JPH08160B2 - Method of decomposing and removing dry cleaning solvent using ultrasonic waves - Google Patents
Method of decomposing and removing dry cleaning solvent using ultrasonic wavesInfo
- Publication number
- JPH08160B2 JPH08160B2 JP5279554A JP27955493A JPH08160B2 JP H08160 B2 JPH08160 B2 JP H08160B2 JP 5279554 A JP5279554 A JP 5279554A JP 27955493 A JP27955493 A JP 27955493A JP H08160 B2 JPH08160 B2 JP H08160B2
- Authority
- JP
- Japan
- Prior art keywords
- dry cleaning
- solvent
- ultrasonic waves
- decomposing
- water
- 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 - Lifetime
Links
- 239000002904 solvent Substances 0.000 title claims description 30
- 238000000034 method Methods 0.000 title claims description 12
- 238000005108 dry cleaning Methods 0.000 title claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 6
- 239000000460 chlorine Substances 0.000 claims description 6
- 229910052801 chlorine Inorganic materials 0.000 claims description 6
- CYTYCFOTNPOANT-UHFFFAOYSA-N Perchloroethylene Chemical group ClC(Cl)=C(Cl)Cl CYTYCFOTNPOANT-UHFFFAOYSA-N 0.000 claims description 5
- 229950011008 tetrachloroethylene Drugs 0.000 claims description 5
- 239000007864 aqueous solution Substances 0.000 claims description 4
- AJDIZQLSFPQPEY-UHFFFAOYSA-N 1,1,2-Trichlorotrifluoroethane Chemical compound FC(F)(Cl)C(F)(Cl)Cl AJDIZQLSFPQPEY-UHFFFAOYSA-N 0.000 claims description 3
- 238000000354 decomposition reaction Methods 0.000 claims description 3
- 230000001678 irradiating effect Effects 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 2
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 claims 1
- 238000001704 evaporation Methods 0.000 claims 1
- UBOXGVDOUJQMTN-UHFFFAOYSA-N trichloroethylene Natural products ClCC(Cl)Cl UBOXGVDOUJQMTN-UHFFFAOYSA-N 0.000 claims 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 5
- 239000002351 wastewater Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 239000000839 emulsion Substances 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- -1 trichloroethylene, tetrachloroethylene, 1.1.1-trichloroethane Chemical class 0.000 description 4
- 239000004094 surface-active agent Substances 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 150000004045 organic chlorine compounds Chemical class 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 238000003895 groundwater pollution Methods 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Accessory Of Washing/Drying Machine, Commercial Washing/Drying Machine, Other Washing/Drying Machine (AREA)
- Cleaning By Liquid Or Steam (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は超音波を利用したドライ
クリーニング溶剤の分解除去方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for decomposing and removing a dry cleaning solvent using ultrasonic waves.
【0002】[0002]
【従来の技術】従来よりドライクリーニングには不燃性
溶剤として、トリクロロエチレンやテトラクロロエチレ
ン、1.1.1-トリクロロエタン、フロン-113、その他の塩
素系溶剤が使われ、さらに石油系溶剤も使われている。
これら溶剤はドライクリーニング後の蒸留器によって被
洗物に含まれる水分等と共沸して気化させ、コンデンサ
で冷却し、セパレータによる比重差で分離される。2. Description of the Related Art Conventionally, non-flammable solvents such as trichloroethylene, tetrachloroethylene, 1.1.1-trichloroethane, CFC-113 and other chlorine-based solvents have been used for dry cleaning, and petroleum-based solvents have also been used.
These solvents are azeotropically vaporized with water and the like contained in the object to be washed by a distiller after dry cleaning, cooled by a condenser, and separated by a specific gravity difference by a separator.
【0003】[0003]
【発明が解決しようとする課題】しかし、上記のように
分離後、排出される水分中に50ppm〜100ppm
程度の溶剤が含まれていることもあり、公害上の問題が
生じる。ドライクリーニング用の洗剤中には界面活性剤
やアルコール類も包含されており、上記蒸留器による水
との共沸時に水分、水分と界面活性剤と溶剤との混合エ
マルジョン、テトラクロロエチレン、1.1.1-トリクロロ
エタン、フロン等の3層に分離されたり、石油系溶剤、
水分と界面活性剤と溶剤の混合エマルジョン及び水分の
3層に分離されることもある。However, in the water discharged after the separation as described above, 50 ppm to 100 ppm is contained.
Since some solvents are included, pollution problems occur. Surfactants and alcohols are also included in the detergent for dry cleaning, and water is azeotropically distilled with water by the distiller, a mixed emulsion of water, a surfactant and a solvent, tetrachloroethylene, 1.1.1- It is separated into three layers such as trichloroethane and freon, petroleum solvent,
It may be separated into a mixed emulsion of water, a surfactant and a solvent, and three layers of water.
【0004】従って、これら3層の分離後に排水した
時、前記混合エマルジョンが一部流入すると排水中に1
20ppm〜200ppm程度の溶剤が混合され、下水
道に流出することになる。さらに、蒸留器の使用時にバ
ルブの操作ミスや急加熱、清掃不良等を原因とした突沸
現象が生じることになると、1000ppm〜1200
ppm以上の溶剤が混合して排水中に含まれることとな
る。その結果、排水の地下浸透から地下水汚染が生じ、
ひいては河川汚染の原因ともなる問題点がみられた。Therefore, when the mixed emulsion is partially drained after draining after the separation of these three layers, 1
Solvents of about 20 ppm to 200 ppm are mixed and discharged into the sewer. Furthermore, when a bumping phenomenon occurs due to a valve operation error, rapid heating, poor cleaning, etc., when using a distiller, 1000 ppm to 1200 ppm
Solvents above ppm will be mixed and contained in the wastewater. As a result, groundwater pollution occurs from the infiltration of wastewater,
Eventually, there were problems that could cause river pollution.
【0005】上記のような溶剤を含む排水を環境庁告示
の0.01ppmに抑えるために種々の方法が検討され
ている。例えば、活性炭層を通過させる方法があるが、
この方法では活性炭による吸着がすぐ飽和状態となる
他、溶剤を含む活性炭の処分が問題となる。また、水と
溶剤との比重差を利用した遠心分離方法では、0.01
ppm以下にすることが難しく、特にエマルジョン層や
突沸現象による排水中の溶剤の分離には効果が認められ
ない難点がある。Various methods have been studied in order to suppress the waste water containing the solvent as described above to 0.01 ppm as announced by the Environmental Agency. For example, there is a method of passing through an activated carbon layer,
In this method, adsorption by activated carbon becomes saturated immediately, and disposal of activated carbon containing a solvent becomes a problem. Further, in the centrifugal separation method utilizing the difference in specific gravity between water and solvent, 0.01
It is difficult to reduce the amount to ppm or less, and there is a drawback that the effect is not recognized particularly in the separation of the solvent in the wastewater due to the emulsion layer or the bumping phenomenon.
【0006】さらに、曝気法としてエアーを吹き込み大
気中に拡散する手段では、環境指針の34ppbの値を
クリヤーすることができず、溶剤臭や脂肪酸分解臭等が
発生するという問題点がみられた。また、煮沸法とし
て、蒸気を送り、加熱し、水蒸気と一緒に溶剤を気化さ
せ、大気に放出する方法もあるが、スチームボイラーを
必要とし、塩素系溶剤の加水、加熱分解が生じ、釜や排
気パイプの腐食及び悪臭の拡散が生じる等の難点があ
る。Further, the aeration method, in which air is blown in and diffused into the atmosphere, cannot clear the value of 34 ppb in the environmental guideline, resulting in a problem that a solvent odor or a fatty acid decomposition odor is generated. . Also, as a boiling method, there is also a method of sending steam, heating, vaporizing the solvent together with water vapor, and releasing it to the atmosphere, but it requires a steam boiler, watering of the chlorine-based solvent, thermal decomposition occurs, and a kettle or There are problems such as corrosion of exhaust pipes and diffusion of malodors.
【0007】本発明の目的は上記のような種々の方法と
は異なり、超音波による溶剤の分解、除去方法を提供し
ようとするものである。An object of the present invention is to provide a method for decomposing and removing a solvent by ultrasonic waves, unlike the above-mentioned various methods.
【0008】[0008]
【課題を解決するための手段】上記目的を達成するため
本発明は、ドライクリーニング後の水を含む溶剤を、蒸
留器により共沸して気化し、コンデンサで冷却し、セパ
レータで分離して得たテトラクロロエチレン、パークロ
ロエチレン、トリクロロエチレン、1.1.1-トリクロロエ
タン、フロン-113等の塩素系溶剤を含む水溶液に対し、
高出力の超音波を照射し振動させることにより分解し除
去する超音波を利用したドライクリーニング溶剤の分解
除去方法とした。In order to achieve the above object, the present invention is obtained by azeotropically vaporizing a solvent containing water after dry cleaning with a distiller, cooling with a condenser, and separating with a separator. For an aqueous solution containing a chlorine-based solvent such as tetrachloroethylene, perchloroethylene, trichloroethylene, 1.1.1-trichloroethane, CFC-113,
A method for decomposing and removing a dry cleaning solvent using ultrasonic waves, which decomposes and removes by irradiating and vibrating a high-power ultrasonic wave.
【0009】[0009]
【作用】ドライクリーニング後の水を含む溶剤を、蒸留
器により共沸して気化し、コンデンサで冷却し、セパレ
ータで分離した後、水溶液中に含まれるテトラクロロエ
チレン、トリクロロエチレン、1.1.1-トリクロロエタ
ン、フロン-113のような有機塩素化合物に対して、超音
波を照射することにより、キャビテーションバブルが生
成され、このバブルの崩壊時に高温高圧状態となって塩
酸、炭酸ガス等に分解されることが判明した。[Function] After the dry cleaning, the solvent containing water is azeotropically vaporized by a distiller, cooled by a condenser, separated by a separator, and then tetrachloroethylene, trichlorethylene, 1.1.1-trichloroethane and freon contained in the aqueous solution. It was found that by irradiating an organic chlorine compound such as -113 with ultrasonic waves, a cavitation bubble is generated, and when this bubble collapses, it becomes a high temperature and high pressure state and decomposes into hydrochloric acid, carbon dioxide gas, etc. .
【0010】[0010]
【実施例】テトラクロロエチレン含有水の超音波照射に
よる分解を行なった実験値を示すと、下表の通りであ
る。 水20リットル テトラクロロエチレン 20cc(濃度1125pp
m) 同溶剤用ソープ 2cc 上記混合水溶液を超音波27KHz、出力250wで1
50分照射し振動させた時のpH値を測定した。[Examples] The following table shows experimental values obtained by decomposing tetrachloroethylene-containing water by ultrasonic irradiation. Water 20 liters Tetrachlorethylene 20cc (concentration 1125pp
m) Soap for the same solvent 2 cc The above mixed aqueous solution is ultrasonic 27 KHz, output 250w 1
The pH value was measured after irradiation for 50 minutes and vibration.
【0011】pH値が当初6.37あったものが、60
分後には3.96、120分後には3.74となったこ
とは、反応時間の経過と共に塩化物イオンの濃度が上昇
してpH値の低下が生じ塩化水素の生成があったものと
考えられる。The initial pH value of 6.37 was 60.
It was 3.96 after minutes and 3.74 after 120 minutes, which suggests that the concentration of chloride ions increased and the pH value decreased with the passage of reaction time, resulting in the generation of hydrogen chloride. To be
【0012】[0012]
【表1】 [Table 1]
【0013】有機塩素化合物として、テトラクロロエチ
レン、トリクロロエチレン、1.1.1-トリクロロエタン等
を用い、周波数200KHz、出力200wで同様の実
験をしたところ、30分の照射によりテトラクロロエチ
レンでは分解率77.0%、トリクロロエチレンでは、
53.7%、1.1.1-トリクロロエタンでは71.5%の
分解が得られた。As the organic chlorine compound, tetrachloroethylene, trichloroethylene, 1.1.1-trichloroethane, etc. were used, and a similar experiment was conducted at a frequency of 200 KHz and an output of 200 w. ,
Decomposition of 53.7% and 71.5% with 1.1.1-trichloroethane was obtained.
【0014】なお、高出力としては20〜600KHz
程度のものが塩素系溶剤の分解に適当である。As a high output, 20 to 600 KHz
Some of them are suitable for decomposing chlorine solvents.
【0015】[0015]
【発明の効果】本発明のようにドライクリーニングに使
用される塩素系溶剤が超音波による照射により塩酸、炭
酸ガス等に分解することができ、排水中に包含した状態
でも公害問題等が生じないようになった。EFFECTS OF THE INVENTION The chlorine-based solvent used for dry cleaning as in the present invention can be decomposed into hydrochloric acid, carbon dioxide gas, etc. by irradiation with ultrasonic waves, and no pollution problem occurs even when it is contained in waste water. It became so.
Claims (1)
を、蒸留器により共沸して気化し、コンデンサで冷却
し、セパレータで分離して得たテトラクロロエチレン、
パークロロエチレン、トリクロロエチレン、1.1.1-トリ
クロロエタン、フロン-113等の塩素系溶剤を含む水溶液
に対し、高出力の超音波を照射し振動させることにより
分解し除去することを特徴とする超音波を利用したドラ
イクリーニング溶剤の分解除去方法。1. Tetrachloroethylene obtained by azeotropically evaporating a solvent containing water after dry cleaning with a distiller, cooling with a condenser, and separating with a separator,
Ultrasonic waves characterized by being decomposed and removed by irradiating and vibrating a high-power ultrasonic wave to an aqueous solution containing a chlorine-based solvent such as perchlorethylene, trichloroethylene, 1.1.1-trichloroethane, and Freon-113. Decomposition and removal method of dry cleaning solvent used.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5279554A JPH08160B2 (en) | 1993-11-09 | 1993-11-09 | Method of decomposing and removing dry cleaning solvent using ultrasonic waves |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5279554A JPH08160B2 (en) | 1993-11-09 | 1993-11-09 | Method of decomposing and removing dry cleaning solvent using ultrasonic waves |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH07132195A JPH07132195A (en) | 1995-05-23 |
| JPH08160B2 true JPH08160B2 (en) | 1996-01-10 |
Family
ID=17612588
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5279554A Expired - Lifetime JPH08160B2 (en) | 1993-11-09 | 1993-11-09 | Method of decomposing and removing dry cleaning solvent using ultrasonic waves |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH08160B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006035217A (en) * | 2005-08-17 | 2006-02-09 | Daio Kensetsu Kk | Method for accelerating reaction of chemical substance utilizing ultrasonic wave |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2813451B2 (en) * | 1990-10-29 | 1998-10-22 | 三菱重工業株式会社 | Dry cleaner wastewater treatment method |
-
1993
- 1993-11-09 JP JP5279554A patent/JPH08160B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH07132195A (en) | 1995-05-23 |
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