次第に沈静化し、
接続管以降のコンデンサなどを汚染する虞れは全
くなくなる。 As explained in detail above, the present invention is structured so that the foaming phenomenon is detected in the distiller and the steam supply is cut off, so the heating source is lost and no further foaming occurs, and the bubbles are kept inside the distiller. It stayed and gradually subsided,
There is no possibility of contaminating the condenser etc. after the connecting pipe.
また泡が沈静化し、発泡検知センサが温度調節
計の作用により設定値に復帰すれば、指示計の指
示により蒸気弁を再び開にして蒸留を再開する。
従つて作業者による蒸留器の監視は全く不要にな
るばかりでなく、コンデンサ、水分離器、溶剤タ
ンク等を汚染して、回復に多くの人手と時間を要
する現象、即ちボイルオーバ等のトラブルがなく
なり、機械の稼動率が向上する。また供給蒸気停
止の他、冷い溶剤を投入しても泡が急速に冷却さ
れ、沈静化して同様の効果が得られる。 Further, when the foam subsides and the foam detection sensor returns to the set value due to the action of the temperature controller, the steam valve is opened again according to the instruction from the indicator to restart distillation.
Therefore, not only does it become unnecessary for operators to monitor the distiller, but it also eliminates troubles such as boilover, which contaminates condensers, water separators, solvent tanks, etc. and requires a lot of manpower and time to recover. , machine operation rate is improved. In addition to stopping the steam supply, even if a cold solvent is introduced, the bubbles are rapidly cooled down and subsided, producing the same effect.
第1図は従来のドライクリーニング機の1例を
示す側断面図、第2図及び第3図は従来の蒸留器
の作用状態を説明する側断面図、第4図は本考案
の実施例を示す蒸留器の側断面図、第5図は第4
図における発泡検知センサの詳細断面図である。
図の主要部分の説明、15……蒸留器、40…
…発泡検知センサ、41……シーズヒータ、42
……温度検出端、44……温度調節計、45……
指示計、46……外筒。
Fig. 1 is a side sectional view showing an example of a conventional dry cleaning machine, Figs. 2 and 3 are side sectional views explaining the operating state of a conventional distiller, and Fig. 4 is a side sectional view showing an example of a conventional dry cleaning machine. A side sectional view of the distiller shown in FIG.
It is a detailed sectional view of the foaming detection sensor in the figure. Explanation of the main parts of the diagram, 15... distiller, 40...
... Foaming detection sensor, 41 ... Sheathed heater, 42
...Temperature detection end, 44...Temperature controller, 45...
Indicator, 46...outer cylinder.
Claims (1)
めの蒸留器において、蒸留室内に臨んで設けられ
た所定温度の雰囲気を保つシーズヒータと熱電対
等の温度検出端、及び温度調節計よりなる泡検知
装置を備え、前記温度検出端は溶剤蒸発温度より
高い温度に保持されており、発泡した泡が触れて
この温度が急低下した場合、この温度の急低下を
前記温度調節計で検知することにより、発泡状態
を検知することを特徴とする蒸留器。 A distiller for recovering solvents in dry cleaning equipment is equipped with a bubble detection device consisting of a sheathed heater facing into the distillation chamber to maintain an atmosphere at a predetermined temperature, a temperature detection end such as a thermocouple, and a temperature controller, The temperature detection end is maintained at a temperature higher than the solvent evaporation temperature, and if the temperature suddenly drops when it comes into contact with foamed foam, the foaming state can be detected by detecting this sudden drop in temperature with the temperature controller. A distiller characterized by detecting.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1981065892U JPS62721Y2 (en) | 1981-05-07 | 1981-05-07 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1981065892U JPS62721Y2 (en) | 1981-05-07 | 1981-05-07 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57177502U JPS57177502U (en) | 1982-11-10 |
| JPS62721Y2 true JPS62721Y2 (en) | 1987-01-09 |
Family
ID=29861919
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1981065892U Expired JPS62721Y2 (en) | 1981-05-07 | 1981-05-07 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62721Y2 (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS49104972U (en) * | 1972-12-20 | 1974-09-09 | ||
| JPS53117550U (en) * | 1977-02-25 | 1978-09-19 |
-
1981
- 1981-05-07 JP JP1981065892U patent/JPS62721Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57177502U (en) | 1982-11-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP4121822B2 (en) | Dry cleaning device | |
| US6609310B2 (en) | Method and apparatus for safety control of the drying cycle in hydrocarbon-solvent dry-cleaning machines | |
| JP2895285B2 (en) | How to monitor a dry cleaner still | |
| US3595037A (en) | Closed cleansing system | |
| EP0340482B1 (en) | Apparatus for extracting solvent from mixtures with oils, greases and impurities for dry-cleaning machines | |
| JPH0422811Y2 (en) | ||
| JPH0722225Y2 (en) | Dry cleaner | |
| JPS6216676B2 (en) | ||
| JPH0422810Y2 (en) | ||
| JPH0919596A (en) | Method and apparatus for combustible solvent dry cleaning | |
| JP2911303B2 (en) | Dryer | |
| JPS6321289Y2 (en) | ||
| JPH0246871Y2 (en) | ||
| JP3021022B2 (en) | Dry cleaning method | |
| JPS629921Y2 (en) | ||
| EP0490501A2 (en) | Cleaning of articles | |
| JP2960989B2 (en) | Dry cleaning machine and method | |
| JP2798849B2 (en) | Dryer | |
| JPH02149297A (en) | Dry-cleaning method | |
| JP2813454B2 (en) | Dry cleaning method | |
| JPH0133027Y2 (en) | ||
| JPH0453594A (en) | Distillation temperature control method in dry cleaning | |
| JPH0647039B2 (en) | Dry cleaner | |
| JP3254025B2 (en) | Empty-fire prevention still | |
| JPH08318093A (en) | Dry cleaning machine |