JPH0636838B2 - Distillation temperature control method in dry cleaning - Google Patents

Distillation temperature control method in dry cleaning

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Publication number
JPH0636838B2
JPH0636838B2 JP2161311A JP16131190A JPH0636838B2 JP H0636838 B2 JPH0636838 B2 JP H0636838B2 JP 2161311 A JP2161311 A JP 2161311A JP 16131190 A JP16131190 A JP 16131190A JP H0636838 B2 JPH0636838 B2 JP H0636838B2
Authority
JP
Japan
Prior art keywords
cleaning
temperature
solvent
tank
valve
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
Application number
JP2161311A
Other languages
Japanese (ja)
Other versions
JPH0453594A (en
Inventor
清教 黒木
繁 古屋
Original Assignee
株式会社東京洗染機械製作所
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 株式会社東京洗染機械製作所 filed Critical 株式会社東京洗染機械製作所
Priority to JP2161311A priority Critical patent/JPH0636838B2/en
Publication of JPH0453594A publication Critical patent/JPH0453594A/en
Publication of JPH0636838B2 publication Critical patent/JPH0636838B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • 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、溶剤を用いてドライクリーニングする装置に
おいて、洗浄により汚れた溶剤を蒸留により精製する
際、安定した状態で能率的に蒸留することができる蒸留
温度制御方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of use] The present invention relates to an apparatus for dry cleaning using a solvent, which is capable of efficiently distilling in a stable state when purifying a solvent soiled by washing by distillation. The present invention relates to a distillation temperature control method capable of controlling the distillation temperature.

〔従来の技術〕[Conventional technology]

第2図は従来例のドライクリーニング装置を示す系統図
である。
FIG. 2 is a system diagram showing a conventional dry cleaning device.

次に、この従来例の装置を用いた従来例のドライクリー
ニング方法について説明する。
Next, a conventional dry cleaning method using this conventional apparatus will be described.

洗浄槽1は、外胴1a内に多孔板製の内胴1bを回転駆
動可能に設置した構造である。
The cleaning tank 1 has a structure in which an inner case 1b made of a perforated plate is rotatably installed inside an outer case 1a.

洗浄工程においては、洗浄しようとする衣類などの被洗
物を内胴1b内に入れ、溶剤タンク2内の溶剤をポンプ
3で吸入,圧送し、フィルタ5,冷却器6,バルブ8を
経て洗浄槽1内に注入する。このとき、洗浄槽1内の溶
剤液面は液面フロート9によって検出され、自動的に制
御される。
In the cleaning process, the clothes to be cleaned such as clothes are put in the inner case 1b, the solvent in the solvent tank 2 is sucked and pumped by the pump 3, and the cleaning is performed through the filter 5, the cooler 6 and the valve 8. Pour into tank 1. At this time, the liquid surface of the solvent in the cleaning tank 1 is detected by the liquid surface float 9 and automatically controlled.

洗浄に必要な洗剤は洗剤投入器12により洗浄缶11から吸
い上げられ、一定量を洗浄槽1内に供給される。
The detergent required for cleaning is sucked up by the detergent injector 12 from the cleaning can 11 and supplied to the cleaning tank 1 in a fixed amount.

そして内胴1bを低速で回転させて洗浄工程が行われ
る。
Then, the cleaning process is performed by rotating the inner case 1b at a low speed.

洗浄工程が終わるとバルブ10が開かれ、洗浄槽1内の溶
剤はボタントラップ13で粗粒の異物を除去された後蒸留
器14に流入する。
When the washing process is completed, the valve 10 is opened, and the solvent in the washing tank 1 is flowed into the distiller 14 after the coarse foreign particles are removed by the button trap 13.

上記の蒸留器14には加熱ジャケット24が設けられてい
る。この加熱ジャケット24に加熱用の蒸気が供給されて
蒸留器14内の溶剤が加熱される。26は加熱用蒸気の供給
管路に設けられた開閉弁である。
The distiller 14 is provided with a heating jacket 24. Steam for heating is supplied to the heating jacket 24 to heat the solvent in the distiller 14. An on-off valve 26 is provided in the heating steam supply pipe.

蒸留器14で加熱されて発生した溶剤の蒸気はスチルコン
デンサ25で冷却されて凝縮し、水分分離器28で水分を除
去され、清浄油タンク23内に貯えられる。
The solvent vapor generated by heating in the distiller 14 is cooled and condensed in the still condenser 25, the moisture is removed by the moisture separator 28, and stored in the clean oil tank 23.

一方、溶剤を排出された洗浄槽1内の洗浄済み被洗物は
内胴1bを回転させて軽く脱液した後すすぎ洗いされ
る。
On the other hand, the cleaned object in the cleaning tank 1 from which the solvent has been discharged is rinsed after being lightly drained by rotating the inner case 1b.

すすぎ洗いは、清浄油タンク23内に貯えられていた蒸留
精製済みの溶剤を洗浄槽1内に注入し、内胴1bを低速
回転させて行なう。
Rinsing is performed by injecting the solvent, which has been distilled and purified, stored in the clean oil tank 23 into the cleaning tank 1 and rotating the inner barrel 1b at a low speed.

すすぎ洗いが終わると、バルブ10を開いて洗浄槽1内の
溶剤をボタントラップ13を経て溶剤タンク2内に流下さ
せる。その後、内胴1bを高速で数分間回転させて脱液
工程を行なう。
When the rinsing is completed, the valve 10 is opened to allow the solvent in the cleaning tank 1 to flow into the solvent tank 2 via the button trap 13. Then, the inner barrel 1b is rotated at a high speed for several minutes to perform the liquid removing step.

次いで乾燥工程を行なう。乾燥工程においては、バルブ
21,23は開の状態になっており、三方弁16を循環方向に
切換え、内胴1bを低速回転させながら、フアン15を作
動させる。該ファン15から送出された空気は、三方弁1
6,1次コンデンサ17a,2次コンデンサ17b,ヒータ1
9,洗浄槽1,ダストフイルタ20を順次に流通してフア
ン15に吸入されて循環される。
Then, a drying process is performed. Valve in the drying process
21 and 23 are in the open state, the three-way valve 16 is switched to the circulation direction, and the fan 15 is operated while rotating the inner case 1b at a low speed. The air sent from the fan 15 is a three-way valve 1
6, primary capacitor 17a, secondary capacitor 17b, heater 1
9. The cleaning tank 1 and the dust filter 20 are sequentially circulated, and then sucked into the fan 15 and circulated.

上記の循環空気流は、ヒータ19を通過するとき加熱され
て熱風となり、洗浄槽1を通過するとき被洗物に残って
いる溶剤を蒸発させる。溶剤蒸気を含んだ空気流はダス
トフイルタ20を経てフアン15に吸入され、送出された
後、三方弁16を経て1次コンデンサ17aを流通するとき
冷水で冷却され、2次コンデンサ17bを流通するとき冷
凍機17cから送られる冷媒で冷却される。冷却された空
気流に含まれていた溶剤蒸気は凝縮して回収され、水分
分離器28で水分を除去されて清浄油タンク23に貯えられ
る。乾燥工程は、以上に説明したように、被洗物に残っ
ていた溶剤を蒸発させて被洗物を乾燥させる操作と、蒸
発した溶剤蒸気を凝縮させて回収する操作とが併行して
行なわれる。
The circulating air flow is heated into hot air when passing through the heater 19, and evaporates the solvent remaining on the object to be washed when passing through the cleaning tank 1. The air flow containing the solvent vapor is sucked into the fan 15 via the dust filter 20 and sent out, and then is cooled by cold water when flowing through the three-way valve 16 and the primary condenser 17a, and when flowing through the secondary condenser 17b. It is cooled by the refrigerant sent from the refrigerator 17c. The solvent vapor contained in the cooled air flow is condensed and recovered, the moisture is removed by the moisture separator 28 and stored in the clean oil tank 23. As described above, the drying step is performed concurrently with the operation of evaporating the solvent remaining in the object to be washed to dry the object to be washed and the operation of condensing and recovering the evaporated solvent vapor. .

また、前記蒸留工程は、洗浄工程が終了した後乾燥工程
が終了するまでの間に行なう。
The distillation step is performed after the washing step and before the drying step.

前記の蒸留は、蒸留器14からの蒸発量とスチルコンデン
サ25の冷却能力とがバランスされた状態で行なう必要が
あり、このため、従来は第2図に示すように、蒸留器14
の蒸発槽中に温度検出センサ29を配設し、その温度検出
センサの検出値に基づいて制御部30により前記開閉弁26
を開閉制御している。
The above-mentioned distillation needs to be carried out in a state where the amount of evaporation from the distiller 14 and the cooling capacity of the still condenser 25 are balanced. Therefore, as shown in FIG.
A temperature detection sensor 29 is provided in the evaporation tank of the control unit 30 and the opening / closing valve 26 is controlled by the control unit 30 based on the detection value of the temperature detection sensor.
Is controlled to open and close.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

従来は、前記の如く、蒸留器14の蒸発槽の中に温度検出
センサ29が配設されているため、温度検出センサの表面
が溶剤によって汚染されて正確な温度検出が出来なくな
り、このため、加熱温度が高くなり過ぎて蒸発量とコン
デンサの冷却能力とのバランスがくずれ、蒸発槽中の汚
れた溶剤がスチルコンデンサ25中に吹き出す現象(これ
を突沸現象という)が発生するおそれがある。また、高
温の状態で蒸留を長時間行なうと、溶剤の分解が促進さ
れて装置全体に悪影響を及ぼすおそれがある。このた
め、従来は、蒸留器の内部を頻繁に掃除しなければなら
ず、手間が掛かるという問題がある。
Conventionally, as described above, since the temperature detection sensor 29 is disposed in the evaporation tank of the distiller 14, the surface of the temperature detection sensor is contaminated by the solvent, and accurate temperature detection cannot be performed. There is a possibility that the heating temperature becomes too high and the balance between the evaporation amount and the cooling capacity of the condenser becomes unbalanced, and the dirty solvent in the evaporation tank blows out into the still condenser 25 (this phenomenon is called bumping phenomenon). Further, if distillation is carried out at a high temperature for a long time, decomposition of the solvent is promoted, which may adversely affect the entire apparatus. Therefore, conventionally, there is a problem that the inside of the distiller must be frequently cleaned, which is troublesome.

本発明は、前記の如き従来技術の問題点を改善し、蒸留
工程に際し、突沸現象を防止すると共に溶剤を分解する
こともなく、しかも能率的に蒸留することができるドラ
イクリーニング装置における蒸留温度制御方法を提供す
ることを目的とする。
The present invention solves the problems of the prior art as described above, prevents the bumping phenomenon during the distillation step, does not decompose the solvent, and can efficiently perform distillation temperature control in a dry cleaning device. The purpose is to provide a method.

〔課題を解決するための手段〕[Means for Solving the Problems]

本発明は、上記の目的を達成するため、低速回転する洗
浄槽中に溶剤を供給して洗浄槽の被洗物を洗浄する洗浄
工程と、洗浄工程終了後洗浄槽を高速回転させて被洗物
から脱液する脱液工程と、脱液工程終了後洗浄槽を乾燥
経路と連通させて加熱空気を洗浄槽と乾燥経路との間に
循環せしめると共にこれにより気化した溶剤をコンデン
サにより凝縮させて回収せしめる乾燥・溶剤回収工程
と、前記洗浄工程終了後洗浄工程により汚れた溶剤を蒸
留して浄化させる蒸留工程とを行なうドライクリーニン
グ装置において、前記蒸留器に至る蒸気供給管に自動開
閉弁と手動減圧弁とを配設し、かつ、蒸留器の加熱ジャ
ケット中に温度検出センサを直接配設し、前記手動減圧
弁を必要とする所望温度が得られるように調整すると共
に、前記温度検出センサの検出値に基づいて前記自動開
閉弁を所望温度以上検出時に閉、所望温度以下検出時に
開となるように制御すべくなしたことを特徴とする。
In order to achieve the above object, the present invention provides a cleaning step of supplying a solvent to a cleaning tank rotating at a low speed to clean an object to be cleaned in the cleaning tank, and rotating the cleaning tank at a high speed after completion of the cleaning step. After the liquid removal process of removing liquid from the object, and after the completion of the liquid removal process, the cleaning tank is connected to the drying path to circulate the heated air between the cleaning tank and the drying path, and the vaporized solvent is condensed by the condenser. In a dry cleaning device that performs a drying / solvent recovery step for recovering and a distillation step for distilling and purifying the dirty solvent by the cleaning step after the cleaning step, an automatic opening / closing valve and a manual valve are provided in a vapor supply pipe leading to the distiller. A pressure reducing valve is installed, and a temperature detecting sensor is directly installed in the heating jacket of the distiller, and the manual pressure reducing valve is adjusted to obtain a desired temperature, and the temperature detecting sensor is installed. Closing the on the basis of the detected value the automatic opening and closing valve when detecting the desired temperature more support, characterized in that none to control so as to open at the time of detection desired temperature or less.

〔作用〕[Action]

本発明は、前記の如く、温度検出センサを蒸留器の加熱
ジャケット中に配設するので、温度検出センサの汚れが
少なくなって長時間に亘る正確な蒸気温度の検出が可能
となり、かつ、減圧弁によって所望温度が得られるよう
に調整しているので、蒸気温度は通常減圧弁によって設
定した所望温度を維持するが、何等かの原因により万一
それより上昇すると開閉弁を閉じて設定した所望温度に
戻し、所望温度以下に下降すると開閉弁を開き、かくし
て、突沸および溶剤の分解を防止しつゝ円滑かつ能率的
な蒸留を行なうことができる。
According to the present invention, as described above, since the temperature detecting sensor is arranged in the heating jacket of the distiller, the temperature detecting sensor is less contaminated and the accurate vapor temperature can be detected for a long time, and the decompression is performed. Since the valve is adjusted to obtain the desired temperature, the steam temperature normally maintains the desired temperature set by the pressure reducing valve, but if it rises above that for some reason, the on-off valve is closed and set as desired. When the temperature is returned to the desired temperature and the temperature falls below the desired temperature, the on-off valve is opened, and thus bumping and decomposition of the solvent can be prevented, and smooth and efficient distillation can be performed.

〔実施例〕〔Example〕

以下、第1図について本発明の実施の一例を説明する。 An example of the embodiment of the present invention will be described below with reference to FIG.

第1図は本発明を適用したドライクリーニング装置の構
成を示し、第2図と同一部分に同一符号を付してその説
明を省略する。
FIG. 1 shows the structure of a dry cleaning apparatus to which the present invention is applied. The same parts as those in FIG. 2 are designated by the same reference numerals and the description thereof will be omitted.

本発明においては、温度検出センサ29を蒸留器14の加熱
ジャケット24中に直接配設し、かつ、蒸留器14に至る蒸
気配管に自動開閉弁26と手動減圧弁31とを配設し、その
手動減圧弁31により所望とする蒸気温度、例えば150℃
(蒸気圧4kg/cm2)に設定し、かつ、前記温度検出セ
ンサ29が設定温度(150℃)以上に達したことを検出す
ると制御部30により自動開閉弁26を閉じ、設定温度より
僅かに低い例えば147℃以下であることを検出すると自
動開閉弁26を開くように開閉制御する。その他の構成は
第2図に示す従来例と同様である。なお、第1図におい
てP1は圧力計である。
In the present invention, the temperature detection sensor 29 is arranged directly in the heating jacket 24 of the still 14, and the automatic opening / closing valve 26 and the manual pressure reducing valve 31 are arranged in the steam pipe leading to the still 14, Manual decompression valve 31 for desired steam temperature, eg 150 ° C
When the vapor pressure is set to 4 kg / cm 2 and the temperature detection sensor 29 detects that the temperature has reached the set temperature (150 ° C.) or higher, the control unit 30 closes the automatic opening / closing valve 26 to slightly lower the set temperature. When it is detected that the temperature is low, for example, 147 ° C. or less, the opening / closing control is performed so that the automatic opening / closing valve 26 is opened. Other configurations are similar to those of the conventional example shown in FIG. In FIG. 1, P1 is a pressure gauge.

本発明は、前記の如く、温度検出センサ29を蒸留器の加
熱ジャケット24中に配設したので、温度検出センサ29は
汚れた溶剤により汚染されることなく、正確な蒸気温度
を検出することができ、しかも、手動減圧弁31により所
望とする蒸気温度を設定したので、蒸留器に送られる蒸
気温度は通常は減圧弁に設定した温度を維持しようとす
るが、何等かの原因例えば一次側の温度や圧力の変動に
より万一設定温度以上に上昇すると温度検出センサ29が
それを検出して制御部30により開閉弁26を閉じ、設定温
度以下のときには同様にして開閉弁26を開き、かくして
例えば150℃〜147℃を維持して突沸および溶剤の分解を
防止しつゝ、円滑にしかも能率的な蒸留を行なうことが
できる。
According to the present invention, as described above, the temperature detecting sensor 29 is arranged in the heating jacket 24 of the still, so that the temperature detecting sensor 29 can detect the accurate vapor temperature without being contaminated by the dirty solvent. Since the desired steam temperature can be set by the manual pressure reducing valve 31, the steam temperature sent to the distiller normally tries to maintain the temperature set in the pressure reducing valve, but some cause such as the primary side Should the temperature rise above the set temperature due to fluctuations in temperature or pressure, the temperature detection sensor 29 will detect it and the control unit 30 will close the open / close valve 26.If the temperature is below the set temperature, the open / close valve 26 will be opened in the same manner. Maintaining 150 to 147 ° C prevents bumping and decomposition of solvent, and enables smooth and efficient distillation.

〔発明の効果〕〔The invention's effect〕

以上述べたように、本発明によれば、ドライクリーニン
グ装置において汚れた溶剤を蒸留する際、突沸および溶
剤の分解を防止しつゝ、円滑にしかも能率的な蒸留を行
なうことができる効果がある。
As described above, according to the present invention, when diluting a dirty solvent in a dry cleaning device, bumping and decomposition of the solvent can be prevented, and smooth and efficient distillation can be performed. .

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明を適用したドライクリーニング装置の構
成を示す系統図、第2図は従来のドライクリーニング装
置の構成を示す系統図である。 1……洗浄槽、2……溶剤タンク、3……ポンプ、5…
…フイルタ、6……冷却器、9……液面フロート、13…
…ボタントラップ、14……蒸留器、15……フアン、17a
……1次コンデンサ、17b……2次コンデンサ、19……
ヒータ、20……ダストフイルタ、23……清浄油タンク、
24……加熱ジャケット、25……スチルコンデンサ、26…
…自動開閉弁、29……温度検出センサ、30……制御部、
31……減圧弁。
FIG. 1 is a system diagram showing a configuration of a dry cleaning device to which the present invention is applied, and FIG. 2 is a system diagram showing a configuration of a conventional dry cleaning device. 1 ... Cleaning tank, 2 ... Solvent tank, 3 ... Pump, 5 ...
… Filter, 6… Cooler, 9… Liquid level float, 13…
… Button trap, 14… Distiller, 15… Juan, 17a
…… Primary capacitor, 17b …… Secondary capacitor, 19 ……
Heater, 20 ... dust filter, 23 ... clean oil tank,
24 ... Heating jacket, 25 ... Still condenser, 26 ...
… Automatic open / close valve, 29 …… Temperature detection sensor, 30 …… Control section,
31 …… Reducing valve.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】低速回転する洗浄槽中に溶剤を供給して洗
浄槽中の被洗物を洗浄する洗浄工程と、洗浄工程終了後
洗浄槽を高速回転させて被洗物から脱液する脱液工程
と、脱液工程終了後洗浄槽を乾燥系路と連通させて加熱
空気を洗浄槽と乾燥経路との間に循環せしめると共にこ
れにより気化した溶剤をコンデンサにより凝縮させて回
収せしめる乾燥・溶剤回収工程と、前記洗浄工程終了後
洗浄工程により汚れた溶剤を蒸留して浄化させる蒸留工
程とを行なうドライクリーニング装置において、前記蒸
留器に至る蒸気供給管に自動開閉弁と手動減圧弁とを配
設し、かつ、蒸留器の加熱ジャケット中に温度検出セン
サを直接配設し、前記手動減圧弁を必要とする所望温度
が得られるように調整すると共に、前記温度検出センサ
の検出値に基づいて前記自動開閉弁を所望温度以上検出
時に閉、所望温度以下検出時に開となるように制御すべ
くなしたことを特徴とするドライクリーニングにおける
蒸留温度制御方法。
1. A cleaning step of supplying a solvent to a cleaning tank rotating at a low speed to clean an object to be cleaned in the cleaning tank, and a cleaning tank rotating at a high speed after completion of the cleaning step to remove liquid from the object to be cleaned. After completion of the liquid process and the dewatering process, the washing tank is connected to the drying system passage to circulate the heated air between the washing tank and the drying passage, and the vaporized solvent is condensed by the condenser and recovered. In a dry cleaning device that performs a recovery step and a distillation step for distilling away and purifying the solvent contaminated by the cleaning step after completion of the cleaning step, an automatic opening / closing valve and a manual pressure reducing valve are arranged in a vapor supply pipe leading to the distiller. The temperature detecting sensor is installed directly in the heating jacket of the distiller, and the manual pressure reducing valve is adjusted to obtain the desired temperature. Based on the detected value of the temperature detecting sensor. Closing the serial automatic opening and closing valve when detecting more than a desired temperature, distillation temperature control method in dry cleaning, characterized in that none to control so as to open at the time of detection desired temperature or less.
JP2161311A 1990-06-21 1990-06-21 Distillation temperature control method in dry cleaning Expired - Lifetime JPH0636838B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2161311A JPH0636838B2 (en) 1990-06-21 1990-06-21 Distillation temperature control method in dry cleaning

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2161311A JPH0636838B2 (en) 1990-06-21 1990-06-21 Distillation temperature control method in dry cleaning

Publications (2)

Publication Number Publication Date
JPH0453594A JPH0453594A (en) 1992-02-21
JPH0636838B2 true JPH0636838B2 (en) 1994-05-18

Family

ID=15732690

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2161311A Expired - Lifetime JPH0636838B2 (en) 1990-06-21 1990-06-21 Distillation temperature control method in dry cleaning

Country Status (1)

Country Link
JP (1) JPH0636838B2 (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5944572A (en) * 1982-09-06 1984-03-13 旭化成株式会社 Method and device for heating circulating air for drying
JPH0325756Y2 (en) * 1987-08-18 1991-06-04
JP3017793U (en) * 1994-11-01 1995-11-07 綜合器材株式会社 Supply cylinder, exhaust pipe connection part, coupling retaining projection piece

Also Published As

Publication number Publication date
JPH0453594A (en) 1992-02-21

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