JPS6342953Y2 - - Google Patents

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Publication number
JPS6342953Y2
JPS6342953Y2 JP5488083U JP5488083U JPS6342953Y2 JP S6342953 Y2 JPS6342953 Y2 JP S6342953Y2 JP 5488083 U JP5488083 U JP 5488083U JP 5488083 U JP5488083 U JP 5488083U JP S6342953 Y2 JPS6342953 Y2 JP S6342953Y2
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JP
Japan
Prior art keywords
temperature
drying
heater
drying air
outlet
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
Application number
JP5488083U
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Japanese (ja)
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JPS59160099U (en
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Priority to JP5488083U priority Critical patent/JPS59160099U/en
Publication of JPS59160099U publication Critical patent/JPS59160099U/en
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Description

【考案の詳細な説明】 (イ) 産業上の利用分野 本考案はドライクリーナに関するものである。[Detailed explanation of the idea] (b) Industrial application fields The present invention relates to a dry cleaner.

(ロ) 従来技術 ドライクリーナは、ドラムを有する外槽に送風
フアンによる循環型の乾燥通風路を接続し、この
乾燥通風路中に凝縮器と加熱器を順に配設してい
る。凝縮器はウオータチラー等により冷却された
水冷媒を流通させ、乾燥風中の溶剤を凝縮して別
途回収せしめる。また、加熱器は蒸溜器から水分
離器に向う蒸溜溶剤を熱媒として流通させ、乾燥
風を加熱して外槽に送ると共に、蒸溜溶剤を液化
せしめる。
(B) Prior Art A dry cleaner has an outer tank having a drum connected to a circulation type drying air passage using a blower fan, and a condenser and a heater are arranged in this order in this drying air passage. The condenser circulates a water refrigerant cooled by a water chiller or the like, condenses the solvent in the drying air, and collects it separately. Further, the heater circulates the distillation solvent from the distiller to the water separator as a heating medium, heats the dry air and sends it to the outer tank, and liquefies the distillation solvent.

加熱器による加熱量は大きくて通常の乾燥風の
温度は約50℃になるので、乾燥工程は比較的短時
間で終了させることができる。一方、加熱器内の
蒸溜溶剤にとつては蒸溜終了まで乾燥風によつて
冷却されねばならないので、所定の乾燥工程時間
が必要であつた。
Since the heating amount by the heater is large and the temperature of normal drying air is about 50°C, the drying process can be completed in a relatively short time. On the other hand, since the distillation solvent in the heater must be cooled by drying air until the distillation is completed, a predetermined drying process time is required.

そこで、従来は加熱器出口での乾燥風の温度を
検知し、これが一定値(約39℃)に低下するまで
乾燥工程を続けるようにしていた。ところが、乾
燥風路中には凝縮器も配設してあるので、出口温
度はここでの冷却能力に応じて変化し、蒸溜状況
に対応できなくなることがあつた。つまり、冷却
能力が大きいと蒸溜終了と共に出口温度は低下し
やすいが、冷却能力が小さいと出口温度は蒸溜が
終了しているにも拘らず仲々一定値まで低下せ
ず、無駄な乾燥運転を続けることになつた。
Conventionally, the temperature of the drying air at the outlet of the heater was detected, and the drying process was continued until the temperature dropped to a certain value (approximately 39°C). However, since a condenser is also provided in the drying air path, the outlet temperature changes depending on the cooling capacity of the condenser, which sometimes makes it impossible to adapt to the distillation conditions. In other words, if the cooling capacity is large, the outlet temperature tends to drop as distillation ends, but if the cooling capacity is small, the outlet temperature does not drop to a constant value even after distillation has finished, and wasteful drying continues. It became a matter of fact.

(ハ) 考案の目的 本考案は加熱器の入口、出口の各温度を検知
し、その温度差により工程制御を行なつて乾燥工
程の適正化を図ることを目的とする。
(c) Purpose of the invention The purpose of the invention is to detect the temperatures at the inlet and outlet of the heater, and to control the process based on the temperature difference to optimize the drying process.

(ニ) 考案の構成 本考案は加熱器の入口、出口での乾燥風の温度
を検知する感温素子と、この検知温度の差を比較
して所定温度差にて乾燥工程を終了させる制御手
段を具備したドライクリーナである。従つて、凝
縮器での冷却能力に応じて入口温度が変化する
が、この温度と出口温度の差でもつて制御するの
で、冷却能力とは無関係に乾燥工程の終了時期を
設定でき、乾燥工程を効率良く実行することがで
きるものである。
(d) Structure of the invention The invention includes a temperature sensing element that detects the temperature of the drying air at the inlet and outlet of the heater, and a control means that compares the difference between the detected temperatures and ends the drying process when a predetermined temperature difference is reached. It is a dry cleaner equipped with Therefore, the inlet temperature changes depending on the cooling capacity of the condenser, but since it is controlled by the difference between this temperature and the outlet temperature, the end time of the drying process can be set regardless of the cooling capacity, and the drying process can be It can be executed efficiently.

(ホ) 実施例 図面に基づいて説明すると、1は回転ドラム
(図示せず)を内装した外槽、2は溶剤のタンク、
3は給液ポンプで、洗濯開始時にはタンク2内の
溶剤は給液ポンプ3によつて一方向弁4及び電気
制御される給液バルブ5を介して外槽1に供給さ
れる。6は溶剤の循環路7中に設けられた循環
用、ドレン用のポンプで、洗濯運転中に外槽1内
の溶剤を下部から上部に給液バルブ5を介して循
環せしめる。尚、洗濯運転中には回転ドラムは低
速で反転駆動されている。
(E) Example To explain based on the drawings, 1 is an outer tank with a rotating drum (not shown) inside, 2 is a solvent tank,
3 is a liquid supply pump, and at the start of washing, the solvent in the tank 2 is supplied by the liquid supply pump 3 to the outer tank 1 via a one-way valve 4 and an electrically controlled liquid supply valve 5. Reference numeral 6 denotes a circulation/drain pump provided in the solvent circulation path 7, which circulates the solvent in the outer tub 1 from the lower part to the upper part via the liquid supply valve 5 during the washing operation. Note that during the washing operation, the rotating drum is driven in reverse at a low speed.

8はポンプ6上流の循環路7から分岐し、終端
を外槽1の上部に連通させた乾燥通風路で、下部
の始端側から順にフイルタ9、フロートを用いた
液位スイツチ10、モータ駆動の送風フアン1
1、凝縮器12及び加熱器13が設けてある。
8 is a drying ventilation path which branches from the circulation path 7 upstream of the pump 6 and whose terminal end communicates with the upper part of the outer tank 1; Blower fan 1
1, a condenser 12 and a heater 13 are provided.

ここで、液位スイツチ10は洗濯運転時に乾燥
通風路8内に浸入する溶剤を検知し、外槽1内の
液位を制御している。また、凝縮器12は蛇行し
ており、一端をバルブ14を介してウオータチラ
ーの流出側Aに接続すると共に、他端を水分離器
15内の冷却コイル16及びタンク2内の冷却コ
イル17を介してウオータチラーの流入側Bに接
続している。そして、加熱器13も蛇行してお
り、一端を蒸溜器18に接続すると共に、他端を
水分離器15に接続している。
Here, the liquid level switch 10 detects the solvent entering the drying air passage 8 during the washing operation, and controls the liquid level in the outer tank 1. The condenser 12 has a meandering shape, and one end is connected to the outflow side A of the water chiller via a valve 14, and the other end is connected to the cooling coil 16 in the water separator 15 and the cooling coil 17 in the tank 2. It is connected to the inlet side B of the water chiller via the water chiller. The heater 13 also has a meandering shape, with one end connected to the distiller 18 and the other end connected to the water separator 15.

水分離器15はタンク2に接続されており、内
部にはフロートスイツチ19を配設している。
The water separator 15 is connected to the tank 2, and has a float switch 19 disposed therein.

20は乾燥通風路8の凝縮器12が在る場所に
形成された集合部で、乾燥運転中に凝縮した溶剤
を集め、水分離器15に流すようにしている。2
1,22は乾燥通風路8の凝縮器12の上流側と
加熱器13の下流側を同時に開閉する排気弁と吸
気弁で、乾燥運転時に開放して外部への排気孔2
3と外部からの吸気孔24を閉成し(図中点線位
置)、脱臭運転時には閉成して排気孔23及び吸
気孔24を開放する(図中実線位置)。
Reference numeral 20 denotes a collection part formed at a location of the condenser 12 in the drying ventilation passage 8, which collects the solvent condensed during the drying operation and flows it to the water separator 15. 2
Reference numerals 1 and 22 designate exhaust valves and intake valves that simultaneously open and close the upstream side of the condenser 12 and the downstream side of the heater 13 in the drying ventilation path 8, which are opened during drying operation to open the exhaust hole 2 to the outside.
3 and the intake hole 24 from the outside are closed (dotted line position in the figure), and closed during deodorizing operation, and the exhaust hole 23 and intake hole 24 are opened (solid line position in the figure).

25は蒸溜器18を循環路7に分岐接続する際
に介挿された電気制御のドレンバルブで、一方で
は手動で制御できるようにしてあり、通常は洗濯
運転後の排液工程に自動的に開放し、その後の脱
液工程の中間で自動的に閉成される。26は蒸溜
器18の加熱室内に配設されたヒータで、その通
断電が時間的に制御されている。27は蒸溜器1
8の所定位置に配設された照明ランプ28と、こ
れに対向するCdS等からなる光検知素子29とか
ら成る液位検知装置である。30は送風フアン1
1から蒸溜器18に送風して蒸溜溶剤の導出を促
す送風路である。
Reference numeral 25 denotes an electrically controlled drain valve inserted when connecting the distiller 18 to the circulation path 7. On the other hand, it can be controlled manually, and normally it is automatically operated in the draining process after washing operation. It opens and then closes automatically in the middle of the subsequent dewatering process. Reference numeral 26 denotes a heater disposed within the heating chamber of the distiller 18, and its energization and disconnection are temporally controlled. 27 is distiller 1
This liquid level detection device is composed of an illumination lamp 28 disposed at a predetermined position of 8, and a photodetection element 29 made of CdS or the like facing the illumination lamp 28. 30 is the ventilation fan 1
This is an air passage that blows air from the distiller 1 to the distiller 18 to promote the extraction of the distillation solvent.

31,32は乾燥通風路8内で加熱器13の入
口、出口での乾燥風の温度を検知するサーミスタ
等から成る感温素子で、その検知結果を第2図で
示す中央制御装置33、読み出し専用メモリ34
等から成る制御装置35に入力するようにしてい
る。
Reference numerals 31 and 32 indicate temperature sensing elements such as thermistors that detect the temperature of the drying air at the inlet and outlet of the heater 13 in the drying ventilation passage 8, and the detection results are read out by the central control unit 33 shown in FIG. Dedicated memory 34
The information is inputted to a control device 35 consisting of, etc.

尚、36…は一方向弁、37はソープ投入用の
ホツパーである。
In addition, 36... is a one-way valve, and 37 is a hopper for soap injection.

通常の洗濯工程が終了すると、溶剤はポンプ6
によつてドレンバルブ25を介して蒸溜器18内
に入れられる。この間、外槽1内では脱液工程ま
で進む。この工程中にヒータ26は通電されて準
備している。バルブ14が開放され、送風フアン
11が駆動することにより、蒸溜器18では蒸溜
運転が始まり、外槽1では脱液工程後にドラムを
低速で反転させつつ乾燥運転が始まる。ドレンバ
ルブ25及びポンプ6は乾燥運転の初期に閉成、
停止する。
When the normal washing process is finished, the solvent is pumped 6
is introduced into the distiller 18 via the drain valve 25. During this time, inside the outer tank 1, the process progresses to the dewatering process. During this process, the heater 26 is energized and prepared. When the valve 14 is opened and the blower fan 11 is driven, distillation operation starts in the distiller 18, and drying operation starts in the outer tank 1 while rotating the drum at a low speed after the liquid removal process. The drain valve 25 and pump 6 are closed at the beginning of drying operation.
Stop.

蒸溜器18から出た蒸溜溶剤は加熱器13で乾
燥風と熱交換して放熱し、液化して水分離器15
に入いる。外槽1及び乾燥通風路8内の少しの溶
剤は加熱された乾燥風と共に循環し、凝縮器12
で凝縮し、集合部20に回収されて水分離器15
に入いる。
The distilled solvent discharged from the distiller 18 exchanges heat with the drying air in the heater 13 to radiate heat, and is liquefied to the water separator 15.
Enter. A small amount of solvent in the outer tank 1 and the drying air passage 8 is circulated together with the heated drying air, and the solvent is passed through the condenser 12.
The water is condensed in the water separator 15 and collected in the collecting section 20.
Enter.

液位検知装置27は蒸溜器18内の溶剤が誤操
作や突沸等で異常液位に成ると作動し、ヒータ2
6を断電し且つ異常を報知せしめる。
The liquid level detection device 27 is activated when the solvent in the distiller 18 reaches an abnormal level due to incorrect operation, bumping, etc., and the heater 2
6 is turned off and an abnormality is reported.

凝縮器12の出口、即ち加熱器13の入口と、
その出口の各温度は感温素子31,32によつて
検知されている。この検知信号は制御装置35に
入力され、比較される。そして、入口、出口の温
度の差が所定値(例えば約10℃)まで低下する
と、制御装置35は蒸溜工程及び乾燥工程を終了
させ、脱臭工程に移行せしめる。
an outlet of the condenser 12, that is, an inlet of the heater 13;
Each temperature at the outlet is detected by temperature sensing elements 31 and 32. This detection signal is input to the control device 35 and compared. Then, when the temperature difference between the inlet and the outlet drops to a predetermined value (for example, about 10° C.), the control device 35 ends the distillation process and the drying process and shifts to the deodorizing process.

脱臭工程では、吸排気弁21,22が吸排気孔
23,24を開き、送風フアン11によつて外気
を導入して臭気を追い出す。
In the deodorizing process, the intake and exhaust valves 21 and 22 open the intake and exhaust holes 23 and 24, and the blower fan 11 introduces outside air to expel the odor.

乾燥及び蒸溜工程に於いて、凝縮器12での冷
却能力が大きい時は入口温度は低いが、蒸溜中で
あれば加熱器13で一定に加熱されている。蒸溜
が終了すれば、出口温度は速やかに低下し、温度
差が10℃以下と成る。一方、冷却能力が小さい時
でも加熱器13では一定な加熱が行なわれるの
で、蒸溜終了時には出口温度は低下する。いずれ
にしても、温度差を判定基準にすれば、乾燥風の
温度とは無関係に、また凝縮器12による冷却能
力とは無関係に蒸溜終了時点を測定でき、且つ乾
燥運転の終了を同期させることができる。
In the drying and distillation process, when the cooling capacity of the condenser 12 is large, the inlet temperature is low, but during distillation, the temperature is kept constant by the heater 13. Once the distillation is finished, the outlet temperature quickly decreases to a temperature difference of 10°C or less. On the other hand, even when the cooling capacity is small, constant heating is performed in the heater 13, so the outlet temperature decreases at the end of distillation. In any case, by using the temperature difference as a criterion, it is possible to measure the end of distillation regardless of the temperature of the drying air and the cooling capacity of the condenser 12, and to synchronize the end of the drying operation. I can do it.

制御装置35と例えばサーミスタから成る感温
素子31,32との関係を第2図の制御回路図で
示す。感温素子31,32による入口、出口温度
は電圧に変換されて夫々比較器38,39の比較
入力に入れられ、その比較基準入力としてエクス
パンダー40及びラダー回路41からラダー出力
電圧が入れられる。比較器38,39はラダー出
力電圧による温度データとサーミスタ電圧による
入口、出口温度を比較し、夫々が一致した時に中
央制御装置33に出力する。尚、42はアドレス
バス、43はデータバスを示す。
The relationship between the control device 35 and the temperature sensing elements 31 and 32, which are comprised of, for example, thermistors, is shown in the control circuit diagram of FIG. The inlet and outlet temperatures from the temperature sensing elements 31 and 32 are converted into voltages and input into the comparison inputs of comparators 38 and 39, respectively, and the ladder output voltages from the expander 40 and the ladder circuit 41 are input as comparison reference inputs. The comparators 38 and 39 compare the temperature data based on the ladder output voltage with the inlet and outlet temperatures based on the thermistor voltage, and output the data to the central controller 33 when they match. Note that 42 represents an address bus, and 43 represents a data bus.

この制御回路による乾燥工程を第3図イ,ロの
フローチヤートにより説明すると、まず入口、出
口温度の各測定値及び温度データをクリアーし、
表示プログラムで乾燥工程であることを表示し、
感温素子31,32で検知した入口、出口の各温
度を制御装置35で第3図ロで示すプログラムに
より測定し、また計時プログラムを実行させる。
これによつて、吸、排気弁21,22に閉成信号
が、送風フアン11に駆動信号が、バルブ14に
開放信号が、ドラム回転用のモータに低速反転の
駆動信号が夫々入力される。尚、ドレンバルブ2
5、ポンプ6及びヒータ26の制御については説
明を省略している。
The drying process using this control circuit will be explained using the flowchart in Figure 3 A and B. First, the measured values and temperature data of the inlet and outlet temperatures are cleared,
Display the drying process on the display program,
The temperature at the inlet and outlet detected by the temperature sensing elements 31 and 32 is measured by the control device 35 according to the program shown in FIG. 3B, and a timing program is also executed.
As a result, a closing signal is input to the intake and exhaust valves 21 and 22, a drive signal is input to the blower fan 11, an open signal is input to the valve 14, and a low-speed reversal drive signal is input to the drum rotation motor. In addition, drain valve 2
5. Description of the control of the pump 6 and the heater 26 is omitted.

そして、1秒経過毎に入口、出口の温度が測定
され、温度差が10゜以上の場合は動作を最初から
繰返し、10゜以下の時は脱臭工程へ移行する。
The temperature at the inlet and outlet is measured every second, and if the temperature difference is 10 degrees or more, the operation is repeated from the beginning, and if it is less than 10 degrees, the process moves to the deodorizing process.

第3図ロで示す入口、出口温度測定プログラム
は、温度データがステツプ状に加えられたラダー
回路の出力電圧と入口、出口の各素子の電圧とを
比較し、不一致の場合は夫々、入口温度測定値と
出口温度測定値を+1ずつ+進加算すると共に、
温度データを+1ずつステツプさせる。こうし
て、一致が採れるまでステツプさせ、その間に入
口、出口の温度測定値が加算されている。
The inlet and outlet temperature measurement program shown in Figure 3B compares the output voltage of the ladder circuit to which temperature data is added in steps with the voltage of each element at the inlet and outlet, and if they do not match, the inlet and outlet temperatures are Add the measured value and the outlet temperature measured value by +1, and
Step the temperature data by +1. In this way, steps are taken until a match is found, during which time the inlet and outlet temperature measurements are added.

そして、一致した時まで加算された入口、出口
の温度測定値が10゜以下か否か比較、判定される
のである。
Then, it is compared and determined whether the temperature measurements at the inlet and outlet, which have been added up until they match, are less than 10 degrees.

第4図は負荷の制御系等を省略して測定プログ
ラム及び温度測定値の比較について、構成した他
のフローチヤートを示している。ここでは、電圧
比較が不一致の度に入口、出口温度の各レジスタ
に+1を加算し、時間とは関係なく一致の度に入
口温度レジスタと出口温度レジスタとを比較し、
温度差が10゜あるか否を測定している。
FIG. 4 shows another flowchart configured for comparing the measurement program and temperature measurement values, omitting the load control system and the like. Here, +1 is added to the inlet and outlet temperature registers each time there is a mismatch in the voltage comparison, and the inlet and outlet temperature registers are compared each time there is a match, regardless of time.
We are measuring whether there is a 10° temperature difference.

(ヘ) 考案の効果 本考案は凝縮器の冷却能力や周囲温度とは無関
係に蒸溜終了、乾燥終了を決定でき、無駄な工程
時間を解消して効率の良いドライクリーナを提供
できるものである。
(f) Effects of the invention This invention can determine the end of distillation and drying regardless of the cooling capacity of the condenser or the ambient temperature, eliminates wasted process time, and provides an efficient dry cleaner.

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

第1図は本考案によるドライクリーナの配管系
統図、第2図は制御回路図、第3図イ,ロはフロ
ーチヤート、第4図は他の実施例のフローチヤー
トである。 1……外槽、2……タンク、8……乾燥風路、
11……送風フアン、12……凝縮器、13……
加熱器、15……水分離器、31,32……感温
素子、35……制御装置、38,39……比較
器。
FIG. 1 is a piping system diagram of a dry cleaner according to the present invention, FIG. 2 is a control circuit diagram, FIGS. 3A and 3B are flowcharts, and FIG. 4 is a flowchart of another embodiment. 1... Outer tank, 2... Tank, 8... Drying air path,
11...Blower fan, 12...Condenser, 13...
Heater, 15... Water separator, 31, 32... Temperature sensing element, 35... Control device, 38, 39... Comparator.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] ドラムを有する外槽に、送風フアンによる循環
型の乾燥通風路を、接続したドライクリーナに於
いて、上記乾燥通風路中に配設された溶剤の凝縮
器と、この凝縮器の下流側の乾燥通風路中に配設
され、水分離器に向う蒸溜溶剤を流通させる加熱
器と、この加熱器の入口及び出口での乾燥風の温
度を検知する感温素子と、この検知温度の差を比
較して所定温度差にて乾燥工程を終了させる制御
手段とを具備したことを特徴とするドライクリー
ナ。
In a dry cleaner, a circulation type drying air passage using a blower fan is connected to an outer tank having a drum, and a solvent condenser disposed in the drying air passage and a drying air flow downstream of this condenser are installed. Comparison of the difference in detected temperature between a heater placed in the ventilation path that circulates the distilled solvent toward the water separator, and a temperature sensing element that detects the temperature of the drying air at the inlet and outlet of this heater. and a control means for terminating the drying process at a predetermined temperature difference.
JP5488083U 1983-04-12 1983-04-12 dry cleaner Granted JPS59160099U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5488083U JPS59160099U (en) 1983-04-12 1983-04-12 dry cleaner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5488083U JPS59160099U (en) 1983-04-12 1983-04-12 dry cleaner

Publications (2)

Publication Number Publication Date
JPS59160099U JPS59160099U (en) 1984-10-26
JPS6342953Y2 true JPS6342953Y2 (en) 1988-11-09

Family

ID=30185219

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5488083U Granted JPS59160099U (en) 1983-04-12 1983-04-12 dry cleaner

Country Status (1)

Country Link
JP (1) JPS59160099U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1991016489A1 (en) * 1990-04-26 1991-10-31 Tosei Denki Kabushiki Kaisha Apparatus for drying clothes and the like and method thereof

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2680747B2 (en) * 1991-01-18 1997-11-19 三洋電機株式会社 Solvent recovery clothes dryer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1991016489A1 (en) * 1990-04-26 1991-10-31 Tosei Denki Kabushiki Kaisha Apparatus for drying clothes and the like and method thereof

Also Published As

Publication number Publication date
JPS59160099U (en) 1984-10-26

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