JPS6329517Y2 - - Google Patents

Info

Publication number
JPS6329517Y2
JPS6329517Y2 JP1982006558U JP655882U JPS6329517Y2 JP S6329517 Y2 JPS6329517 Y2 JP S6329517Y2 JP 1982006558 U JP1982006558 U JP 1982006558U JP 655882 U JP655882 U JP 655882U JP S6329517 Y2 JPS6329517 Y2 JP S6329517Y2
Authority
JP
Japan
Prior art keywords
solvent
heater
distiller
distillation
drying
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
JP1982006558U
Other languages
Japanese (ja)
Other versions
JPS58109491U (en
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 filed Critical
Priority to JP655882U priority Critical patent/JPS58109491U/en
Publication of JPS58109491U publication Critical patent/JPS58109491U/en
Application granted granted Critical
Publication of JPS6329517Y2 publication Critical patent/JPS6329517Y2/ja
Granted legal-status Critical Current

Links

Description

【考案の詳細な説明】 本案は、溶剤の蒸溜性能を向上したドライクリ
ーナに関する。
[Detailed Description of the Invention] The present invention relates to a dry cleaner with improved solvent distillation performance.

ドライクリーナの溶剤は繰返して使用される為
に、汚れた時には蒸溜器で再生し、再び使用して
いる。しかるに蒸溜も終期に近づいて蒸溜器内の
溶剤がほとんど蒸溜されると、蒸溜器内は飽和蒸
気圧になり、残つた少量の溶剤ガス、及び残滓中
に含まれている溶剤はなかなか蒸溜器から出てい
かず、蒸溜時間が長くかかると共に、蒸溜後残滓
を取出す時に溶剤蒸気が作業場に漏れ出ることが
多かつた。
The solvent in dry cleaners is used repeatedly, so when it becomes dirty, it is recycled in a distiller and used again. However, when distillation approaches the end and most of the solvent in the still is distilled, the inside of the still reaches saturated vapor pressure, and the remaining small amount of solvent gas and the solvent contained in the residue are difficult to remove from the still. The distillation time was long, and solvent vapor often leaked into the workplace when removing the residue after distillation.

本案は洗濯物乾燥用の乾燥通風路と蒸溜器間を
通風管で接続することにより、蒸溜器内に空気を
流し込んで溶剤ガスを押出すと共に、蒸溜器の底
に残つた残滓中に含まれている僅かな溶剤でもそ
の蒸発を促進させ、蒸溜性能を向上したものであ
る。
This method connects the drying air passage for laundry drying and the distiller with a ventilation pipe, allowing air to flow into the distiller and pushing out the solvent gas, while also removing the solvent gas contained in the residue remaining at the bottom of the distiller. Even with a small amount of solvent present, the evaporation is accelerated and the distillation performance is improved.

以下実施例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は溶剤通路7中に設けたドレンポン
プで、洗濯運転中はこのドレンポンプにより、洗
濯槽1内の溶剤を一方向弁8及び電磁弁5を通し
て循環せしめる。
To explain based on the following examples, 1 is a washing tub;
2 is a solvent tank, and 3 is a liquid supply pump. When washing starts, the liquid supply pump 3 supplies the solvent in the solvent tank 2 to the washing tub 1 through a one-way valve 4 and a solenoid valve 5. Reference numeral 6 denotes a drain pump provided in the solvent passage 7. During the washing operation, the drain pump circulates the solvent in the washing tub 1 through the one-way valve 8 and the solenoid valve 5.

9は両端を前記洗濯槽1に接続した乾燥通風路
で、該通風路内には、フイルタ10、フロートス
イツチ11、送風機12、凝縮器13及び加熱器
14が設けられている。なお前記した洗濯運転中
は、前記フロートスイツチ11の位置までこの乾
燥通風路9内にも溶剤が入り、このフロートスイ
ツチ11によつて洗濯槽1内の溶剤液位が制御さ
れる。前記加熱器14は蛇行状をしており、その
一端を後述する蒸溜器15に接続すると共に、他
端は水分離器16に接続し、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
3を蛇行状をしており、その一端はウオータチラ
ーの流出側Aに接続すると共に、他端は前記水分
離器16内の冷却コイル17及び溶剤タンク2内
の冷却コイル18を通してウオーターチラーの流
入側Bに接続している。19は前記凝縮器13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20に一旦集めた後、電磁弁
21を介して前記水分離器16に流すようにして
いる。22,23は夫々吸気弁と排気弁で、乾燥
行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24と排気口25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9を遮断すると同時に前記吸気
口24と排気口25を開放する。26は前記送風
機12を駆動するモータである。
Reference numeral 9 denotes a drying ventilation passage whose both ends are connected to the washing tub 1, and a filter 10, a float switch 11, a blower 12, a condenser 13, and a heater 14 are provided in the ventilation passage. During the above-mentioned washing operation, the solvent enters the drying ventilation passage 9 up to the position of the float switch 11, and the solvent level in the washing tub 1 is controlled by the float switch 11. The heater 14 has a meandering shape, and one end thereof is connected to a distiller 15, which will be described later, and the other end is connected to a water separator 16, which is further connected to the solvent tank 2. There is. On the other hand, condenser 1
3 has a meandering shape, one end of which connects to the outflow side A of the water chiller, and the other end of which connects the inflow of the water chiller through the cooling coil 17 in the water separator 16 and the cooling coil 18 in the solvent tank 2. Connected to side B. Reference numeral 19 denotes a solvent recovery pipe for recovering the solvent condensed in the condenser 13, which once collects the solvent in the collected liquid collecting tank 20 and then flows it to the water separator 16 via the electromagnetic valve 21. . Reference numerals 22 and 23 are an intake valve and an exhaust valve, respectively, which are located at the positions indicated by the broken lines in the figure during the drying process, and close the intake port 24 and exhaust port 25 provided in the drying ventilation path.
During the deodorizing process after the drying process, the position is switched to the solid line position shown in the figure, and the drying air passage 9 is shut off, while at the same time the intake port 24 and the exhaust port 25 are opened. 26 is a motor that drives the blower 12.

而して前記蒸溜器15は、蒸発した溶剤蒸気の
流出口27を前記加熱器14に接続すると共に、
溶剤液の流入口28は電磁弁29を介して前記溶
剤通路7に接続し、更に逆止弁30を有する通風
管31によつて前記乾燥通風路9とも送風機12
の風下側に於て接続している。又この蒸溜器15
内は仕切板32を介して蒸溜室33と加熱室34
に区画されており、この加熱室内には電気ヒータ
35が設けられていてこのヒータで加熱室内の水
を加熱し、その蒸気で蒸溜室33内の溶剤を加熱
するようにしている。36は加熱室34内の圧力
を検出する為の圧力スイツチである。以上の構成
に於て、洗い行程及び脱液工程が終了すると、乾
燥工程に入ると同時に溶剤の蒸溜が行われる。即
ち洗い工程が終了すると、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29を通し
て蒸溜室33に入る。脱液工程中も同様である。
一方脱液工程の終了までに蒸溜器の電気ヒータ3
5には通電され、加熱室34内に蒸気を発生す
る。従つて蒸溜室33内に入つた溶剤は前記蒸気
に加熱されて蒸発し、溶剤蒸気の流出口27を通
つて加熱器14に流入する。一方この時には送風
機12が回転すると共に、ウオータチラーから凝
縮器13に冷水が流れている。従つて送風機12
によつて洗濯槽1から乾燥通風路9内に吸引され
た空気は、凝縮器13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20に集められ、乾燥行程終了後電
磁弁21が開いた時に水分離器16に流れて、更
に溶剤タンク2に回収される。一方凝縮器13を
通過した空気は加熱器14を通過する。この加熱
器14には、前述の如く蒸溜器15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1
4は高温になつている。従つて前記空気はこの加
熱器14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
器を流れている溶剤蒸気は、この加熱器14に於
て放熱することによつて凝縮し、更に水分離器1
6に流入する。水分離器16に入つた溶剤は、コ
イル17によつて更に冷却され、且つ水を分離し
た後溶剤タンク2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
て蒸溜室33内の溶剤が無くなると加熱室34内
の圧力が急上昇するので、それを圧力スイツチ3
6が検出して乾燥行程及び蒸溜を終える。
The distiller 15 connects the outlet 27 of the evaporated solvent vapor to the heater 14, and
The solvent inlet 28 is connected to the solvent passage 7 via a solenoid valve 29, and is connected to the drying ventilation passage 9 and the blower 12 by a ventilation pipe 31 having a check valve 30.
It is connected on the leeward side of the Also, this distiller 15
Inside is a distillation chamber 33 and a heating chamber 34 via a partition plate 32
This heating chamber is provided with an electric heater 35, which heats the water in the heating chamber, and uses the steam to heat the solvent in the distillation chamber 33. 36 is a pressure switch for detecting the pressure inside the heating chamber 34. In the above configuration, when the washing process and the deliquifying 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 33 through the electromagnetic valve 29. The same applies during the deliquoring process.
On the other hand, the electric heater 3 of the distiller is
5 is energized and generates steam in the heating chamber 34. Therefore, the solvent that has entered the distillation chamber 33 is heated by the vapor, evaporates, and flows into the heater 14 through the solvent vapor outlet 27. Meanwhile, at this time, the blower 12 is rotating and cold water is flowing from the water chiller to the condenser 13. Therefore, the blower 12
The air sucked into the drying air passage 9 from the washing tub 1 by the above condenses the solvent contained in the air when passing through the condenser 13, and this condensed solvent is collected in the collected liquid collecting tank 20. When the solenoid valve 21 is opened after the drying process is completed, the water flows to the water separator 16 and is further collected in the solvent tank 2. On the other hand, the air that has passed through the condenser 13 passes through the heater 14 . As described above, the high temperature solvent vapor evaporated from the distiller 15 is flowing through the heater 14.
4 is getting hot. Therefore, the air is heated when passing through the heater 14, 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, the solvent vapor flowing through the heater is condensed by dissipating heat in the heater 14, and is further condensed in the water separator 1.
6. The solvent that has entered the water separator 16 is further cooled by a coil 17 and is recovered into the solvent tank 2 after separating water. This drying process continues until the distillation is complete. That is, when the distillation is completed and the solvent in the distillation chamber 33 disappears, the pressure in the heating chamber 34 rises rapidly, so the pressure switch 3
6 is detected and the drying process and distillation are completed.

しかるに乾燥行程の終了時近くには、蒸溜室3
3内に多量の残滓が堆積し、この残滓中に含まれ
ている溶剤は完全に蒸発しにくい。そころが本案
では、循環通風路9内を流れている空気流の一部
が通風管31を通つて蒸溜室33内に吹込んでお
り、この風によつて残滓中に残つている溶剤の蒸
発を促進すると共にこの蒸溜室33内に充満して
いる溶剤ガスを流出口27より押出してしまうの
で、蒸溜は短時間で終了する。なお前記通風管3
1内には、洗濯槽1内の衣類から蒸発した溶剤も
流れるが、これは蒸溜器の溶剤蒸気流出口27か
ら加熱器14側に流出して凝縮されるので問題は
ない。
However, near the end of the drying process, distillation chamber 3
A large amount of residue is deposited in the 3, and the solvent contained in this residue is difficult to completely evaporate. In this case, a part of the air flow flowing through the circulation ventilation passage 9 is blown into the distillation chamber 33 through the ventilation pipe 31, and this air evaporates the solvent remaining in the residue. Since the solvent gas filling the distillation chamber 33 is pushed out from the outlet 27, the distillation is completed in a short time. Note that the ventilation pipe 3
The solvent evaporated from the clothes in the washing tub 1 also flows into the washing tub 1, but this is not a problem because it flows out from the solvent vapor outlet 27 of the distiller to the heater 14 side and is condensed.

なお通風管31内に介在した逆止弁30を省略
すると共に、この通風管の一端を熱風循環通風路
の送風機12よりも風上側に接続すると、蒸溜室
33内の溶剤ガスの多くはこの通風管31を通し
て吸い出されるので、この場合にも蒸溜を促進す
ることができるが、前記加熱器14内に溶剤蒸気
があまり流れなくなるので加熱器14の発熱量が
減少し、洗濯物の乾燥効率を低下する。従つて本
実施例の場合には通風管31を送風機12よりも
風上側に接続することは出来ないが、多くのドラ
イクリーナに於けるように、加熱器14内に別途
設けた温水ボイラで発生した蒸気を通したり、こ
の加熱器を電気ヒータにした場合には、通風管3
1を送風機17よりも風上側に接続することがで
きる。
Note that if the check valve 30 interposed in the ventilation pipe 31 is omitted and one end of this ventilation pipe is connected to the upwind side of the blower 12 in the hot air circulation ventilation path, most of the solvent gas in the distillation chamber 33 will be absorbed by this ventilation. Since the solvent vapor is sucked out through the pipe 31, distillation can be promoted in this case as well, but since less solvent vapor flows into the heater 14, the amount of heat generated by the heater 14 is reduced, and the laundry drying efficiency is reduced. descend. Therefore, in the case of this embodiment, the ventilation pipe 31 cannot be connected to the windward side of the blower 12, but as in many dry cleaners, the hot water boiler installed separately in the heater 14 may If the heater is an electric heater, the ventilation pipe 3
1 can be connected to the windward side of the blower 17.

以上の如く本案は、蒸溜器と熱風循環通風路間
を通風管で接続しているので、この通風管を通し
て蒸溜器内に空気が流入又は流出し、蒸溜器内に
充満している溶剤蒸気をこの蒸溜器から迅速に追
出すと共に、残滓中に残つている溶剤の蒸発を促
進するので、蒸溜は短時間のうちに完全に行わ
れ、又蒸溜完了後残滓をかき出すために蒸溜器の
ドアを開いても作業場に漏れ出る溶剤蒸気は皆無
に近くなり、その効果は大である。
As described above, in this case, the distiller and the hot air circulation air passage are connected by a ventilation pipe, so air flows into or out of the distiller through this ventilation pipe, and the solvent vapor filling the distiller is removed. This allows for quick ejection of the residue from the still and promotes the evaporation of the solvent remaining in the residue, so that distillation is completed in a short period of time. Even when opened, almost no solvent vapor leaks into the workplace, which is very effective.

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

図面は本案ドライクリーナの溶剤回路図であ
る。 9……乾燥通風路、15……蒸溜器、31……
通風管、12……送風機、14……加熱器。
The drawing is a solvent circuit diagram of the dry cleaner of the present invention. 9... Drying ventilation channel, 15... Distiller, 31...
Ventilation pipe, 12...Blower, 14...Heater.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 加熱器、凝縮器及び送風機を有し、両端を洗濯
槽に接続した乾燥通風路と、汚れた溶剤を加熱蒸
溜し、溶剤蒸気を前記加熱器に熱媒として供給す
る蒸溜器とを備え、前記送風機よりも風下側の乾
燥通風路と前記蒸溜器とを独立した通風管で接続
したことを特徴とするドライクリーナ。
A drying ventilation passage having a heater, a condenser, and a blower and connected to a washing tub at both ends, and a distiller that heats and distills the dirty solvent and supplies solvent vapor to the heater as a heat medium, A dry cleaner characterized in that a drying ventilation passage on the leeward side of the blower and the distiller are connected by an independent ventilation pipe.
JP655882U 1982-01-20 1982-01-20 dry cleaner Granted JPS58109491U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP655882U JPS58109491U (en) 1982-01-20 1982-01-20 dry cleaner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP655882U JPS58109491U (en) 1982-01-20 1982-01-20 dry cleaner

Publications (2)

Publication Number Publication Date
JPS58109491U JPS58109491U (en) 1983-07-26
JPS6329517Y2 true JPS6329517Y2 (en) 1988-08-08

Family

ID=30019346

Family Applications (1)

Application Number Title Priority Date Filing Date
JP655882U Granted JPS58109491U (en) 1982-01-20 1982-01-20 dry cleaner

Country Status (1)

Country Link
JP (1) JPS58109491U (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5865199A (en) * 1981-10-12 1983-04-18 三洋電機株式会社 Dry cleaner

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5865199A (en) * 1981-10-12 1983-04-18 三洋電機株式会社 Dry cleaner

Also Published As

Publication number Publication date
JPS58109491U (en) 1983-07-26

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