JPS6213593Y2 - - Google Patents

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Publication number
JPS6213593Y2
JPS6213593Y2 JP1981073807U JP7380781U JPS6213593Y2 JP S6213593 Y2 JPS6213593 Y2 JP S6213593Y2 JP 1981073807 U JP1981073807 U JP 1981073807U JP 7380781 U JP7380781 U JP 7380781U JP S6213593 Y2 JPS6213593 Y2 JP S6213593Y2
Authority
JP
Japan
Prior art keywords
solvent
condenser
exhaust port
pipe
exhaust
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
JP1981073807U
Other languages
Japanese (ja)
Other versions
JPS57187188U (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 JP1981073807U priority Critical patent/JPS6213593Y2/ja
Publication of JPS57187188U publication Critical patent/JPS57187188U/ja
Application granted granted Critical
Publication of JPS6213593Y2 publication Critical patent/JPS6213593Y2/ja
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 本案は溶剤損失の少い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 low solvent loss.

蒸溜装置を備えたドライクリーナは、蒸溜時に
溶剤凝縮用コンデンサ内の圧力が変動するため
に、このコンデンサに排気用パイプと吸気用パイ
プを接続したり両パイプを一本で兼用した均圧パ
イプを接続したりして前記蒸溜用コンデンサ内の
圧力変動を少くしているが、前記パイプから溶剤
が蒸気となつて漏れることが多く、溶剤損失の原
因となるばかりか作業場の空気を汚染する原因に
もなつていた。
In dry cleaners equipped with a distillation device, the pressure inside the solvent condensation condenser fluctuates during distillation, so it is necessary to connect an exhaust pipe and an intake pipe to the condenser, or to install a pressure equalizing pipe that serves as both pipes. Although pressure fluctuations in the distillation condenser are reduced by connecting the pipes, the solvent often leaks as vapor from the pipes, which not only causes solvent loss but also contaminates the air in the workplace. It was also getting old.

本案はこのような欠点を解消せんとするもの
で、以下従来例に引き続いて本案を説明する。
The present invention is intended to eliminate such drawbacks, and the present invention will be explained below following the conventional example.

第1図は従来例で、1,2は第1溶剤タンク及
び第2溶剤タンク、3はポンプ、4は洗濯槽、5
は洗濯中にとれた釦や糸屑等をとるボタントラツ
プで、これ等によつて溶剤回路を構成している。
洗濯は2回行われ、第1回目の洗濯行程時にはバ
ルブ6が開いてポンプ3が回転し、第1溶剤タン
ク1内の溶剤が洗濯槽4に入れられる。
Figure 1 shows a conventional example, where 1 and 2 are a first solvent tank and a second solvent tank, 3 is a pump, 4 is a washing tub, and 5
is a button trap that collects buttons, lint, etc. that come off during washing, and these traps make up the solvent circuit.
Washing is performed twice, and during the first washing process, the valve 6 is opened, the pump 3 is rotated, and the solvent in the first solvent tank 1 is poured into the washing tub 4.

7は蒸溜器、8は溶剤蒸気を凝縮するためのコ
ンデンサ、9は凝縮した溶剤から水分を分離する
ための水分離器であり、これ等によつて蒸溜装置
が構成されている。前記第1回目の洗濯が終つた
時、バルブ10が開いて洗濯槽4内の溶剤が蒸溜
器7に入り、蒸溜が行われる。即ち蒸溜器7内の
ヒータが発熱して溶剤を蒸発し、この蒸発した溶
剤はコンデンサ8に於て冷却されて凝縮する。凝
縮した溶剤は水分離器9に入つてここで水分を分
離し、純粋の溶剤のみが第2溶剤タンク2に回収
される。
7 is a distiller, 8 is a condenser for condensing solvent vapor, and 9 is a water separator for separating water from the condensed solvent, and these constitute a distillation apparatus. When the first washing is completed, the valve 10 is opened and the solvent in the washing tub 4 enters the distiller 7, where it is distilled. That is, the heater in the distiller 7 generates heat to evaporate the solvent, and the evaporated solvent is cooled and condensed in the condenser 8. The condensed solvent enters a water separator 9 where water is separated and only pure solvent is collected in the second solvent tank 2.

なお第1回目の洗濯が終つて洗濯槽4内の溶剤
が蒸溜器7に入れられた後、バルブ11が開いて
ポンプ3が回転し、第2溶剤タンク2内の溶剤が
洗濯槽4に入れられて第2回目の洗濯が行われ
る。第2回目の洗濯が終了した時、バルブ12が
開いて洗濯槽4内の溶剤は第1溶剤タンク1に回
収され、その後脱液と乾燥が行われる。乾燥は、
回収槽13内に設けたヒータで熱した空気を洗濯
槽4内に吹出し、この洗濯槽内の衣類から溶剤を
蒸発して、この蒸発した溶剤を前記回収槽13内
に再び吸込み、この回収槽内の凝縮器で凝縮する
ことによつて行う。凝縮した溶剤はバルブ14を
通つて水分離器9に入り、更に第2溶剤タンク2
に回収される。この乾燥行程の最終時には排気バ
ルブを開き、回収槽に突設した排気口15から排
気ダクト16を通して残つた溶剤蒸気を室外に排
気するようにしている。
After the first washing is finished and the solvent in the washing tub 4 is put into the distiller 7, the valve 11 is opened and the pump 3 is rotated, and the solvent in the second solvent tank 2 is put into the washing tub 4. The second washing is then carried out. When the second washing is completed, the valve 12 is opened and the solvent in the washing tub 4 is collected into the first solvent tank 1, after which dehydration and drying are performed. Drying is
Air heated by a heater installed in the collection tank 13 is blown into the washing tub 4 to evaporate the solvent from the clothes in the washing tub, and the evaporated solvent is sucked into the collection tank 13 again. This is done by condensing it in the condenser inside. The condensed solvent enters the water separator 9 through the valve 14 and then into the second solvent tank 2.
will be collected. At the end of this drying process, the exhaust valve is opened and the remaining solvent vapor is exhausted to the outside through an exhaust port 15 protruding from the recovery tank and an exhaust duct 16.

しかるに前記した蒸溜時には、蒸溜器7からコ
ンデンサ8に溶剤蒸気が流入するので、このコン
デンサ8内の圧力が上昇する。圧力が高くなり過
ぎるとこのコンデンサが破裂するおそれがあるの
で、一般に水分離器9と排気口15との間に排気
パイプ17を設け、コンデンサ8内の圧力を水分
離器9と排気パイプ17を介して逃がすようにし
ている。しかるに1回目の蒸溜が終り、2回目の
蒸溜をするために新たな溶剤を蒸溜器7に入れる
と、この蒸溜器が溶剤により冷やされて内部の圧
力が低下し、前記排気口15から排気パイプ1
7・水分離器9及びコンデンサ8を通して空気を
吸込もうとする。この時この空気と一緒に水分離
器9内の水も一緒にコンデンサ8に吸込まれるこ
とがあり、折角溶剤と分離した水が再び溶剤と混
合してしまうことになる。そこで従来は、コンデ
ンサ8に逆止弁18を有する吸気パイプ19を接
続し、コンデンサ8が負圧になつた時にこの吸気
パイプ19から空気を吸込んで圧力が一定になる
ようにしている。しかるに前記逆止弁18が故障
していると、コンデンサ8内の圧力が高くなつた
時に、溶剤蒸気が逆止弁18を逆流して作業場に
吹き出ることがあり、作業場の空気を汚染するこ
とがあつた。又逆止弁18が正常に作働している
場合は、コンデンサ8内の圧力が高くなつた時
に、この中にある溶剤蒸気は水分離器9と排気パ
イプ17を通して排気口15に流出し、この排気
口に流出した溶剤蒸気は排気ダクト16を通して
大気中に排出されるので、この点からも大気汚染
の原因となると共に溶剤損失の原因となつてい
た。
However, during the above-mentioned distillation, solvent vapor flows from the distiller 7 into the condenser 8, so that the pressure inside the condenser 8 increases. If the pressure becomes too high, there is a risk that this condenser will burst, so generally an exhaust pipe 17 is provided between the water separator 9 and the exhaust port 15 to reduce the pressure inside the condenser 8. I'm trying to let it escape. However, when the first distillation is finished and a new solvent is put into the still 7 for the second distillation, the still is cooled by the solvent and the internal pressure decreases, and the exhaust pipe is discharged from the exhaust port 15. 1
7. Try to suck air through the water separator 9 and condenser 8. At this time, the water in the water separator 9 may be sucked into the condenser 8 together with this air, and the water separated from the solvent will be mixed with the solvent again. Conventionally, an intake pipe 19 having a check valve 18 is connected to the capacitor 8, and when the pressure in the capacitor 8 becomes negative, air is sucked in from the intake pipe 19 to keep the pressure constant. However, if the check valve 18 is malfunctioning, when the pressure inside the condenser 8 becomes high, solvent vapor may flow back through the check valve 18 and blow out into the workplace, contaminating the air in the workplace. It was hot. If the check valve 18 is operating normally, when the pressure inside the condenser 8 becomes high, the solvent vapor therein will flow out to the exhaust port 15 through the water separator 9 and the exhaust pipe 17. The solvent vapor flowing out of the exhaust port is discharged into the atmosphere through the exhaust duct 16, which causes air pollution and solvent loss.

これに対して本案は、第2図に示す如く逆止弁
18を有する吸気パイプ19をコンデンサ8と排
気口15との間に接続している。その結果、蒸溜
時にコンデンサ8内の圧力が高くなると、その圧
力空気は水分離器9と排気パイプ17を介して排
気口15に逃げ、この逃げた空気中に含まれてい
る溶剤は排気口15内にただよつている。そこで
第2回目の蒸溜時にコンデンサ8内の圧力が低下
すると、前記排気口15内の空気が吸気パイプ1
9を通してコンデンサ8に吸込まれ、この時排気
口15内にただよつていた溶剤蒸気も再びコンデ
ンサ8に吸込まれるので、溶剤損失が少く、又大
気汚染の原因となることも少い。なお20,21
は溶剤タンクやボタントラツプ内を大気圧に保つ
ための均圧パイプである。
In contrast, in the present invention, as shown in FIG. 2, an intake pipe 19 having a check valve 18 is connected between the condenser 8 and the exhaust port 15. As a result, when the pressure inside the condenser 8 increases during distillation, the pressure air escapes to the exhaust port 15 via the water separator 9 and the exhaust pipe 17, and the solvent contained in this escaped air is removed from the exhaust port 15. It's floating inside. Therefore, when the pressure inside the condenser 8 decreases during the second distillation, the air inside the exhaust port 15 flows into the intake pipe 1.
Since the solvent vapor that was floating in the exhaust port 15 at this time is also sucked into the condenser 8 again, there is little loss of solvent and it is less likely to cause air pollution. Note 20, 21
is a pressure equalizing pipe that maintains atmospheric pressure inside a solvent tank or button trap.

第3図は他の実施例を示している。この実施例
ではコンデンサ8が水分離器を兼用しており、そ
の詳細は第4図に示されている。即ちこのコンデ
ンサ8は、外装ケーシング22内に気水分離筒2
3と冷却コイル24とを有すると共に、このケー
シングの底面より前記気水分離筒23内に向つて
溢水パイプ25と溶剤流出パイプ26とを突出し
ている。27は溶剤流出パイプ26より水が溢水
しないようにするための遮蔽パイプである。又前
記外装ケーシング22には、前記蒸溜器7で蒸発
した溶剤蒸気の流入する溶剤蒸気流入口28と、
前記溶剤回収槽13内で凝縮した溶剤の流入する
液状溶剤流入口29とを備えると共に、この外装
ケーシング22内の圧力を逃がすための均圧パイ
プ30を接続している。この均圧パイプははその
先端側が排気パイプ17と吸気パイプ19とに分
岐し、それ等排気パイプと吸気パイプの先端は前
記排気口15に夫々接続している。なお吸気パイ
プ19には、前記コンデンサ8が負圧になつた時
にすぐ開く逆止弁18が設けられ、又排気パイプ
17には、コンデンサ8内の圧力が一定値以上に
なつた時に開く逆止弁31が設けられている。
FIG. 3 shows another embodiment. In this embodiment, the condenser 8 also serves as a water separator, the details of which are shown in FIG. That is, this condenser 8 has a steam/water separation tube 2 inside an outer casing 22.
3 and a cooling coil 24, and an overflow pipe 25 and a solvent outflow pipe 26 protrude into the steam/water separation cylinder 23 from the bottom surface of the casing. 27 is a shielding pipe for preventing water from overflowing from the solvent outflow pipe 26. The exterior casing 22 also includes a solvent vapor inlet 28 into which the solvent vapor evaporated in the distiller 7 flows;
It is provided with a liquid solvent inlet 29 through which the solvent condensed in the solvent recovery tank 13 flows, and is connected to a pressure equalizing pipe 30 for releasing the pressure inside the exterior casing 22. The pressure equalizing pipe branches into an exhaust pipe 17 and an intake pipe 19 at its distal end, and the distal ends of the exhaust pipe and intake pipe are connected to the exhaust port 15, respectively. The intake pipe 19 is provided with a check valve 18 that opens immediately when the condenser 8 becomes negative pressure, and the exhaust pipe 17 is provided with a check valve 18 that opens when the pressure inside the condenser 8 exceeds a certain value. A valve 31 is provided.

従つてこの実施例に於ても、蒸溜時にコンデン
サ8内の圧力が一定値以上になると、前記排気パ
イプ内の逆止弁17を押し開いて圧力を排気口1
5内に逃がす。この時溶剤蒸気も一緒に排気口に
桃げるが、この溶剤蒸気は排気口15部分にただ
よつている。第2回目の蒸溜時に蒸溜器7内に溶
剤を入れると、この蒸溜器7及びコンデンサ8内
が負圧となり、吸気パイプ19に設けた逆止弁1
8がただちに開いて排気口15からコンデンサ8
内に空気を吸込んで圧力を一定に保つと共に、前
記排気口15にただよつていた溶剤蒸気も一緒に
吸込んで回収するので溶剤の損失が少い。
Therefore, in this embodiment, when the pressure inside the condenser 8 exceeds a certain value during distillation, the check valve 17 in the exhaust pipe is pushed open to release the pressure to the exhaust port 1.
Escape within 5. At this time, solvent vapor also flows into the exhaust port, but this solvent vapor floats to the exhaust port 15. When the solvent is put into the still 7 during the second distillation, the inside of the still 7 and the condenser 8 become negative pressure, and the check valve 1 installed in the intake pipe 19
8 opens immediately and the condenser 8 is removed from the exhaust port 15.
Air is sucked into the exhaust port 15 to keep the pressure constant, and the solvent vapor that has been floating in the exhaust port 15 is also sucked in and recovered, so there is little loss of solvent.

以上の如く本案は、吸気パイプ19と排気パイ
プ17の先端を共に回収槽に設けた排気口15に
接続しているので、蒸溜時に排気パイプ17を通
つて排気口15に流れ出た溶剤蒸気は、次の蒸溜
時に蒸溜器7内に溶剤を入れた時に、吸気パイプ
19を通して再びコンデンサ8に吸込まれ、溶剤
損失を減少することができると共に、逆止弁1
8,31の故障によつて溶剤蒸気が多量に流出し
ても、前記排気口15から排気ダクト16を通し
て所定位置に導かれるので、作業場の空気を汚す
こともない。
As described above, in this case, the tips of the intake pipe 19 and the exhaust pipe 17 are both connected to the exhaust port 15 provided in the recovery tank, so that the solvent vapor flowing out to the exhaust port 15 through the exhaust pipe 17 during distillation is When the solvent is introduced into the distiller 7 during the next distillation, it is sucked into the condenser 8 again through the suction pipe 19, reducing solvent loss, and the check valve 1
Even if a large amount of solvent vapor leaks out due to a failure of the vents 8 and 31, it will not contaminate the air in the workplace because it will be guided from the exhaust port 15 to a predetermined position through the exhaust duct 16.

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

第1図は従来のドライクリーナの溶剤回路図、
第2図及び第3図は互に異なる実施例に於ける本
案ドライクリーナの溶剤回路図、第4図は第3図
のドライクリーナに使用されている蒸溜用コンデ
ンサの縦断側面図である。 7……蒸溜器、8……コンデンサ、9……水分
離器、13……回収槽、15……排気口、17…
…排気パイプ、18……逆止弁、19……吸気パ
イプ。
Figure 1 is a conventional dry cleaner solvent circuit diagram.
2 and 3 are solvent circuit diagrams of the dry cleaner of the present invention in mutually different embodiments, and FIG. 4 is a longitudinal sectional side view of a distillation capacitor used in the dry cleaner of FIG. 3. 7... Distiller, 8... Condenser, 9... Water separator, 13... Recovery tank, 15... Exhaust port, 17...
...Exhaust pipe, 18...Check valve, 19...Intake pipe.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 蒸溜器とコンデンサと水分離器よりなる蒸溜装
置、及び洗濯槽内の衣類から溶剤を回収する回収
槽を備えたものに於て、この回収槽に設けた排気
口と前記コンデンサ又は水分離器との間にコンデ
ンサ内の圧力が高くなつた時にそれを逃す排気パ
イプを設けると共に、前記排気口とコンデンサと
の間に、このコンデンサ内が負圧になつた時に開
く逆止弁を介挿した吸気パイプを設けてなるドラ
イクリーナ。
In a device equipped with a distillation device consisting of a distiller, a condenser, and a water separator, and a recovery tank for recovering the solvent from clothes in the washing tub, an exhaust port provided in the recovery tank and the condenser or water separator are connected to each other. In addition, an exhaust pipe is provided to release the pressure inside the condenser when it becomes high, and a check valve is inserted between the exhaust port and the condenser, which opens when the pressure inside the condenser becomes negative. A dry cleaner with a pipe.
JP1981073807U 1981-05-20 1981-05-20 Expired JPS6213593Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1981073807U JPS6213593Y2 (en) 1981-05-20 1981-05-20

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1981073807U JPS6213593Y2 (en) 1981-05-20 1981-05-20

Publications (2)

Publication Number Publication Date
JPS57187188U JPS57187188U (en) 1982-11-27
JPS6213593Y2 true JPS6213593Y2 (en) 1987-04-08

Family

ID=29869573

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1981073807U Expired JPS6213593Y2 (en) 1981-05-20 1981-05-20

Country Status (1)

Country Link
JP (1) JPS6213593Y2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5818874Y2 (en) * 1979-03-07 1983-04-16 三洋電機株式会社 dry cleaner

Also Published As

Publication number Publication date
JPS57187188U (en) 1982-11-27

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