JPS6157798B2 - - Google Patents
Info
- Publication number
- JPS6157798B2 JPS6157798B2 JP16845881A JP16845881A JPS6157798B2 JP S6157798 B2 JPS6157798 B2 JP S6157798B2 JP 16845881 A JP16845881 A JP 16845881A JP 16845881 A JP16845881 A JP 16845881A JP S6157798 B2 JPS6157798 B2 JP S6157798B2
- Authority
- JP
- Japan
- Prior art keywords
- solvent
- air
- distiller
- cooler
- ejector
- 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
Links
- 238000001035 drying Methods 0.000 claims description 22
- 238000004821 distillation Methods 0.000 claims description 17
- 238000009423 ventilation Methods 0.000 claims description 14
- 238000005406 washing Methods 0.000 claims description 8
- 239000002904 solvent Substances 0.000 description 40
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000000203 mixture Substances 0.000 description 2
- 239000005909 Kieselgur Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
Description
【発明の詳細な説明】
本発明は、蒸溜器内を減圧することによつて蒸
溜を完全に行なうように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 that completely carries out distillation by reducing the pressure inside the still.
溶剤の回収効果を上げるために、蒸溜時に蒸溜
器内を減圧する考えは特公昭50―16589号に既に
示されている。しかしながら蒸溜器内を減圧する
ために、蒸溜器と凝縮器との間に真空ポンプを接
続すると、凝縮器内に多量の空気が入り込んで溶
剤を凝縮する能力が低下してしまう。そこで前記
公報では、蒸溜器内を真空ポンプで減圧した後、
この真空ポンプの入口と出口側を遮断し、この真
空ポンプを側路して蒸溜器から蒸発した溶剤蒸気
を凝縮器に案内するようにしている。従つて蒸溜
運転を長時間連続して行なうと、蒸溜器内の圧力
が高くなり、所期の目的を達成することができな
い。 In order to increase the effectiveness of solvent recovery, the idea of reducing the pressure inside the distiller during distillation was already presented in Japanese Patent Publication No. 16589/1983. However, when a vacuum pump is connected between the distiller and the condenser in order to reduce the pressure inside the distiller, a large amount of air enters the condenser, reducing the ability to condense the solvent. Therefore, in the above publication, after reducing the pressure inside the distiller with a vacuum pump,
The inlet and outlet sides of this vacuum pump are shut off, and the vacuum pump is bypassed so that the solvent vapor evaporated from the distiller is guided to the condenser. Therefore, if the distillation operation is continued for a long time, the pressure inside the still will increase, making it impossible to achieve the desired purpose.
そこで本発明は、両端を洗濯槽に接続した乾燥
通風路に空気パイプを接続して、該パイプの途中
にエゼクタを介挿し、一端を蒸溜器に接続した蒸
溜パイプの他端側をこのエゼクタの低圧部分に接
続することにより、蒸溜運転中も連続して蒸溜器
内を低圧に保つて蒸溜効果を上げると共に、洗濯
物乾燥用のクーラによつて前記蒸溜器から蒸発し
た溶剤を凝縮して回収することにより、溶剤蒸気
の凝縮効果をも向上することを目的としている。 Therefore, in the present invention, an air pipe is connected to a drying ventilation passage whose both ends are connected to a washing tub, an ejector is inserted in the middle of the pipe, and one end of the distillation pipe is connected to a distiller, and the other end of the distillation pipe is connected to the ejector. By connecting to the low-pressure part, the inside of the distiller is continuously maintained at a low pressure during distillation operation to increase the distillation effect, and the solvent evaporated from the distiller is condensed and recovered by a cooler for drying laundry. By doing so, the purpose is to also improve the condensation effect of solvent vapor.
即ち、蒸溜器に一端を接続した蒸溜パイプの他
端側をエゼクタの低圧部に接続して蒸溜運転中も
蒸溜器内を減圧すると共に、エゼクタに吸込まれ
た溶剤を洗濯物乾燥用の乾燥通風路に吹込んで、
該通風路内のクーラで前記溶剤を凝縮することに
より、前記溶剤中に多量の空気を含んでいても凝
縮効率を低下することのないようにしている。 That is, one end of the distillation pipe is connected to the distiller, and the other end is connected to the low-pressure part of the ejector to reduce the pressure inside the distiller during distillation operation, and at the same time, the solvent sucked into the ejector is used as a drying ventilation for drying laundry. blow into the road,
By condensing the solvent in the cooler in the ventilation passage, even if the solvent contains a large amount of air, the condensation efficiency is not reduced.
以下実施例に基いて説明すると、1は溶剤タン
ク、2は循環ポンプ、3はフイルタ、4は洗濯槽
で、洗濯行程時は前記循環ポンプによつてこれら
各部分を通して溶剤を循環している。5は両端を
洗濯槽に接続した乾燥通風路で、その内部にリン
トフイルタ6と送風機7とクーラ8及びヒータ9
を設けると共に、このクーラとヒータの両側に乾
燥通風路5を遮断するための遮断弁10,10を
設け、更に乾燥通風路の側壁に形成した吸気口1
1と排気口12を開閉するための吸気弁13と排
気弁14を設けている。なお前記クーラ8とヒー
タ9は蛇行状をした冷媒及び熱媒通路に多数の板
状フインを装着した通常のラジエータと同一の構
造である。 The following description will be given based on an example. 1 is a solvent tank, 2 is a circulation pump, 3 is a filter, and 4 is a washing tub. During the washing process, the solvent is circulated through these parts by the circulation pump. Reference numeral 5 denotes a drying ventilation passage whose both ends are connected to the washing tub, and a lint filter 6, a blower 7, a cooler 8 and a heater 9 are installed inside the drying ventilation passage.
In addition, cutoff valves 10, 10 are provided on both sides of the cooler and heater to shut off the drying ventilation path 5, and an air intake port 1 formed on the side wall of the drying ventilation path is provided.
1 and an exhaust port 12 are provided. The cooler 8 and heater 9 have the same structure as a normal radiator in which a large number of plate-like fins are attached to meandering refrigerant and heat medium passages.
乾燥行程時には吸気弁13及び排気弁14が吸
気口11と排気口12を閉鎖すると共に、遮断弁
10,10は乾燥通風路5を開いており、ヒータ
9で加熱された空気が送風機7によつてこの乾燥
通風路5内を循環することにより、洗濯槽内の洗
濯物から溶剤を蒸発してクーラ8で凝縮するよう
になつている。而して凝縮した溶剤は弁15を通
つて水分離器16に入り、更に前記溶剤タンク1
に回収される。 During the drying process, the intake valve 13 and the exhaust valve 14 close the intake port 11 and the exhaust port 12, and the cutoff valves 10 and 10 open the drying ventilation passage 5, so that the air heated by the heater 9 is passed through the blower 7. By circulating the solvent in the drying air passage 5, the solvent is evaporated from the laundry in the washing tub and condensed in the cooler 8. The condensed solvent then enters the water separator 16 through the valve 15 and is further transferred to the solvent tank 1.
will be collected.
脱臭行程時には遮断弁10,10が乾燥通風路
5を遮断すると共に、吸気弁13と排気弁14が
吸気口11と排気口12を開く。従つて吸気口1
1から新鮮な空気が吸込まれて、洗濯槽4内に充
満していた溶剤蒸気を排気口12から押出す。 During the deodorizing process, the cutoff valves 10, 10 shut off the drying air passage 5, and the intake valve 13 and the exhaust valve 14 open the intake port 11 and the exhaust port 12. Therefore, intake port 1
Fresh air is sucked in from 1, and the solvent vapor filling the washing tub 4 is pushed out from the exhaust port 12.
17は、基端側にエアコンプレツサを接続する
と共に、先端側を前記乾燥通風路5のクーラ8近
傍に接続した空気パイプで、該空気パイプ17か
ら流入した空気が前記クーラ8を通過してから排
出されるように、この乾燥通風路5と前記排気口
12との間に排気パイプ18を接続している。 Reference numeral 17 denotes an air pipe whose base end is connected to an air compressor and whose distal end is connected to the vicinity of the cooler 8 of the drying ventilation passage 5. Air flowing from the air pipe 17 passes through the cooler 8. An exhaust pipe 18 is connected between this drying ventilation path 5 and the exhaust port 12 so that the drying air is discharged from the drying air passage 5.
而して前記空気パイプ17内にはエゼクタ19
を介挿しており、該エゼクタの低圧部と蒸溜器2
0との間を蒸溜パイプ21で接続している。又こ
の蒸溜パイプから分岐した部分にコンデンサ22
を接続し、該コンデンサを前記水分離器16に接
続している。 There is an ejector 19 in the air pipe 17.
is inserted between the low pressure part of the ejector and the distiller 2.
0 through a distillation pipe 21. Also, a condenser 22 is installed at the part that branches off from this distillation pipe.
and the condenser is connected to the water separator 16.
溶剤の蒸溜時には、バルブ23を開いてフイル
タ3内の溶剤を硅藻土等の濾過材と共に蒸溜器2
0内に落とし、蒸溜を行なう。蒸溜器20内での
加熱によつて蒸発した溶剤蒸気は、コンデンサ2
2内で凝縮した後水分離器16に流入し、更に溶
剤タンク1に回収される。蒸溜器20内の溶剤が
ほとんど蒸発しきつた時にエアコンプレツサを運
転して空気パイプ17内に勢いよく空気を流し、
エゼクタ19によつて蒸溜器20内を減圧する。
減圧によつて蒸溜器20内の残滓に含まれている
溶剤まで完全に蒸発し、蒸発した溶剤はエゼクタ
19に吸込まれて、空気パイプ17を通つて乾燥
通風路5内に吹出る。この溶剤を含む空気は、乾
燥通風路5に吹出た後クーラ8を通過するが、こ
の時空気中に含まれている溶剤は凝縮して回収さ
れ、空気のみが排気パイプ18を通つて排出され
る。従つて蒸溜器20内の残滓に含まれている溶
剤まで全て回収される。 When distilling a solvent, the valve 23 is opened and the solvent in the filter 3 is pumped into the distiller 2 together with a filter material such as diatomaceous earth.
0 and perform distillation. The solvent vapor evaporated by heating in the distiller 20 is transferred to the condenser 2.
After being condensed in the solvent tank 2, it flows into the water separator 16 and is further collected in the solvent tank 1. When the solvent in the distiller 20 has almost completely evaporated, the air compressor is operated to forcefully flow air into the air pipe 17.
The pressure inside the distiller 20 is reduced by the ejector 19.
Due to the reduced pressure, the solvent contained in the residue in the distiller 20 is completely evaporated, and the evaporated solvent is sucked into the ejector 19 and blown out into the drying ventilation path 5 through the air pipe 17. This air containing the solvent is blown out into the drying air passage 5 and then passes through the cooler 8. At this time, the solvent contained in the air is condensed and recovered, and only the air is exhausted through the exhaust pipe 18. Ru. Therefore, all the solvent contained in the residue in the distiller 20 is recovered.
なお、前記コンデンサ22は、この中に一旦溶
剤蒸気を入れて貯溜し、その間に凝縮するもので
あるのに対して、クーラ8は空気がその表面を流
れる時にそこに含まれている溶剤を凝縮するのに
適するように設計されているので、このクーラ8
はコンデンサ22よりも溶剤の凝縮効果は低く、
従つて蒸溜の初期からエゼクタ19を使用してク
ーラ8側に溶剤蒸気を流すのは得策ではない。し
かしながらクーラ8の容量を大きくすれば、蒸溜
初期からクーラ8側に溶剤蒸気を流してもよい。 The condenser 22 temporarily stores solvent vapor and condenses it, whereas the cooler 8 condenses the solvent contained in the air as it flows over its surface. This cooler is designed to be suitable for
has a lower solvent condensation effect than condenser 22,
Therefore, it is not a good idea to use the ejector 19 to flow the solvent vapor toward the cooler 8 from the beginning of distillation. However, if the capacity of the cooler 8 is increased, the solvent vapor may be allowed to flow toward the cooler 8 from the initial stage of distillation.
以上の如く本発明は、乾燥通風路に一端を接続
した空気通路にエゼクタを介挿し、このエゼクタ
の低圧部を蒸溜器に接続しているので、エゼクタ
によつて蒸溜器内は減圧されて溶剤が蒸発し易く
なり、残滓に含まれている溶剤まで全て蒸発して
回収される。又前記乾燥通風路内のクーラは、空
気と溶剤蒸気の混合体から溶剤を凝縮して洗濯物
を乾燥するのに最も都合のよい形状に設計されて
いるので、エゼクタに於いて溶剤蒸気と多量の空
気が混合しても、蒸溜専用のコンデンサのように
凝縮効率を低下するようなことはない。更に前記
クーラは空気と溶剤の混合体から溶剤のみを凝縮
するのに適しているため、蒸溜器内を減圧するた
めにエゼクタを連続して作動させることができ、
蒸溜器内の溶剤を効率よく蒸発させることができ
る。 As described above, in the present invention, an ejector is inserted into the air passage whose one end is connected to the drying ventilation passage, and the low pressure part of this ejector is connected to the distiller, so that the pressure inside the distiller is reduced by the ejector, and the solvent is evaporates easily, and even the solvent contained in the residue is all evaporated and recovered. Also, the cooler in the drying air passage is designed in the most convenient shape to condense the solvent from the mixture of air and solvent vapor to dry the laundry, so that a large amount of solvent vapor and Even if air is mixed in, the condensation efficiency will not be reduced like in a condenser dedicated to distillation. Furthermore, since the cooler is suitable for condensing only the solvent from the mixture of air and solvent, the ejector can be operated continuously to reduce the pressure in the still;
The solvent in the distiller can be efficiently evaporated.
図面は本発明ドライクリーナの溶剤回路図であ
る。
4……洗濯槽、8……クーラ、9……ヒータ、
7……送風機、5……乾燥通風路、17……空気
パイプ、19……エゼクタ、20……蒸溜器、2
1……蒸溜パイプ。
The drawing is a solvent circuit diagram of the dry cleaner of the present invention. 4...Washing tub, 8...Cooler, 9...Heater,
7... Blower, 5... Drying ventilation path, 17... Air pipe, 19... Ejector, 20... Distiller, 2
1... Distillation pipe.
Claims (1)
タ及び送風機を内設した乾燥通風路に空気パイプ
を接続して、該パイプの途中にエゼクタを介挿
し、一端を蒸溜器に接続した蒸溜パイプの他端側
をこのエゼクタの低圧部分に接続してなるドライ
クリーナ。1. Other than a distillation pipe, in which both ends are connected to a washing tub, an air pipe is connected to a drying ventilation passage with a cooler/heater and a blower installed inside, an ejector is inserted in the middle of the pipe, and one end is connected to a distiller. A dry cleaner whose end is connected to the low pressure part of this ejector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16845881A JPS5869597A (en) | 1981-10-20 | 1981-10-20 | Dry cleaner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16845881A JPS5869597A (en) | 1981-10-20 | 1981-10-20 | Dry cleaner |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5869597A JPS5869597A (en) | 1983-04-25 |
| JPS6157798B2 true JPS6157798B2 (en) | 1986-12-08 |
Family
ID=15868479
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16845881A Granted JPS5869597A (en) | 1981-10-20 | 1981-10-20 | Dry cleaner |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5869597A (en) |
-
1981
- 1981-10-20 JP JP16845881A patent/JPS5869597A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5869597A (en) | 1983-04-25 |
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