JPS5865199A - Dry cleaner - Google Patents

Dry cleaner

Info

Publication number
JPS5865199A
JPS5865199A JP16295081A JP16295081A JPS5865199A JP S5865199 A JPS5865199 A JP S5865199A JP 16295081 A JP16295081 A JP 16295081A JP 16295081 A JP16295081 A JP 16295081A JP S5865199 A JPS5865199 A JP S5865199A
Authority
JP
Japan
Prior art keywords
solvent
heater
drying
washing tub
distiller
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.)
Granted
Application number
JP16295081A
Other languages
Japanese (ja)
Other versions
JPS6216677B2 (en
Inventor
修一 山中
敏昭 坂本
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
Sanyo Denki Co Ltd
Original Assignee
Sanyo Electric Co Ltd
Sanyo Denki 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, Sanyo Denki Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP16295081A priority Critical patent/JPS5865199A/en
Publication of JPS5865199A publication Critical patent/JPS5865199A/en
Publication of JPS6216677B2 publication Critical patent/JPS6216677B2/ja
Granted legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は、蒸溜器に於て蒸発した溶剤蒸気中の熱を、衣
類乾燥用の熱源として利用すると共に。
DETAILED DESCRIPTION OF THE INVENTION The present invention utilizes heat in solvent vapor evaporated in a still as a heat source for drying clothes.

前記溶剤蒸気を乾燥通風路内を流れる空気によって凝縮
せんとするものである。
The solvent vapor is condensed by the air flowing through the drying ventilation path.

従来のドライクリーナは、乾燥通風路内に設けられてい
る加熱器が電気ヒータあるいはスチームヒータであり、
電気ヒータであれば消費電力が増大し、スチームヒータ
であれはボイラを必要とする。又蒸榴器から蒸発した溶
剤蒸気を凝縮するために特別のクーラを必要とする。
In conventional dry cleaners, the heater installed in the drying ventilation path is an electric heater or a steam heater.
Electric heaters increase power consumption, and steam heaters require a boiler. It also requires a special cooler to condense the solvent vapors evaporated from the steamer.

本発明は、乾燥通風路内に設けた加熱器の熱媒通路の一
端を溶剤の蒸溜器に接続すると共に、他端を水分離器K
li続すbことによシ、蒸溜器で蒸発した溶剤蒸気が加
熱器内を通る時に放出する熱マ衣類の乾燥を行うと共に
%放熱によ〉接剤蒸気を凝縮させ、これを水分離器を通
して回収せんとするもので、衣類乾燥用に電気ヒータや
がイラを使用する必要がなく、溶剤蒸気を凝縮するのに
別違のクーラを設ける必要がなくなシ、たとえ必要とし
ても小容量のものですむのである。
In the present invention, one end of the heating medium passage of the heater provided in the drying ventilation passage is connected to a solvent distiller, and the other end is connected to a water separator K.
Particularly, when the solvent vapor evaporated in the distiller passes through the heater, the heat emitted is used to dry the clothes and condense the adhesive vapor, which is then transferred to the water separator. This system eliminates the need for electric heaters and ovens for drying clothes, eliminates the need for separate coolers to condense solvent vapors, and even if necessary, only a small capacity It's all you need.

以下図に基いて説明すると、(1)は洗濯槽、(!)は
溶剤タンク、(3)は給液ポンプで、洗濯開始時には溶
剤タンク11+内の溶剤が、給液ボ/プ(3)により 
一方向弁(4)尊び電磁弁+61 今通して洗濯槽(1
)に供給される。16)はドレンポンプで、洗濯運転中
はこのドレンポンプにより、洗濯槽(1)内の溶剤が一
方向弁(7)及び電磁弁+6>を通って循環する。(m
lは蒸溜器で、仕切板(9)によって蒸溜室(1(至)
と加熱室(U)に区画されており、この加熱器内には電
気ヒータ(1!+が設けられている。崗は加熱室1ll
l内の圧力を検出するための圧力スイッチである。との
蒸溜器talの使用時には前記加熱室(Ill内に水が
入れられ、この水を前記電気ヒータθ乃で加熱すること
によって蒸気を発生し、この蒸気によって前記仕切板棒
jを介して蒸溜器(101内の溶剤を加熱し蒸溜を行う
To explain based on the diagram below, (1) is the washing tub, (!) is the solvent tank, and (3) is the liquid supply pump. by
One-way valve (4) Solenoid valve +61 Washing tub (1)
). 16) is a drain pump, and during washing operation, this drain pump circulates the solvent in the washing tub (1) through the one-way valve (7) and the solenoid valve +6>. (m
1 is a distiller, and the distillation chamber (1) is separated by a partition plate (9).
It is divided into a heating chamber (U) and an electric heater (1!+) is installed in this heater.
This is a pressure switch for detecting the pressure inside the tank. When using the distiller tal, water is put into the heating chamber (Ill), and this water is heated by the electric heater θ to generate steam, and this steam is used to distill the water through the partition plate rod j. The solvent in the vessel (101) is heated and distilled.

04)は両端を前記洗濯室fllに連通した乾燥通風路
で、該通風路内には、フィルタ賎・フロートスイッチ(
11・送風機(Iη・凝縮gias及び加熱嘉慴が設け
られている。なお前記した洗濯運転中は、前A11ノロ
ートスイツチθ―の位置までこの乾燥通風路an内にも
溶剤が入り、このフロートスイッチ11ψによって洗濯
槽111内の溶剤液位が制御される。又前記加熱器(l
Sは蛇行状の熱媒通路(i−に多数の板状放熱7チラー
の流出側(優に接続し、他端側は前記水分離器!21+
内の冷却コイル(四、及び溶剤タンク+21内の冷却コ
イル(割を通してウォーターチラーの流入11411 
(B)に接続している。
04) is a drying ventilation passage whose both ends communicate with the laundry room full, and inside the ventilation passage there is a filter tube/float switch (
11. A blower (Iη) is provided with a condensing dias and a heating device. During the above-mentioned washing operation, the solvent also enters this drying ventilation passage an up to the position of the front A11 noroto switch θ-, and this float The solvent level in the washing tub 111 is controlled by the switch 11ψ.
S is a meandering heat medium path (i- is connected to the outflow side of a large number of plate-shaped heat dissipation 7 chillers, and the other end is connected to the water separator!21+
cooling coil (4), and cooling coil (4) in the solvent tank + 21 (inflow of the water chiller through the
(B) is connected.

囚)は前記凝縮器(l19に於て凝縮した溶剤を回収す
る九めの溶剤回収パイプで、回収液集合槽□□□に一旦
集めた後、電磁弁−を介して前記水分離器い)に流すよ
うにしている。鰭(ハ)は夫々吸気弁と排気弁で、乾燥
行程中は図0破線の位置にあって、乾燥通風路に設けた
吸気口器と排気口−を閉じると共に、乾燥行程後の脱臭
行程時には図の実線位置に切換って、乾燥通風路(14
を速断すると同時に前記吸気口器と排気口−を開放する
。C11lは前記送風機・ηを駆動するモータである。
The condenser (l19) is the ninth solvent recovery pipe that recovers the condensed solvent, and once it is collected in the collected liquid collecting tank □□□, it is transferred to the water separator via the solenoid valve. I try to let it flow. The fins (C) are an intake valve and an exhaust valve, respectively, and are located at the position indicated by the broken line in Figure 0 during the drying process, closing the intake port and exhaust port provided in the drying ventilation path, and during the deodorization process after the drying process. Switch to the solid line position in the figure, and then move the drying ventilation path (14
At the same time, the intake port device and the exhaust port are opened. C11l is a motor that drives the blower η.

以上の構成に於て、洗い行程及び脱液行程が終了すると
、乾燥行程に入ると同時に溶剤の蒸溜が行われる。即ち
洗い行程が終了すると、ドレンポンプ(6)が回転して
、洗濯槽ill内の溶剤が電磁パルプ(至)を通して蒸
溜11:瑚に入る。脱赦行程中4同一である。一方洗い
行程がJI6に近すいた時に蒸溜器の電気ヒータ轢に通
電され、加熱室間内に蒸気を発生する。従って蒸置皇叫
内に入った溶剤は前記蒸気に加熱されて蒸発し、パルプ
翰を通って加熱器(I@に流入する。一方この時には送
風機αηが回転すると共に、クォータチラーから凝縮器
(I縛に冷水が流れている。従って送風機aηによって
洗濯槽eelから乾燥通風路04内に吸引された空気は
、凝縮器O8を通過する時にこの空気に含まれている溶
剤を凝縮し、この凝縮した溶剤は回収液集合槽−に集め
られ、乾燥行程終了後電磁弁−が開いた時に水分離器2
1)に流れて、更に溶剤タンク(!)VC回収される。
In the above configuration, when the washing process and the deliquid process are completed, the solvent is distilled at the same time as the drying process begins. That is, when the washing process is completed, the drain pump (6) rotates, and the solvent in the washing tub (ill) enters the distillation tank (11) through the electromagnetic pulp. 4 are the same during the forgiveness process. On the other hand, when the washing process approaches JI6, the electric heater track of the distiller is energized and steam is generated in the heating chamber. Therefore, the solvent that has entered the steam chamber is heated by the steam, evaporates, and flows into the heater (I@) through the pulp screen.Meanwhile, at this time, the blower αη rotates, and the condenser ( Cold water is flowing through the air pipe I.Therefore, when the air sucked into the drying ventilation passage 04 from the washing tub eel by the blower aη passes through the condenser O8, it condenses the solvent contained in this air. The solvent is collected in the collected liquid collection tank, and when the solenoid valve is opened after the drying process, the water separator 2
1) and is further collected in a solvent tank (!) VC.

一方凝縮器o1を通過した空気は加熱6帽を通過する。On the other hand, the air that has passed through the condenser o1 passes through the heating cap.

この加熱器軸の熱媒回路alKは、前述の如く蒸溜器(
8)から蒸発した高温の溶剤蒸気が流れているので、こ
の加熱器軸は高温になっている。
The heating medium circuit alK of this heater shaft is connected to the distiller (
Since the high temperature solvent vapor evaporated from 8) is flowing, this heater shaft is at a high temperature.

従って前記空気はこの加熱6舖を通過する際に加熱され
、熱風となって前記洗濯槽illに吹出てこの洗濯槽内
の衣類から溶剤を蒸発させ、衣類の乾燥を行う。一方前
記加熱器の熱媒通路(−を流れている溶剤蒸気は、この
加熱器−に於て放熱することによって凝縮し、更に水分
離器シllに流入する。水分離器シυに入った溶剤は、
コイル固によって更ンc冷却され、且つ水を分離した後
溶剤タンクfi+に回収される。この乾燥行程は蒸溜が
完了するまで継続する。即ち蒸溜が完了して蒸溜器(1
内の溶剤が無くなると、加熱器用)内の圧力が、急上昇
するので、それを圧力スイッチ+14が検出し−C乾燥
行程を終える。
Therefore, the air is heated as it passes through the heating tube 6, and is blown into the washing tub as hot air to evaporate the solvent from the clothes in the washing tub and dry the clothes. On the other hand, the solvent vapor flowing through the heating medium path (-) of the heater is condensed by dissipating heat in this heater, and further flows into the water separator sill. The solvent is
After being further cooled by a coil and separating water, it is collected in a solvent tank fi+. This drying process continues until the distillation is complete. That is, the distillation is completed and the distiller (1
When the solvent in the heater runs out, the pressure in the heater rises rapidly, which is detected by the pressure switch +14 and the -C drying process ends.

このように乾燥が終了すると脱臭行程に入る。Once drying is completed, the deodorizing process begins.

脱臭行程では吸気弁シフ;と排気弁−が図の実線位置に
切換って吸気口器と排気口(関1を開き、吸気口器から
洗濯槽11)内に新鮮な空気をル4入れ、更に排気口(
晴より排出する。これにより、乾燥行程後も洗濯槽(1
)内に充満していた溶剤蒸気(は排気口倒より排出され
る。
In the deodorizing process, the intake valve shift and the exhaust valve - are switched to the solid line position shown in the figure, and fresh air is introduced into the intake port device and the exhaust port (Section 1 is opened, and from the intake device to the washing tub 11). Furthermore, the exhaust port (
Discharge from the sun. As a result, even after the drying process, the washing tub (1
The solvent vapor that was filling the inside of the tank () is discharged from the exhaust port.

以上の如く本発明は、乾燥通1截路に設けた加熱器内に
蒸溜器から蒸発した溶剤蒸気を通し、該溶剤蒸気の熱を
利用して衣類を乾燥するようにしているので、別違に衣
類乾燥用の熱源を必要とせず、又必要としても小容瀘の
ものでよい。更に前記加熱器の表面を流れる空気は凝縮
器によって冷却されているので、この加熱器内の浴剤蒸
気は熱を奪われて速やかに凝縮する。従つ−C蒸溜器か
ら蒸発した溶剤蒸気を凝縮するのに特別のクーラを必要
とせず、又必訣としても小容値のもので済み、経剛的な
ドライクリーナを提供することができる。
As described above, in the present invention, the solvent vapor evaporated from the distiller is passed through the heater provided in one drying passage, and the heat of the solvent vapor is used to dry the clothes. There is no need for a heat source for drying clothes, and even if one is needed, one with a small capacity can be used. Furthermore, since the air flowing over the surface of the heater is cooled by the condenser, the bath agent vapor within the heater is deprived of heat and quickly condenses. Therefore, a special cooler is not required for condensing the solvent vapor evaporated from the -C distiller, and even if only one with a small volume is necessary, it is possible to provide a rigid dry cleaner.

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

図面は本発明ドライクリーナの溶剤回路図である0 (1)・・・洗濯槽、I・・・乾燥通風路、同・・・送
風機、−・・・凝縮器、舖・・・加熱器、四・・・熱媒
通路、(8)・・・蒸滴器、しl)・・・水分離器。
The drawing is a solvent circuit diagram of the dry cleaner of the present invention. 4... Heat medium passage, (8)... Steam dropper, (l)... Water separator.

Claims (1)

【特許請求の範囲】[Claims] (1)両端を洗濯槽に連通した乾燥通風路内に、送風機
と凝縮器とツノ1】熱器とに装着し、この加熱器の熱媒
通路の一暮を溶剤の蒸溜器に接続すると共に、他端を水
分離器に接続してなるドライクリーナ。
(1) Install a blower, a condenser, and a horn heater in a drying ventilation passage that communicates with the washing tub at both ends, and connect the heating medium passage of this heater to a solvent distiller. , a dry cleaner whose other end is connected to a water separator.
JP16295081A 1981-10-12 1981-10-12 Dry cleaner Granted JPS5865199A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16295081A JPS5865199A (en) 1981-10-12 1981-10-12 Dry cleaner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16295081A JPS5865199A (en) 1981-10-12 1981-10-12 Dry cleaner

Publications (2)

Publication Number Publication Date
JPS5865199A true JPS5865199A (en) 1983-04-18
JPS6216677B2 JPS6216677B2 (en) 1987-04-14

Family

ID=15764338

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16295081A Granted JPS5865199A (en) 1981-10-12 1981-10-12 Dry cleaner

Country Status (1)

Country Link
JP (1) JPS5865199A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5869595A (en) * 1981-10-20 1983-04-25 三洋電機株式会社 Dry cleaner
JPS58109491U (en) * 1982-01-20 1983-07-26 三洋電機株式会社 dry cleaner
JPS58127697A (en) * 1982-01-26 1983-07-29 三洋電機株式会社 Dry cleaner
JPH0290789U (en) * 1989-09-21 1990-07-18

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11504644B2 (en) * 2020-07-02 2022-11-22 Colorado Extraction Systems, LLC Closed loop extraction system

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58109096A (en) * 1981-08-12 1983-06-29 三菱重工業株式会社 Dry cleaning apparatus

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58109096A (en) * 1981-08-12 1983-06-29 三菱重工業株式会社 Dry cleaning apparatus

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5869595A (en) * 1981-10-20 1983-04-25 三洋電機株式会社 Dry cleaner
JPS6340118B2 (en) * 1981-10-20 1988-08-09 Sanyo Electric Co
JPS58109491U (en) * 1982-01-20 1983-07-26 三洋電機株式会社 dry cleaner
JPS6329517Y2 (en) * 1982-01-20 1988-08-08
JPS58127697A (en) * 1982-01-26 1983-07-29 三洋電機株式会社 Dry cleaner
JPH0290789U (en) * 1989-09-21 1990-07-18

Also Published As

Publication number Publication date
JPS6216677B2 (en) 1987-04-14

Similar Documents

Publication Publication Date Title
TW555951B (en) Liquid desiccant dehumidifier and air conditioner
US3032887A (en) Clothes drier
JPS62500436A (en) drying equipment
CN106733871A (en) A kind of energy saving recovery method of agent for carbon hydrogen detergent and a kind of hydrocarbon cleaning equipment
JPS5865199A (en) Dry cleaner
JPS6340118B2 (en)
JPH04281178A (en) Vacuum drying treatment device
JPS6329517Y2 (en)
JPS5897398A (en) Dry cleaning machine
JPS601778Y2 (en) filtration device
JPS6353845B2 (en)
JPS6321289Y2 (en)
US3738127A (en) Dry cleaning recovery unit
JPS6342954Y2 (en)
JPS6239837Y2 (en)
JPS5844097A (en) Dry cleaning apparatus
JPS6321291Y2 (en)
JPS629921Y2 (en)
JPS6279098A (en) Dry cleaner
JPS5869596A (en) Dry cleaner
JPS58127697A (en) Dry cleaner
JP3728295B2 (en) Absorption refrigerator with improved thermal efficiency
TR202006623A1 (en) A device containing a water collection unit.
JP3082787B2 (en) Dry cleaning machine
JPS60236695A (en) Drycleaner