JPH0121672Y2 - - Google Patents
Info
- Publication number
- JPH0121672Y2 JPH0121672Y2 JP1981046465U JP4646581U JPH0121672Y2 JP H0121672 Y2 JPH0121672 Y2 JP H0121672Y2 JP 1981046465 U JP1981046465 U JP 1981046465U JP 4646581 U JP4646581 U JP 4646581U JP H0121672 Y2 JPH0121672 Y2 JP H0121672Y2
- Authority
- JP
- Japan
- Prior art keywords
- solvent
- tank
- light
- amount
- pump
- 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
- 239000002904 solvent Substances 0.000 claims description 104
- 238000011084 recovery Methods 0.000 claims description 19
- 238000011109 contamination Methods 0.000 claims description 14
- 238000005108 dry cleaning Methods 0.000 claims description 12
- 239000003960 organic solvent Substances 0.000 claims description 11
- 238000004821 distillation Methods 0.000 claims description 9
- 238000004140 cleaning Methods 0.000 claims description 7
- 238000005192 partition Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 2
- 230000003287 optical effect Effects 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000000498 cooling water Substances 0.000 description 3
- 238000001514 detection method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 2
- 238000010186 staining Methods 0.000 description 2
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- CYTYCFOTNPOANT-UHFFFAOYSA-N Perchloroethylene Chemical group ClC(Cl)=C(Cl)Cl CYTYCFOTNPOANT-UHFFFAOYSA-N 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 210000004243 sweat Anatomy 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
Landscapes
- Investigating Or Analysing Materials By Optical Means (AREA)
Description
【考案の詳細な説明】
本考案はパークロエチレン、111トリクロルエ
タン、R113等の有機溶剤を使用するドライクリ
ーニング機の溶剤回収制御装置に関する。[Detailed Description of the Invention] The present invention relates to a solvent recovery control device for a dry cleaning machine that uses organic solvents such as perchloroethylene, 111 trichloroethane, and R113.
例えば、ドライクリーニング機械は、第1図系
統図に示すように、ドア1から処理ドラム11中
に投入された衣料2を上記有機溶剤を使用して下
記工程でクリーニングする。 For example, as shown in the system diagram of FIG. 1, a dry cleaning machine cleans clothing 2 placed into a processing drum 11 through a door 1 using the organic solvent described above in the following steps.
(1) 溶剤タンク3から溶剤4をバルブ5を介して
ポンプ6で汲揚げ、これをバルブ7、フイルタ
8から成る経路又はバルブ9から成る経路を経
て処理槽10に必要量送り込む。(1) The solvent 4 is pumped up from the solvent tank 3 through the valve 5 with the pump 6, and the required amount is sent into the processing tank 10 through the path consisting of the valve 7 and the filter 8 or the path consisting of the valve 9.
(2) 処理ドラム11をゆつくり回動し、溶剤4を
処理槽10、ボタントラツプ12、バルブ1
3、ポンプ6、バルブ7、フイルタ8、又はバ
ルブ9から成る回路を通して循環することによ
り衣料2を洗浄する。(2) Slowly rotate the processing drum 11 and pour the solvent 4 into the processing tank 10, button trap 12, and valve 1.
3. Clothes 2 are washed by circulation through a circuit consisting of pump 6, valve 7, filter 8 or valve 9.
(3) 溶剤を処理槽11、ボタントラツプ12、バ
ルブ13、ポンプ6、バルブ14、蒸留器15
の経路で排液し、続いて処理ドラム11を高速
回転して衣料2中の溶剤4を遠心分離し、同様
に排液する。(3) Solvent processing tank 11, button trap 12, valve 13, pump 6, valve 14, distiller 15
Subsequently, the processing drum 11 is rotated at high speed to centrifugally separate the solvent 4 in the clothing 2, and the liquid is drained in the same manner.
(4) (1)項、(2)項の工程をくり返す。(4) Repeat steps (1) and (2).
(5) 処理ドラム11、ボタントラツプ12、バル
ブ13、バルブ5の経路で溶剤を溶剤タンク3
に排液し、続いて処理ドラム11を高速回転し
て衣料2中の溶剤4を遠心分離し、排液する。(5) Transfer the solvent to the solvent tank 3 through the processing drum 11, button trap 12, valve 13, and valve 5.
Then, the processing drum 11 is rotated at high speed to centrifugally separate the solvent 4 in the clothing 2, and the liquid is drained.
(6) 再び処理ドラム11をゆつくり回動し、フア
ン16、エアクーラ17、エアヒータ18から
成るリカバリエアダクト19と処理槽10の間
を矢印20の方向にエアを循環し、衣料2を乾
燥する。(6) The processing drum 11 is slowly rotated again, and air is circulated in the direction of the arrow 20 between the recovery air duct 19 consisting of the fan 16, the air cooler 17, and the air heater 18 and the processing tank 10 to dry the clothes 2.
衣料2から蒸発した溶剤ガスは、エアクーラ
17で凝縮し、回収経路21を経て水分離器2
2、溶剤配管23を経てクリンタンク24に回
収する。 The solvent gas evaporated from the clothing 2 is condensed in the air cooler 17 and passed through the recovery path 21 to the water separator 2.
2. Collect into the clean tank 24 via the solvent pipe 23.
(7) 乾燥が終了すると、ダンパ25,26を破線
の如く開き、ダンパ25から新鮮空気を取入
れ、ダンパ26からエアクーラ17では回収で
きない未凝縮溶剤ガスを排気し、衣料2中の溶
剤臭を脱臭する。(7) When drying is completed, the dampers 25 and 26 are opened as shown by the broken lines, fresh air is taken in from the damper 25, and uncondensed solvent gas that cannot be recovered by the air cooler 17 is exhausted from the damper 26, thereby deodorizing the solvent odor in the clothing 2. do.
(8) (2)項の工程で蒸留器15に入つた溶剤4を蒸
発してコンデンサ27で凝縮回収し、水分離器
22、溶剤配管23、クリンタンク24、オー
バフロー付仕切板28を経て溶剤タンク3に回
収する。(8) The solvent 4 that entered the distiller 15 in the step (2) is evaporated, condensed and recovered in the condenser 27, and the solvent passes through the water separator 22, solvent piping 23, clean tank 24, and overflow partition plate 28. Collect into tank 3.
なお、水分離器22で分離した水は水配管29
によつて系外へ排出する。 Note that the water separated by the water separator 22 is transferred to the water pipe 29.
It is discharged out of the system by
こうして衣料を洗浄した溶剤の汚れには大きく
分けて固形汚れと溶剤汚れがあり、前者には、土
砂、人毛、リントなどが、後者には一般の油性汚
れ、汗、染料落ちなどが含まれ、溶剤の汚れの程
度は、前者汚れの含有率で決まるが、通常のドラ
イクリーニング機械では、衣料から排出される汚
れ量と、蒸留量の多少によつて溶剤汚れは左右さ
れる。 The solvent stains that wash clothes in this way can be broadly divided into solid stains and solvent stains.The former includes dirt, human hair, lint, etc., and the latter includes general oil stains, sweat, dye removal, etc. The degree of solvent staining is determined by the content of the former stain, but in ordinary dry cleaning machines, solvent staining depends on the amount of stains discharged from clothing and the amount of distillation.
しかしながら、従来のクリーニング機械では、
溶剤に大きな影響のある衣料の汚れの多少はこれ
を無視して常に一定量の溶剤を蒸留しており、場
合によつては、溶剤中の汚れが過剰に蓄積するの
で、洗浄力が低下したり、一旦溶剤側に移つた汚
れが衣料に再び付着(吸着)する逆汚染(グレイ
イング)を生ずることがあり、また、逆に衣料の
汚れが少ないときは、必要以上の溶剤を蒸留する
ことになり、エネルギ、冷却水、洗剤などの無駄
使いになる。 However, with conventional cleaning machines,
A certain amount of solvent is always distilled, ignoring the amount of dirt on clothing that has a large effect on the solvent. In some cases, too much dirt accumulates in the solvent, reducing the cleaning power. Otherwise, dirt that has once transferred to the solvent side may be reattached (adsorbed) to the clothing, resulting in reverse contamination (graying).On the other hand, when the clothing is lightly soiled, it may be necessary to distill more solvent than necessary. This results in wasted energy, cooling water, detergent, etc.
本考案はこのような事情に鑑みて提案されたも
ので、省エネルギを図り、冷却水、溶剤等の無駄
使いをなくするドライクリーニング機の溶剤回収
制御装置を提供することを目的とし、洗浄工程中
処理槽内の有機溶剤をポンプを介してフイルター
に導き同溶剤を過したのち再び該処理槽に戻す
循環回路と、上記処理槽からの使用済有機溶剤を
上記ポンプにより蒸溜器に導き溶剤分を蒸溜回収
し同回収溶剤をクリーンタンクに導く第1の溶剤
回収回路と、上記クリーンタンクにオーバフロー
仕切板を介して接続され貯溜溶剤を上記ポンプに
供給し、また上記処理槽の溶剤を受入れることの
できる溶剤タンクと、上記処理槽に接続するリカ
バリダクト内に配設したフアン、エアクーラ、エ
アヒータをそれぞれ作動させ同処理槽から発生す
る溶剤ガスから溶剤分を凝縮回収し、同回収溶剤
を上記クリーンタンクに導く第2の溶剤回収回路
とを備えてなる大型ドライクリーニング機におい
て、該溶剤の流路あるいは収納タンクに付設され
一部を透明部材で形成し同透明部材の近傍で同部
材に投光し溶剤中に光路を通過させる投光器及び
該投光器からの光路を受光し同受光量に基づき上
記溶剤の汚れ度をリアルタイムで連続的に検知す
る受光器よりなる汚れ度検知器と、同受光器の検
知結果に基づいて溶剤流路に設けた弁をリアルタ
イムで連続的に切替調整し、上記処理槽から排出
される有機溶剤の上記蒸留器への供給量並びに溶
剤タンクへの戻し量をそれぞれ制御する蒸留量溶
剤制御装置とを具えたことを特徴とする。 The present invention was proposed in view of these circumstances, and aims to provide a solvent recovery control device for dry cleaning machines that saves energy and eliminates wasted use of cooling water, solvent, etc. A circulation circuit in which the organic solvent in the medium treatment tank is guided through a pump to a filter, where the solvent is passed through, and then returned to the treatment tank, and the spent organic solvent from the treatment tank is guided into the distiller by the pump, where the solvent is removed. a first solvent recovery circuit that distills and recovers the solvent and guides the recovered solvent to a clean tank; and a first solvent recovery circuit that is connected to the clean tank via an overflow partition plate, supplies the stored solvent to the pump, and receives the solvent from the processing tank. The fans, air coolers, and air heaters installed in the solvent tank that can be used for cleaning, and the recovery duct connected to the treatment tank are operated to condense and recover the solvent from the solvent gas generated from the treatment tank, and the recovered solvent is transferred to the above-mentioned cleaner. In a large dry cleaning machine equipped with a second solvent recovery circuit leading to a tank, the solvent flow path or the storage tank is attached to the tank and a part thereof is formed of a transparent member, and light is projected onto the member near the transparent member. a contamination degree detector consisting of a light projector that allows an optical path to pass through the solvent, and a light receiver that receives the light path from the projector and continuously detects the degree of contamination of the solvent in real time based on the amount of received light; Based on the detection results, the valves installed in the solvent flow path are continuously switched and adjusted in real time to control the amount of organic solvent discharged from the treatment tank that is supplied to the distiller and the amount that is returned to the solvent tank. It is characterized by comprising a distillation amount solvent control device.
本考案を第1図のドライクリーニング機械に適
用した一実施例の溶剤汚れ度検出装置を、図面に
ついて説明すると、第2図はその部分縦断面図で
ある。 An embodiment of a solvent stain level detecting device in which the present invention is applied to the dry cleaning machine shown in FIG. 1 will be described with reference to the drawings. FIG. 2 is a partial vertical sectional view thereof.
上図において、aは第1図の洗浄回路、そのバ
イパス回路又は溶剤タンクの一部を構成する溶剤
管路、bは管路aに挿入されガラス等の透明部材
よりなる円筒状透明チヤンバ、fおよびeは透明
チヤンバbの対向する両側にそれぞれ付設された
投光器および受光器、dはガスケツトcを介して
透明チヤンバbの上下端をそれぞれ溶剤管路aに
気密に固着する袋ナツトである。 In the above diagram, a is a solvent pipe constituting part of the cleaning circuit shown in FIG. 1, its bypass circuit, or a solvent tank, b is a cylindrical transparent chamber inserted into pipe a and made of a transparent member such as glass, and f is and e are a light projector and a light receiver respectively attached to opposite sides of transparent chamber b, and d is a cap nut for airtightly fixing the upper and lower ends of transparent chamber b to solvent pipe a through gasket c.
このような装置において、透明チヤンバbに流
入する溶剤の汚れ程度によつて、投光器fから発
光される光量の受光器eに入る光量は変化する。 In such a device, the amount of light emitted from the projector f and the amount of light entering the receiver e changes depending on the degree of contamination of the solvent flowing into the transparent chamber b.
受光器eには一般的は光電素子を使用し、アン
プを介して、光量と比例した直流アナログ電圧信
号を取出すことにより、溶剤汚れを電圧に変換す
る。 A photoelectric element is generally used in the light receiver e, and the solvent stain is converted into voltage by extracting a DC analog voltage signal proportional to the amount of light via an amplifier.
なお、投光器fとしてはタングステンランプ、
各種発光ダイオードなど、受光器eでは、赤外か
ら可視域までの受光素子(Cds素子など)が一般
的であり、発光ダイオードではドリフト対策とし
て交流点灯も有効である。 In addition, the floodlight f is a tungsten lamp,
In the light receiver e, such as various light emitting diodes, a light receiving element (such as a CDS element) ranging from infrared to visible range is generally used, and alternating current lighting is also effective as a countermeasure against drift in light emitting diodes.
受光器の出力する直流アナログ電圧は必要度に
応じて下記の如く使い分ける。 The DC analog voltage output from the photoreceiver is used as shown below depending on the necessity.
(1) 基準汚れに対応する基準電圧を設定し、出力
電圧が基準電圧を下廻れば警報を出し、又は規
定量の蒸留を行なう。(1) Set a reference voltage corresponding to reference contamination, and if the output voltage falls below the reference voltage, issue an alarm or perform a specified amount of distillation.
(2) 溶剤汚れを段階的に規定し、それぞれに対応
する電圧を設定して出力がどの段階に入るか
で、蒸留量を決定する。(2) The amount of distillation is determined by defining the solvent contamination in stages, setting the voltage corresponding to each stage, and determining which stage the output falls into.
(3) 溶剤汚れに対応する直流アナログ電圧に比例
して弁5及び又は弁14を介して蒸留量を連続
的に制御する(比例制御)。(3) Continuously control the distillation amount via valve 5 and/or valve 14 in proportion to the DC analog voltage corresponding to solvent contamination (proportional control).
前記(1)〜(3)を適用することにより、溶剤汚れの
程度に応じて蒸留量を制御することができるの
で、蒸留エネルギの無駄使いの防止、洗浄力増
大、逆汚染の軽減が可能となり、特に大量のドラ
イクリーニングを高稼働率で経済的に行うことが
できる。 By applying (1) to (3) above, it is possible to control the amount of distillation depending on the degree of solvent contamination, thereby preventing wasted distillation energy, increasing cleaning power, and reducing back contamination. In particular, large quantities of dry cleaning can be carried out economically at high operating rates.
(4) さらに、必要に応じて、溶剤タンク中の溶剤
の一部をポンプを介して処理槽に供給するとと
もに、処理槽中の溶剤の一部をポンプを介して
蒸留器へ供給することにより、溶剤タンクの溶
剤ひいては処理槽中の溶剤の汚れ度を自動的に
設定値以内に係持することができる。(4) Furthermore, if necessary, part of the solvent in the solvent tank is supplied to the treatment tank via a pump, and a part of the solvent in the treatment tank is supplied to the distiller via a pump. The degree of contamination of the solvent in the solvent tank and, in turn, the solvent in the processing tank can be automatically maintained within a set value.
その際、透明チヤンバbが汚れた場合は袋ナ
ツトdを外して容易にこれを掃除することがで
きる。 At this time, if the transparent chamber b becomes dirty, it can be easily cleaned by removing the cap nut d.
上記実施例では、透過型受光量検出器を用いた
が、投光器と受光器とを共通のブロツク中に収容
した反射型のものを使用することもできる。 In the above embodiment, a transmission type received light amount detector is used, but a reflection type one in which a light emitter and a light receiver are housed in a common block may also be used.
要するに本考案によれば、洗浄工程中処理槽内
の有機溶剤をポンプを介してフイルターに導き同
溶剤を過したのち再び該処理槽に戻す循環回路
と、上記処理槽からの使用済有機溶剤を上記ポン
プにより蒸溜器に導き溶剤分を蒸溜回収し同回収
溶剤をクリーンタンクに導く第1の溶剤回収回路
と、上記クリーンタンクにオーバフロー仕切板を
介して接続され貯溜溶剤を上記ポンプに供給し、
また上記処理槽の溶剤を受入れることのできる溶
剤タンクと、上記処理槽に接続するリカバリダク
ト内に配設したフアン、エアクーラ、エアヒータ
をそれぞれ作動させ同処理槽から発生する溶剤ガ
スから溶剤分を凝縮回収し、同回収溶剤を上記ク
リーンタンクに導く第2の溶剤回収回路とを備え
てなる大型ドライクリーニング機において、該溶
剤の流路あるいは収納タンクに付設され一部を透
明部材で形成し同透明部材の近傍で同部材に投光
し溶剤中に光路を通過させる投光器及び該投光器
からの光路を受光し同受光量に基づき上記溶剤の
汚れ度をリアルタイムで連続的に検知する受光器
よりなる汚れ度検知器と、同受光器の検知結果に
基づいて溶剤流路に設けた弁をリアルタイムで連
続的に切替調整し、上記処理槽から排出される有
機溶剤の上記蒸留器への供給量並びに溶剤タンク
への戻し量をそれぞれ制御する蒸留量溶剤制御装
置とを具えたことにより、省エネルギを図り、冷
却水、溶剤等の無駄使いをなくする経済的なドラ
イクリーニングの溶剤回収制御装置を得るから、
本考案は産業上極めて有益なものである。 In short, according to the present invention, the organic solvent in the treatment tank during the cleaning process is introduced into the filter through a pump, the solvent is passed through, and the spent organic solvent is returned to the treatment tank again. a first solvent recovery circuit that is guided to the distiller by the pump, distills and recovers the solvent, and guides the recovered solvent to a clean tank; and a first solvent recovery circuit that is connected to the clean tank via an overflow partition plate and supplies the stored solvent to the pump;
In addition, the solvent tank that can receive the solvent from the processing tank and the fan, air cooler, and air heater installed in the recovery duct connected to the processing tank are activated to condense the solvent from the solvent gas generated from the processing tank. A large dry cleaning machine is equipped with a second solvent recovery circuit that collects the recovered solvent and guides the recovered solvent to the clean tank. Contamination consisting of a light projector that projects light onto the member near the member and passes the light path into the solvent, and a light receiver that receives the light path from the projector and continuously detects the degree of contamination of the solvent in real time based on the amount of light received. Based on the detection results of the temperature detector and the light receiver, the valves installed in the solvent flow path are continuously switched and adjusted in real time, and the amount of organic solvent discharged from the treatment tank is supplied to the distiller, as well as the amount of solvent By including a distillation amount solvent control device that controls the amount returned to the tank, an economical dry cleaning solvent recovery control device that saves energy and eliminates wasted use of cooling water, solvent, etc. is obtained. ,
The present invention is extremely useful industrially.
第1図は公知のドライクリーニング機械を示す
系統図、第2図は本考案の一実施例の溶剤汚れ度
検出装置を示す部分縦断面図である。
a……溶剤管路、b……透明チヤンバ、c……
ガスケツト、d……袋ナツト、e……受光器、f
……投光器。
FIG. 1 is a system diagram showing a known dry cleaning machine, and FIG. 2 is a partial vertical cross-sectional view showing a solvent stain level detection device according to an embodiment of the present invention. a... Solvent pipe line, b... Transparent chamber, c...
Gasket, d... Cap nut, e... Receiver, f
...Floodlight.
Claims (1)
てフイルターに導き同溶剤を過したのち再び該
処理槽に戻す循環回路と、上記処理槽からの使用
済有機溶剤を上記ポンプにより蒸溜器に導き溶剤
分を蒸溜回収し同回収溶剤をクリーンタンクに導
く第1の溶剤回収回路と、上記クリーンタンクに
オーバフロー仕切板を介して接続され貯溜溶剤を
上記ポンプに供給し、また上記処理槽の溶剤を受
入れることのできる溶剤タンクと、上記処理槽に
接続するリカバリダクト内に配設したフアン、エ
アクーラ、エアヒータをそれぞれ作動させ同処理
槽から発生する溶剤ガスから溶剤分を凝縮回収
し、同回収溶剤を上記クリーンタンクに導く第2
の溶剤回収回路とを備えてなる大型ドライクリー
ニング機において、該溶剤の流路あるいは収納タ
ンクに付設され一部を透明部材で形成し同透明部
材の近傍で同部材に投光し溶剤中に光路を通過さ
せる投光器及び該投光器からの光路を受光し同受
光量に基づき上記溶剤の汚れ度をリアルタイムで
連続的に検知する受光器よりなる汚れ度検知器
と、同受光器の検知結果に基づいて溶剤流路に設
けた弁をリアルタイムで連続的に切替調整し、上
記処理槽から排出される有機溶剤の上記蒸留器へ
の供給量並びに溶剤タンクへの戻し量をそれぞれ
制御する蒸留量溶剤制御装置とを具えたことを特
徴とする大型ドライクリーニング機の溶剤回収制
御装置。 During the cleaning process, the organic solvent in the treatment tank is guided to a filter via a pump, and the solvent is passed through, and then returned to the treatment tank again. The spent organic solvent from the treatment tank is guided to the distiller by the pump. a first solvent recovery circuit that distills and recovers the solvent and leads the recovered solvent to a clean tank; and a first solvent recovery circuit that is connected to the clean tank via an overflow partition plate, supplies the stored solvent to the pump, and supplies the solvent in the processing tank. The fans, air coolers, and air heaters installed in the solvent tank that can receive the solvent and the recovery duct connected to the processing tank are operated to condense and recover the solvent from the solvent gas generated from the processing tank, and the recovered solvent is recovered. The second one leads to the above clean tank.
In a large dry cleaning machine equipped with a solvent recovery circuit, a part of the solvent recovery circuit is attached to the solvent flow path or storage tank and is made of a transparent member, and light is projected onto the member near the transparent member to form an optical path into the solvent. a contamination degree detector consisting of a light emitter that transmits the light, and a light receiver that receives the light path from the light emitter and continuously detects the degree of contamination of the solvent in real time based on the amount of received light; A distillation amount solvent control device that continuously switches and adjusts a valve provided in a solvent flow path in real time to control the amount of organic solvent discharged from the treatment tank supplied to the distiller and the amount returned to the solvent tank. A solvent recovery control device for a large dry cleaning machine, characterized by comprising:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1981046465U JPH0121672Y2 (en) | 1981-04-02 | 1981-04-02 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1981046465U JPH0121672Y2 (en) | 1981-04-02 | 1981-04-02 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS57160651U JPS57160651U (en) | 1982-10-08 |
JPH0121672Y2 true JPH0121672Y2 (en) | 1989-06-27 |
Family
ID=29843310
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1981046465U Expired JPH0121672Y2 (en) | 1981-04-02 | 1981-04-02 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0121672Y2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4316983B2 (en) | 2003-10-29 | 2009-08-19 | 浩平 澤 | Dry cleaning method and apparatus |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5165685A (en) * | 1974-12-03 | 1976-06-07 | Mitsubishi Electric Corp | ODAKUDOKENSHUTSUSOCHI |
JPS5218071A (en) * | 1975-07-31 | 1977-02-10 | Sanyo Electric Co Ltd | Purifying device of dry cleaning solvent |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4919822U (en) * | 1972-05-27 | 1974-02-20 |
-
1981
- 1981-04-02 JP JP1981046465U patent/JPH0121672Y2/ja not_active Expired
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5165685A (en) * | 1974-12-03 | 1976-06-07 | Mitsubishi Electric Corp | ODAKUDOKENSHUTSUSOCHI |
JPS5218071A (en) * | 1975-07-31 | 1977-02-10 | Sanyo Electric Co Ltd | Purifying device of dry cleaning solvent |
Also Published As
Publication number | Publication date |
---|---|
JPS57160651U (en) | 1982-10-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4802253A (en) | Dry cleaning method using at least two kinds of solvents | |
EP0255421B1 (en) | Dry cleaning method and apparatus | |
US4520577A (en) | Cleaning apparatus | |
JPH0121672Y2 (en) | ||
ATE150812T1 (en) | METHOD AND DEVICE FOR CLEANING THE AIR EXHAUSTED FROM THE DRYER DRUM OF A DRYER | |
JP2001198394A (en) | Dry cleaning equipment and dry cleaning method | |
JP3202387B2 (en) | Dry cleaner turbidity detector | |
JPH0422811Y2 (en) | ||
JP2534606Y2 (en) | Distillation residue treatment equipment | |
JPS646794Y2 (en) | ||
JPH081753Y2 (en) | Distillation residue treatment equipment | |
JPS5818874Y2 (en) | dry cleaner | |
JP2868765B2 (en) | Dry cleaning machine | |
JPS5980301A (en) | Distillation apparatus | |
JPS6137435Y2 (en) | ||
JPH0722226Y2 (en) | Dry cleaner distiller | |
JPH0636838B2 (en) | Distillation temperature control method in dry cleaning | |
JP2761110B2 (en) | Dry cleaner odor removal method | |
JPH084954Y2 (en) | Distillation residue treatment equipment | |
JPS6329517Y2 (en) | ||
JPH0538394A (en) | Dry cleaning machine | |
JP2591153Y2 (en) | Dry cleaning machine | |
JPH0222680B2 (en) | ||
JPS6143434Y2 (en) | ||
JPH0246871Y2 (en) |