JPH038797B2 - - Google Patents

Info

Publication number
JPH038797B2
JPH038797B2 JP63095897A JP9589788A JPH038797B2 JP H038797 B2 JPH038797 B2 JP H038797B2 JP 63095897 A JP63095897 A JP 63095897A JP 9589788 A JP9589788 A JP 9589788A JP H038797 B2 JPH038797 B2 JP H038797B2
Authority
JP
Japan
Prior art keywords
temperature
drying
heater
air
fan
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
JP63095897A
Other languages
Japanese (ja)
Other versions
JPS63288194A (en
Inventor
Tomohiko Ikeda
Yoshifumi Enami
Koichi Kuroda
Hiroaki Kataue
Koichi Hatsuda
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co Ltd
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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP63095897A priority Critical patent/JPS63288194A/en
Publication of JPS63288194A publication Critical patent/JPS63288194A/en
Publication of JPH038797B2 publication Critical patent/JPH038797B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】[Detailed description of the invention]

(イ) 産業上の利用分野 本発明は、石油系の可燃性溶剤によつて洗われ
た衣類を乾燥する衣類乾燥機に関する。 (ロ) 従来の技術 石油系の可燃性溶剤を用いて衣類を洗い、乾燥
するドライクリーナの一例が特開昭60−99300号
公報に示されている。ここでは乾燥の際にヒータ
によつて加熱された乾燥風を用いるが、乾燥運転
中にフイルターの目づまりが生じて乾燥室内の溶
剤のガス濃度が上ると、この濃度を検知して加熱
の停止、運転停止、警報を行なう。 (ハ) 発明が解決しようとする課題 このように斯る石油系溶剤使用のドライクリー
ナにあつては、乾燥運転中に溶剤ガス濃度の爆発
下限界濃度以下になるよう送風量を大としている
が、衣類の温度が低い間は高温乾燥風を大量に送
る割には乾燥効率が上らず、一方ではフイルター
目づまりを的確に検知して爆発を防止する必要が
あつた。 本発明は、石油系溶剤を用いる衣類乾燥機にあ
つて、乾燥運転時に於ける爆発の危険を簡単に防
止せんとするものである。 (ニ) 課題を解決するための手段 本発明の衣類乾燥機は、石油系の可燃性溶剤で
洗われた衣類を収容する乾燥室と、この乾燥室内
に乾燥風を循環させるための循環路と、この循環
路内に配設された送風手段、乾燥風を加熱するた
めの加熱手段及び衣類と熱交換した後の乾燥風を
凝縮する凝縮手段と、乾燥風の温度を検知し出力
する温度センサーと、この温度センサーからの温
度信号と上記可燃性溶剤の引火点温度より低い所
定温度とを比較する比較手段と、乾燥中は前記送
風手段、加熱手段及び凝縮手段の全てを駆動する
と共に、前記比較手段からの信号に応じて、乾燥
風の温度が前記所定温度よりも高い場合に前記加
熱手段のみの駆動を停止するよう指令する制御手
段とを具備したものである。 (ホ) 作用 乾燥室内に送給される乾燥風の温度は、温度セ
ンサーによつて測定されており、この温度が可燃
性溶剤の引火点温度より低い所定温度になるよう
に、センサーからの温度信号に基づいて作動制御
手段がヒータとフアンを制御する。即ち乾燥風の
温度が所定温度を保持するようにヒータをON−
OFFし、フアンを連続的にONする。従つて、乾
燥室内では爆発の危険のない低温の乾燥風が送給
され、また例えば連続的に大量に供給することに
より乾燥効率を維持するようにする。 (ヘ) 実施例 第2図に基づいてドライクリーナとしての機構
から説明すると、1は洗濯及び乾燥運転では低速
で、脱液運転では高速で夫々回転するドラムで、
洗濯兼乾燥室2内に配設してある。3は洗濯運転
時に洗濯兼乾燥室2にタンク4から石油系溶剤
(引火点温度42℃)を供給するポンプ、5は給液
弁、6はフイルターである。7は脱液、排液時に
洗濯兼乾燥室2内の溶剤をタンク4に戻すための
排液弁である。 ここで、洗濯兼乾燥室2は、上部左右に入口
8、出口9を開口した循環路10を連設してい
る。この循環路10は、入口8から出口9まで順
に、リントフイルター11、フアン12、冷水等
を通すパイプから成る凝縮装置13、電気或いは
スチーム等のヒータ14を配設している。15は
フアン12を駆動するモータ、16は出口9に在
つて洗濯兼乾燥室2に循環する風の温度を検知す
るサーミスタ等の温度センサー、17は凝縮装置
13によつて凝縮、液化した溶剤等を集めて水を
分離した後にタンク4に戻す水分離器である。 面して、第1図で示すように、ドラム1を駆動
するモータ18、ポンプ3、フアンモータ15、
ヒータ14、給液弁5、排液弁7及び凝縮装置1
3のための冷水弁19は、作動制御手段としての
マイクロコンピユータ20に組込まれた運転プロ
グラムに従つて制御され、斯るマイクロコンピユ
ータ20には操作スイツチ等の入力部21及び温
度センサー16から所定の信号が入力される。特
に、温度センサー16からの出力電圧はラダー回
路22からのラダー出力と比較器23によつて常
時比較され、マイクロコンピユータ20自体に温
度信号として読み込まれている。尚、ラダー回路
22を省いて、比較器23に変更可能な基準入力
を付設しても良い。 マイクロコンピユータ20に予め記憶された
(組込まれた)運転プログラムは、給液、洗い、
排脱液、乾燥(回収)の各運転を逐次的に実行す
るものを基本としており、また適宜時間の変更、
運転の省略等が可能にしてある。 ここで、乾燥(回収)運転について第3図のフ
ローチヤートに基づいて説明する。即ち、プログ
ラムが乾燥運転に移行した時、或いは独立した乾
燥運転では、まず温度センサー16が測定する乾
燥風の温度と石油系溶剤の引火点温度より低い所
定温度、例えば40℃とが比較される。測定温度が
40℃以下であれば、ヒータ14、フアンモータ1
5及びドラム駆動モータ18をONし、給液弁5
及び排液弁7を閉じ、冷水弁19を開くように、
また40℃を越えればヒータ14をOFFするよう
にマイクロコンピユータ20が制御する。かくし
て、ドラム1内では溶剤で洗われ、溶剤を含有し
た衣類を引火点温度以下の低温の乾燥風によつて
乾燥し、凝縮装置13では溶剤ガスが低温である
だけに効率良く凝縮、液化して水分離器17に送
つている。 一般に高温の乾燥風によつて乾燥運転を実行す
れば、乾燥効率が向上すると云われており、本実
施例の如き低温乾燥では斯る効率が課題になる。
しかし、本実施例では従来と同じ熱量のヒータを
用いる中で予め送風量を大きく設計し、衣類に与
える総熱量を下げずに乾燥風の温度を下げ、乾燥
運転時間の延長を避けているのである。ここで、
次の表1と表2は、同熱量のヒータ(1224W)を
用い、同一外気温(17℃)の中で、送風量を2.65
m3/分として乾燥風温度を39℃に下げた場合と送
風量を0.83m3/分として乾燥風温度を83℃に上げ
た場合の測定結果を示している。また、表3と表
4は、同熱量のヒータ(1224W)を用い、略同一
外気温(15℃〜17℃)の中で、送風量を2.53m3
分として乾燥風温度を40℃に下げた場合と送風量
を0.88m3/分として乾燥風温度を83℃に上げた場
合の測定結果を示している。
(a) Industrial Application Field The present invention relates to a clothes dryer for drying clothes washed with a petroleum-based flammable solvent. (b) Prior Art An example of a dry cleaner that washes and dries clothes using a petroleum-based flammable solvent is disclosed in Japanese Patent Application Laid-open No. 60-99300. Here, drying air heated by a heater is used during drying, but if the filter becomes clogged during drying operation and the concentration of solvent gas in the drying chamber increases, this concentration will be detected and the heating will be stopped. Stop operation and issue a warning. (c) Problems to be Solved by the Invention As described above, in dry cleaners that use petroleum-based solvents, the amount of air blown is increased during drying operation so that the concentration of solvent gas is below the lower explosive limit concentration. However, when the temperature of the clothes is low, the drying efficiency cannot be improved even though a large amount of high-temperature drying air is sent, and on the other hand, it was necessary to accurately detect clogged filters to prevent explosions. The present invention aims to easily prevent the risk of explosion during drying operation in a clothes dryer that uses petroleum-based solvents. (d) Means for Solving the Problems The clothes dryer of the present invention includes a drying chamber for storing clothes washed with a petroleum-based flammable solvent, and a circulation path for circulating drying air in the drying chamber. , a blowing means disposed in this circulation path, a heating means for heating the drying air, a condensing means for condensing the drying air after heat exchange with the clothes, and a temperature sensor for detecting and outputting the temperature of the drying air. a comparison means for comparing the temperature signal from the temperature sensor with a predetermined temperature lower than the flash point temperature of the flammable solvent; and control means for instructing to stop driving only the heating means when the temperature of the drying air is higher than the predetermined temperature, in response to a signal from the comparison means. (E) Effect The temperature of the drying air sent into the drying chamber is measured by a temperature sensor, and the temperature from the sensor is adjusted so that this temperature becomes a predetermined temperature lower than the flash point temperature of the flammable solvent. An operation control means controls the heater and fan based on the signal. In other words, turn on the heater so that the temperature of the drying air remains at the specified temperature.
OFF, then turn the fan ON continuously. Therefore, low-temperature drying air without the risk of explosion is fed into the drying chamber, and the drying efficiency is maintained by, for example, continuously feeding a large amount of drying air. (F) Embodiment To explain the mechanism of the dry cleaner based on FIG. 2, 1 is a drum that rotates at a low speed during washing and drying operations and at a high speed during a dehydrating operation.
It is located inside the washing/drying room 2. 3 is a pump that supplies a petroleum solvent (flash point temperature: 42° C.) from a tank 4 to the washing/drying chamber 2 during washing operation, 5 is a liquid supply valve, and 6 is a filter. Reference numeral 7 denotes a drain valve for returning the solvent in the washing/drying chamber 2 to the tank 4 at the time of liquid removal and draining. Here, the washing/drying room 2 has a circulation path 10 with an inlet 8 and an outlet 9 opened on the left and right sides of the upper part. This circulation path 10 is provided with a lint filter 11, a fan 12, a condensing device 13 consisting of a pipe for passing cold water, etc., and a heater 14 such as electric or steam heater 14 in this order from the inlet 8 to the outlet 9. 15 is a motor that drives the fan 12; 16 is a temperature sensor such as a thermistor that is located at the outlet 9 and detects the temperature of the air circulating in the washing/drying room 2; and 17 is a solvent condensed and liquefied by the condensing device 13. This is a water separator that collects water, separates it, and then returns it to tank 4. As shown in FIG. 1, a motor 18 for driving the drum 1, a pump 3, a fan motor 15,
Heater 14, liquid supply valve 5, liquid drain valve 7, and condensing device 1
The cold water valve 19 for 3 is controlled according to an operation program built into a microcomputer 20 as an operation control means, and the microcomputer 20 receives predetermined signals from an input unit 21 such as an operation switch and a temperature sensor 16. A signal is input. In particular, the output voltage from the temperature sensor 16 is constantly compared with the ladder output from the ladder circuit 22 by the comparator 23, and is read into the microcomputer 20 itself as a temperature signal. Note that the ladder circuit 22 may be omitted and the comparator 23 may be provided with a changeable reference input. The operation program stored (incorporated) in the microcomputer 20 includes liquid supply, washing,
Basically, each operation of draining, deliquid, and drying (recovery) is executed sequentially, and the time can be changed as appropriate.
It is possible to omit driving. Here, the drying (recovery) operation will be explained based on the flowchart of FIG. 3. That is, when the program shifts to a drying operation, or in an independent drying operation, the temperature of the drying air measured by the temperature sensor 16 is first compared with a predetermined temperature lower than the flash point temperature of the petroleum solvent, for example, 40°C. . The measured temperature
If it is below 40℃, heater 14, fan motor 1
5 and the drum drive motor 18, and turn on the liquid supply valve 5.
and close the drain valve 7 and open the cold water valve 19.
Further, the microcomputer 20 controls the heater 14 to be turned off if the temperature exceeds 40°C. Thus, in the drum 1, the clothes washed with the solvent and containing the solvent are dried by drying air at a low temperature below the flash point temperature, and in the condensing device 13, the solvent gas is efficiently condensed and liquefied because the temperature is low. The water is then sent to the water separator 17. Generally, it is said that drying efficiency is improved if drying operation is performed using high-temperature drying air, but such efficiency becomes an issue in low-temperature drying as in this embodiment.
However, in this embodiment, while using a heater with the same amount of heat as the conventional heater, the amount of air blown is designed to be large in advance, and the temperature of the drying air is lowered without reducing the total amount of heat given to the clothes, thereby avoiding an extension of the drying operation time. be. here,
The following Tables 1 and 2 show that using heaters with the same heat output (1224W) and at the same outside temperature (17℃), the air flow rate was 2.65.
The measurement results are shown when the drying air temperature was lowered to 39°C at m 3 /min and when the drying air temperature was raised to 83°C at air flow rate of 0.83m 3 /min. In addition, Tables 3 and 4 show that using heaters with the same calorific value (1224 W) and at approximately the same outside temperature (15°C to 17°C), the amount of air blown was 2.53 m 3 /
The measurement results are shown when the drying air temperature was lowered to 40°C per minute and when the drying air temperature was raised to 83°C with an air flow rate of 0.88m 3 /min.

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】 即ち、表1と表3は低温乾燥運転を示している
が、表2と表4の高温乾燥運転に比べて乾燥運転
の所要時間に大きな差はなく、所定の乾燥効率が
維持できている。 乾燥運転時間は低温乾燥運転の場合には予め少
し長めに設定できる。 ヒータ14を2分割し、一方を連続で、他方を
温度センサー16によつて間欠で夫々作動させ、
分割ヒータ14のON−OFFで所定温度を保持し
ても良い。 また、加熱量を一定としてフアンモータ15を速
度制御して送風量を増減し、所定温度を保持して
も良い。 そして、本実施例は溶剤を回収する型式である
が、凝縮装置13を省き、フアン12によつて外
気をヒータ14を介して乾燥室2内に吸引し、乾
燥後には外部へ放出する型式としても良い。 また、本実施例はヒータ14をON−OFFする
と共にフアン12の送風量を予め増加しておくこ
とにより、低温乾燥を全運転時間に亘つて実行し
ているが、30分前後の乾燥時間の最初の12分程度
を低温乾燥運転とすると、この運転中に当初低温
である衣類と効果的に熱交換が行なわれる。当初
から高温の乾燥風を供給しても熱交換せずに素通
りするものが多く、無駄がある。この低温乾燥後
には衣類の温度も上り切つているので、ここから
高温乾燥を実行すると全体の乾燥効率が上る。因
みに、ほぼ同一の条件で当初から高温乾燥した場
合に比べて3分程度の時間が短縮できた。表5が
高温乾燥を続けた場合、表6が低温乾燥に続いて
高温乾燥を行なつた場合を示している。この実施
例は通常の市水で洗つた衣類の乾燥機にも簡単に
適用できる。
[Table] In other words, although Tables 1 and 3 show low-temperature drying operation, there is no significant difference in the time required for the drying operation compared to the high-temperature drying operation in Tables 2 and 4, and the specified drying efficiency cannot be maintained. ing. The drying operation time can be set slightly longer in advance in the case of low temperature drying operation. The heater 14 is divided into two, one is operated continuously and the other is operated intermittently by the temperature sensor 16,
A predetermined temperature may be maintained by turning the divided heater 14 ON and OFF. Alternatively, the heating amount may be kept constant and the speed of the fan motor 15 may be controlled to increase or decrease the amount of air blown to maintain a predetermined temperature. In this embodiment, the solvent is recovered, but the condensing device 13 is omitted, and the outside air is sucked into the drying chamber 2 via the heater 14 by the fan 12, and then released to the outside after drying. Also good. Furthermore, in this embodiment, low-temperature drying is performed for the entire operating time by turning the heater 14 on and off and increasing the air flow rate of the fan 12 in advance. If the first 12 minutes are a low-temperature drying operation, heat exchange is effectively performed with the clothing, which is initially at a low temperature, during this operation. Even if high-temperature dry air is supplied from the beginning, it often passes through without heat exchange, resulting in waste. After this low-temperature drying, the temperature of the clothes has already risen, so if you perform high-temperature drying from this point on, the overall drying efficiency will increase. Incidentally, compared to the case where high temperature drying was performed from the beginning under almost the same conditions, the time could be reduced by about 3 minutes. Table 5 shows the case where high temperature drying was continued, and Table 6 shows the case where high temperature drying was performed following low temperature drying. This embodiment can be easily applied to a dryer for clothes washed with normal city water.

【表】【table】

【表】 (ト) 発明の効果 本発明に依れば、爆発の危険の無い状態で、し
かも通常の効率に近い効率で乾燥運転を遂行で
き、きわめて安全な衣類乾燥機を簡単な構成で提
供できるものである。
[Table] (G) Effects of the Invention According to the present invention, an extremely safe clothes dryer is provided with a simple configuration, which can carry out drying operation without the risk of explosion and at an efficiency close to normal efficiency. It is possible.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明による乾燥機能を組込んだドラ
イクリーナの制御回路図、第2図は全体機構図、
第3図は動作説明のためのフローチヤートであ
る。 2…洗濯兼乾燥室、11…リントフイルター、
12…フアン、13…凝縮装置、14…ヒータ、
15…フアンモータ、16…温度センサー、20
…マイクロコンピユータ、23…比較器。
Fig. 1 is a control circuit diagram of a dry cleaner incorporating a drying function according to the present invention, Fig. 2 is an overall mechanical diagram,
FIG. 3 is a flowchart for explaining the operation. 2...Washing and drying room, 11...Lint filter,
12... Fan, 13... Condensing device, 14... Heater,
15...Fan motor, 16...Temperature sensor, 20
...Microcomputer, 23...Comparator.

Claims (1)

【特許請求の範囲】[Claims] 1 石油系の可燃性溶剤で洗われた衣類を収容す
る乾燥室と、この乾燥室内にフアンによつて発生
される乾燥風を循環させるための循環路と、この
循環路内に配設され乾燥風を加熱するためのヒー
タ及び衣類と熱交換した後の乾燥風を凝縮する凝
縮装置と、乾燥風の温度を検知し出力する温度セ
ンサーと、この温度センサーからの温度信号と前
記可燃性溶剤の引火点温度より低い所定温度とを
比較する比較器と、前記フアンとヒータ及び凝縮
装置の動作を制御する制御手段とからなり、前記
制御手段は乾燥中にフアンとヒータ及び凝縮装置
とを駆動せしめ、比較器からの信号に基づいて乾
燥風の温度が前記所定温度よりも高い時にヒータ
のみの駆動を停止せしめるように動作することを
特徴とする衣類乾燥機。
1. A drying room for storing clothes washed with a petroleum-based flammable solvent, a circulation path for circulating drying air generated by a fan in this drying room, and a drying chamber installed within this circulation path. A heater for heating the air, a condensing device for condensing the drying air after heat exchange with clothing, a temperature sensor for detecting and outputting the temperature of the drying air, and a temperature signal from the temperature sensor and the temperature of the flammable solvent. It comprises a comparator that compares the temperature with a predetermined temperature lower than the flash point temperature, and a control means that controls the operation of the fan, heater, and condensing device, and the control means drives the fan, heater, and condensing device during drying. A clothes dryer, characterized in that the clothes dryer operates to stop driving only the heater when the temperature of the drying air is higher than the predetermined temperature based on a signal from a comparator.
JP63095897A 1988-04-19 1988-04-19 Clothing dryer Granted JPS63288194A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63095897A JPS63288194A (en) 1988-04-19 1988-04-19 Clothing dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63095897A JPS63288194A (en) 1988-04-19 1988-04-19 Clothing dryer

Publications (2)

Publication Number Publication Date
JPS63288194A JPS63288194A (en) 1988-11-25
JPH038797B2 true JPH038797B2 (en) 1991-02-06

Family

ID=14150096

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63095897A Granted JPS63288194A (en) 1988-04-19 1988-04-19 Clothing dryer

Country Status (1)

Country Link
JP (1) JPS63288194A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0775640B2 (en) * 1992-08-24 1995-08-16 三洋電機株式会社 Dryer
JP5976494B2 (en) * 2012-10-17 2016-08-23 象印マホービン株式会社 Futon dryer and control method thereof
JP6116854B2 (en) * 2012-10-17 2017-04-19 象印マホービン株式会社 Futon dryer and control method thereof

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* Cited by examiner, † Cited by third party
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DE2242632C3 (en) * 1972-08-30 1981-05-21 BÖWE Maschinenfabrik GmbH, 8900 Augsburg Method and device for drying textiles or the like treated with volatile solvents.

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JPS63288194A (en) 1988-11-25

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