JPS6216677B2 - - Google Patents

Info

Publication number
JPS6216677B2
JPS6216677B2 JP56162950A JP16295081A JPS6216677B2 JP S6216677 B2 JPS6216677 B2 JP S6216677B2 JP 56162950 A JP56162950 A JP 56162950A JP 16295081 A JP16295081 A JP 16295081A JP S6216677 B2 JPS6216677 B2 JP S6216677B2
Authority
JP
Japan
Prior art keywords
solvent
heater
condenser
water
water separator
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
JP56162950A
Other languages
Japanese (ja)
Other versions
JPS5865199A (en
Inventor
Shuichi Yamanaka
Toshiaki Sakamoto
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 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

Description

【発明の詳細な説明】 (イ) 産業上の利用分野 本発明は、洗濯槽内で洗いから乾燥まで行な
い、乾燥時には、衣類中の溶剤を回収すると共
に、使用溶剤を蒸溜再生できるドライクリーナに
関する。
[Detailed Description of the Invention] (a) Field of Industrial Application The present invention relates to a dry cleaner that performs washing and drying in a washing tub, and when drying, can recover the solvent in clothes and distill and regenerate the used solvent. .

(ロ) 従来の技術 この種のドライクリーナの一例は特願昭56―
125373号(特開昭58―109096号公報)に記載され
ており、そこでは蒸溜された溶剤を乾燥通風路内
の加熱器の熱媒通路に送り、一次冷却と乾燥風の
加熱とに共用している。そして、加熱器の熱媒通
路を出た溶剤はコンデンサに導出されて冷却コイ
ルによつて冷却され、その後水分離器に導出され
ている。また、乾燥通風路内のクーラは独立して
冷却作業を実行している。
(b) Conventional technology An example of this type of dry cleaner is the patent application filed in 1983.
No. 125373 (Japanese Unexamined Patent Publication No. 109096/1983), the distilled solvent is sent to the heating medium passage of the heater in the drying ventilation passage, and is used for both primary cooling and heating of the drying air. ing. The solvent that has exited the heating medium passage of the heater is led out to a condenser, cooled by a cooling coil, and then led out to a water separator. Moreover, the cooler in the drying ventilation passage performs cooling work independently.

従つて、斯る従来例にあつては、蒸溜溶剤の冷
却のために専用のコンデンサ27を要すると共
に、このコンデンサ27とクーラ17の各々に個
別に冷却水を供給する必要があり、ドライクリー
ナとしての配管の複雑さと機構の大型化が避けら
れなかつた。
Therefore, in such a conventional example, a dedicated condenser 27 is required for cooling the distillation solvent, and cooling water must be supplied to each of the condenser 27 and the cooler 17 separately, making it difficult to use as a dry cleaner. The complexity of the piping and the enlargement of the mechanism were unavoidable.

(ハ) 発明が解決しようとする問題点 本発明は、熱媒及び冷媒の各流路を合理的に設
けることにより、配管の簡素化と機構の小型化を
図るものである。
(c) Problems to be Solved by the Invention The present invention aims to simplify piping and downsize the mechanism by rationally providing flow paths for heat medium and coolant.

(ニ) 問題点を解決するための手段 本発明による解決手段は、両端を洗濯槽に連通
し且つ送風機を装着して成る乾燥通風路内を左右
に仕切りも、この通風路内の左右に夫々凝縮器と
加熱器とを装着し、前記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
器を経て溶剤タンクに連通し、前記凝縮器の冷媒
通路の一端をウオーターチラーの流出側に接続す
ると共に、他端を水分離器内の冷却コイルを経て
溶剤タンク内の冷却コイルに連通した構成であ
る。
(d) Means for Solving the Problems The solution according to the present invention includes partitioning the inside of the drying ventilation duct, which is connected to the washing tub at both ends and equipped with a blower, to the left and right, and partitioning the inside of the drying ventilation duct, which is connected to the washing tub at both ends and equipped with a blower, to the left and right, respectively. A condenser and a heater are installed, one end of the heat medium passage of the heater is connected to a solvent distiller, the other end is connected to the solvent tank via a water separator, and the refrigerant passage of the condenser is connected to the solvent distiller. One end is connected to the outflow side of the water chiller, and the other end is connected to the cooling coil in the solvent tank via the cooling coil in the water separator.

(ホ) 作用 蒸溜溶剤を加熱器、水分離器、溶剤タンクの順
に流すのに対し、冷媒を凝縮器、水分離器の冷却
コイル、溶剤タンクの冷却コイルの順に流し、加
熱器内の溶剤を、最も低温の水が通る凝縮器で冷
却した風と熱交換させ、凝縮の効率と溶剤の冷却
効率を極めて大とする。冷媒は水分離器及び溶剤
タンクの溶剤を順次適度に冷却しており、熱媒系
と冷媒系を適合させることにより過熱、過冷却が
生じない。
(E) Function The distilled solvent flows through the heater, water separator, and solvent tank in this order, whereas the refrigerant flows through the condenser, the water separator cooling coil, and the solvent tank cooling coil in that order, and the solvent in the heater is The condenser, through which the coldest water passes, exchanges heat with the cooled air, greatly increasing condensation efficiency and solvent cooling efficiency. The refrigerant cools the water separator and the solvent in the solvent tank in order, and by matching the heating and refrigerant systems, overheating and overcooling do not occur.

(ヘ) 実施例 以下図に基いて説明すると、1は洗濯槽、2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2内の溶剤が、給液ポンプ3により一
方向弁4及び電磁弁5を通して洗濯槽1に供給さ
れる。6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5を通つて循環する。8は蒸溜器
で、仕切板9によつて蒸溜室10と加熱室11に
区画されており、この加熱室内には電気ヒータ1
2が設けられている。13は加熱室11内の圧力
を検出するための圧力スイツチである。この蒸溜
器8の使用時には前記加熱室11内に水が入れら
れ、この水を前記電気ヒータ12で加熱すること
によつて蒸気を発生し、この蒸気によつて前記仕
切板9を介して蒸溜室10内の溶剤を加熱し蒸溜
を行う。
(f) Example To explain based on the following figures, 1 is a washing tub, 2 is a solvent tank, and 3 is a liquid supply pump. and is supplied to the washing tub 1 through the solenoid valve 5. A drain pump 6 circulates the solvent in the washing tub 1 through the one-way valve 7 and the solenoid valve 5 during the washing operation. Reference numeral 8 denotes a distiller, which is divided into a distillation chamber 10 and a heating chamber 11 by a partition plate 9, and an electric heater 1 is installed in this heating chamber.
2 is provided. 13 is a pressure switch for detecting the pressure inside the heating chamber 11. When this distiller 8 is used, water is put into the heating chamber 11, and this water is heated by the electric heater 12 to generate steam, and this steam is used to distill the water through the partition plate 9. The solvent in the chamber 10 is heated and distilled.

14は両端を前記洗濯室1に連通した乾燥通風
路で、該通風路内には、フイルタ15、フロート
スイツチ16、送風機17が設けられると共に、
凝縮器18及び加熱器19が左右に仕切つて設け
られている。なお、前記した洗濯運転中は、前記
フロートスイツチ16の位置までこの乾燥通風路
14内にも溶剤が入り、このフロートスイツチ1
6によつて洗濯槽1内の溶剤液位が制御される。
又前記加熱器19は蛇行状の熱媒通路19′に多
数の板状放熱フインを嵌合した通常のラジエータ
構造を有しており、前記熱媒通路19′の一端は
バルブ20を介して前記蒸溜器8に接続し、他端
は水分離器21に接続して、この水分離器は更に
前記溶剤タンク2に接続している。一方凝縮器1
8の冷媒通路18′は、その一端をウオータチラ
ーの流出側Aに接続し、他端側は前記水分離器2
1内の冷却コイル22、及び溶剤タンク2内の冷
却コイル23を通してウオーターチラーの流入側
Bに接続している。
Reference numeral 14 denotes a drying ventilation passage whose both ends communicate with the laundry room 1, and a filter 15, a float switch 16, and a blower 17 are installed in the ventilation passage.
A condenser 18 and a heater 19 are provided partitioned into left and right sides. During the washing operation described above, the solvent enters the drying ventilation passage 14 up to the position of the float switch 16, and the float switch 1
6 controls the solvent level in the washing tub 1.
Further, the heater 19 has a normal radiator structure in which a number of plate-shaped heat dissipating fins are fitted into a meandering heat medium passage 19', and one end of the heat medium passage 19' is connected to the heat medium passage 19' through a valve 20. It is connected to the distiller 8, and the other end is connected to a water separator 21, which is further connected to the solvent tank 2. On the other hand, condenser 1
One end of the refrigerant passage 18' of No. 8 is connected to the outflow side A of the water chiller, and the other end is connected to the water separator 2.
It is connected to the inflow side B of the water chiller through a cooling coil 22 in the solvent tank 1 and a cooling coil 23 in the solvent tank 2.

24は前記凝縮器18に於て凝縮した溶剤を回
収するための溶剤回収パイプで、回収液集合槽2
5に一旦集めた後、電磁弁26を介して前記水分
離器21に流すようにしている。27,28は
夫々吸気弁と排気弁で、乾燥工程中は図の破線の
位置にあつて、乾燥通風路に設けた吸気口29と
排気口30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つて、乾燥通風路1
4を遮断すると同時に前記吸気口29と排気口3
0を開放する。31は前記送風機17を駆動する
モータである。
24 is a solvent recovery pipe for recovering the solvent condensed in the condenser 18;
After the water is once collected in the water separator 21 via the electromagnetic valve 26. Reference numerals 27 and 28 are intake valves and exhaust valves, respectively, which are located at the positions indicated by the broken lines in the figure during the drying process to close the intake port 29 and exhaust port 30 provided in the drying ventilation path, and during the deodorization process after the drying process. Switch to the solid line position and dry ventilation path 1.
4 and at the same time shut off the intake port 29 and the exhaust port 3.
Release 0. 31 is a motor that drives the blower 17.

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1内の溶剤が電磁バル
ブ32を通して蒸溜室10に入る。脱液行程中も
同様である。一方、洗い行程が終りに近ずいた時
に蒸溜器の電気ヒータ12に通電され、加熱室1
1内に蒸気を発生する。従つて、蒸溜室10内に
入つた溶剤は前記蒸気に加熱されて蒸発し、バル
ブ20を通つて加熱器19に流入する。一方この
時には送風機17が回転すると共に、ウオータチ
ラーから凝縮器18に最も低温の冷水が冷媒通路
18′により流れている。従つて、送風機17に
よつて洗濯槽1から乾燥通風路14内に吸引され
た空気は、凝縮器18を通過する時に非常に良く
冷却され、含まれている溶剤を確実に凝縮し、こ
の凝縮した溶剤は回収液集合槽25に集められ、
乾燥行程終了後電磁弁26が開いた時に水分離器
21に流れて、更に溶剤タンク2に回収される。
一方、凝縮器18を通過した空気は加熱器19を
通過する。この加熱器19の熱媒回路19′に
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19は非常な
高温になつている。従つて、前記の冷却された空
気はこの加熱器19を通過する際に加熱され、熱
風となつて前記洗濯槽1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19′を流れている溶剤
蒸気は、空気が良く冷却されている関係上この加
熱器19に於てよく放熱して凝縮し、更に水分離
器21に流入する。水分離器21に入つた溶剤
は、コイル22にて凝縮器18の水よりは高温の
冷却水によつて冷却され、且つ水を分離した後溶
剤タンク2に回収され、ここでも更により高温の
冷却水によつて適度に冷却される。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
了して蒸溜室10内の溶剤が無くなると、加熱室
11内の圧力が急上昇するので、それを圧力スイ
ツチ13が検出して乾燥行程を終える。
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 1 enters the distillation chamber 10 through the electromagnetic valve 32. The same applies during the dehydration process. On the other hand, when the washing process is nearing the end, the electric heater 12 of the distiller is energized, and the heating chamber 1
1 to generate steam. Therefore, the solvent entering the distillation chamber 10 is heated by the vapor, evaporates, and flows into the heater 19 through the valve 20. On the other hand, at this time, the blower 17 is rotating and the coldest water is flowing from the water chiller to the condenser 18 through the refrigerant passage 18'. Therefore, the air sucked into the drying air passage 14 from the washing tub 1 by the blower 17 is very well cooled when passing through the condenser 18, and the contained solvent is reliably condensed, and this condensation The solvent is collected in a collected liquid collection tank 25,
After the drying process is completed, when the solenoid valve 26 is opened, the water flows to the water separator 21 and is further collected in the solvent tank 2.
On the other hand, the air that has passed through the condenser 18 passes through the heater 19. Since the high temperature solvent vapor evaporated from the distiller 8 is flowing through the heat medium circuit 19' of the heater 19 as described above, the heater 19 is at a very high temperature. Therefore, the cooled air is heated when passing through the heater 19, and is blown into the washing tub 1 as hot air to evaporate the solvent from the clothes in the washing tub and dry the clothes. . On the other hand, since the air is well cooled, the solvent vapor flowing through the heating medium passage 19' of the heater radiates heat well in the heater 19, condenses, and further flows into the water separator 21. The solvent that has entered the water separator 21 is cooled in the coil 22 by cooling water that is higher temperature than the water in the condenser 18, and after separating the water, it is collected in the solvent tank 2, where it is also collected at a higher temperature. Cooled appropriately by cooling water. This drying process continues until the distillation is complete. That is, when the distillation is completed and the solvent in the distillation chamber 10 disappears, the pressure in the heating chamber 11 rises rapidly, and the pressure switch 13 detects this and ends the drying process.

このように乾燥が終了すると脱臭工程に入る。
脱臭工程では吸気弁27と排気弁28が図の実線
位置に切換つて吸気口29と排気口30を開き、
吸気口29から洗濯槽1内に新鮮な空気を取入
れ、更に排気口30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30より排出される。
When drying is completed in this way, a deodorizing process begins.
In the deodorizing process, the intake valve 27 and the exhaust valve 28 are switched to the solid line position shown in the figure to open the intake port 29 and the exhaust port 30.
Fresh air is taken into the washing tub 1 through an intake port 29, and is further discharged through an exhaust port 30. This results in
Even after the drying process, the solvent vapor that filled the washing tub 1 is discharged from the exhaust port 30.

(ト) 発明の効果 本発明に依れば、加熱器の熱媒に蒸溜溶剤を用
いて熱源の省略を可能とする一方、冷媒を凝縮器
から熱媒の流れに合せて水分離器、タンクの順に
流すことにより、加熱器内での溶剤の効率良い凝
縮を可能とすると共に水分離器をも冷却コンデン
サに兼用でき、過熱及び過冷却を生じさせること
が無い。かくして、冷却系統を一本化することに
より機構の小型化、配管の簡素化を達成できるも
のである。
(g) Effects of the Invention According to the present invention, it is possible to omit the heat source by using a distilled solvent as the heating medium of the heater, and at the same time, the refrigerant is transferred from the condenser to the water separator and tank in accordance with the flow of the heating medium. By flowing in this order, it is possible to efficiently condense the solvent in the heater, and the water separator can also be used as a cooling condenser, thereby preventing overheating and supercooling. Thus, by unifying the cooling system, it is possible to downsize the mechanism and simplify the piping.

【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。 1……洗濯槽、14……乾燥通風路、17……
送風機、18……凝縮器、18′……冷媒通路、
19……加熱器、19′……熱媒通路、8……蒸
溜器、21……水分離器。
The drawing is a solvent circuit diagram of the dry cleaner of the present invention. 1...Washing tub, 14...Drying ventilation path, 17...
Blower, 18... condenser, 18'... refrigerant passage,
19... Heater, 19'... Heat medium path, 8... Distiller, 21... Water separator.

Claims (1)

【特許請求の範囲】[Claims] 1 両端を洗濯槽に連通し且つ送風機を装着して
成る乾燥通風路内を左右に仕切り、この通風路内
の左右に夫々凝縮器と加熱器とを装着し、前記加
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、他端を水分離器を経て溶剤タンクに連通
し、前記凝縮器の冷媒通路の一端をウオーターチ
ラーの流出側に接続すると共に、他端を水分離器
内の冷却コイルを経て溶剤タンク内の冷却コイル
に連通したことを特徴とするドライクリーナ。
1. A drying ventilation path, which is connected to a washing tub at both ends and is equipped with a blower, is partitioned into left and right sides, and a condenser and a heater are installed on the left and right sides of this ventilation path, respectively, and the heating medium path of the heater is One end is connected to a solvent distiller, the other end is connected to a solvent tank via a water separator, one end of the refrigerant passage of the condenser is connected to the outlet side of a water chiller, and the other end is connected to a water separator. A dry cleaner characterized by communicating with a cooling coil in a solvent tank through a cooling coil in the dry cleaner.
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 JPS5865199A (en) 1983-04-18
JPS6216677B2 true 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 (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20230009898A1 (en) * 2020-07-02 2023-01-12 Colorado Extraction Systems, LLC Closed loop extraction system

Families Citing this family (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

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 (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20230009898A1 (en) * 2020-07-02 2023-01-12 Colorado Extraction Systems, LLC Closed loop extraction system

Also Published As

Publication number Publication date
JPS5865199A (en) 1983-04-18

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