JP2526978Y2 - Wastewater treatment equipment for dry cleaning machines - Google Patents
Wastewater treatment equipment for dry cleaning machinesInfo
- Publication number
- JP2526978Y2 JP2526978Y2 JP1991102535U JP10253591U JP2526978Y2 JP 2526978 Y2 JP2526978 Y2 JP 2526978Y2 JP 1991102535 U JP1991102535 U JP 1991102535U JP 10253591 U JP10253591 U JP 10253591U JP 2526978 Y2 JP2526978 Y2 JP 2526978Y2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- waste water
- drainage
- solvent
- evaporation
- 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
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Physical Water Treatments (AREA)
Description
【0001】[0001]
【産業上の利用分野】この考案は、ドライクリーニング
機の排水をその排水中の溶剤と共に蒸発させるための排
水処理装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a wastewater treatment apparatus for evaporating wastewater from a dry cleaning machine together with a solvent contained in the wastewater.
【0002】[0002]
【従来の技術】ドライクリーニング機においては、衣類
の洗浄工程中、衣類に含まれた水が溶剤に混入するが、
この混入した水は、水分離器で溶剤と分離された後、排
水処理装置において処理される。2. Description of the Related Art In a dry cleaning machine, water contained in clothes is mixed into a solvent during a washing process of clothes.
The mixed water is separated from the solvent by a water separator and then treated in a wastewater treatment device.
【0003】このような排水処理装置として、排水が導
入される蒸発槽に、排水の蒸発用空気の吹出し口と排水
の加熱手段を設け、排水を蒸発させると共に、加熱によ
り排水温度を上昇させ、水を蒸発ガスとして次工程に放
出する構造が考えられている(例えば、本出願人が先に
提案した実願昭3−48561号)。As such a waste water treatment apparatus, the evaporation tank waste water is introduced, a heating means and drainage evaporation air outlet of the air drainage is provided, Rutotomoni evaporated drainage increases the drainage temperature by heating A structure has been considered in which water is released as evaporative gas to the next step (for example, Japanese Utility Model Application No. 3-48561 proposed earlier by the present applicant).
【0004】[0004]
【考案が解決しようとする課題】ところで、上記のよう
に排水の蒸発と排水加熱を併用した処理構造において
は、排水温度を高めると蒸発効率が上がるが、反面、排
水温度が水と溶剤の共沸点温度以上に上昇すると、共沸
現象のために蒸発ガスに含まれる溶剤濃度が著しく増大
する問題がある。By the way, in the treatment structure using both the evaporation of the wastewater and the heating of the wastewater as described above, the efficiency of the evaporation increases when the temperature of the wastewater is increased. When the temperature rises above the boiling point, there is a problem that the concentration of the solvent contained in the evaporative gas increases significantly due to the azeotropic phenomenon.
【0005】このように溶剤濃度が高い蒸発ガスは、次
に活性炭槽等に通して溶剤成分を吸着させても、溶剤を
完全に取除くことができず、外部へ放出されることによ
り公害問題を引き起こす不具合がある。[0005] Even if the evaporated gas having such a high solvent concentration is then passed through an activated carbon tank and the like to adsorb the solvent component, the solvent cannot be completely removed and is discharged to the outside. There is a problem that causes.
【0006】そこで、この考案は、上記の問題を解決
し、排水の蒸発と排水加熱を併用する構造において、蒸
発ガス中の溶剤濃度を低く抑えることができる処理装置
を提供することを目的としている。Accordingly, an object of the present invention is to solve the above-mentioned problem and to provide a processing apparatus capable of suppressing the concentration of a solvent in an evaporative gas to a low level in a structure in which evaporation of waste water and heating of waste water are used in combination. .
【0007】[0007]
【課題を解決するための手段】上記の課題を解決するた
め、この考案は、蒸発槽に溶剤から分離した排水の導入
通路を連結し、その蒸発槽の上部に排水の蒸発用空気の
吹出し口と蒸発ガスの排出口を設け、上記蒸発槽の下部
には排水の加熱手段と、排水温度を検出する温度検出器
とを設け、その温度検出器の検出信号により排水温度を
共沸点以下に加熱するように上記加熱手段の作動を制御
する制御手段を備えた構造としたのである。Means for Solving the Problems] To solve the above problems, this invention concatenates introduction passage of the waste water separated from SOLVENTS the evaporation tank, blowing evaporation air drainage on top of the evaporation tank the outlet of the mouth and the evaporation gas is provided, the temperature detector at the bottom of the evaporator tank for detecting the heating means of the drainage, the drainage temperature
And the temperature of waste water is determined by the detection signal of the temperature detector.
The structure is provided with a control means for controlling the operation of the heating means so as to heat it to an azeotropic point or lower .
【0008】[0008]
【作用】上記の構造においては、排水の温度を検出し、
排水温度が共沸点以下となるように加熱手段の作動を制
御する。このように加熱温度を低く制御することによ
り、共沸現象を防止でき、蒸発ガス中の溶剤濃度を減少
させることができる。In the above structure, the temperature of the waste water is detected,
The operation of the heating means is controlled so that the temperature of the waste water becomes lower than the azeotropic point. By controlling the heating temperature low in this way, an azeotropic phenomenon can be prevented, and the concentration of the solvent in the evaporated gas can be reduced.
【0009】排水を共沸点以下の一定温度範囲に加熱制
御するから、共沸点付近で溶剤が沸騰することはなく、
乾燥空気を排水表面に吹きかけて排水表面から一定の割
合で排水を蒸発させることにより排気中の溶剤濃度が絶
えず一定の低い割合となるように蒸発する。Since the wastewater is controlled to be heated to a certain temperature range below the azeotropic point, the solvent does not boil near the azeotropic point.
Dry air is blown onto the drainage surface to evaporate the wastewater at a constant rate from the drainage surface, thereby evaporating the solvent concentration in the exhaust gas so that the solvent concentration is constantly at a constant low rate.
【0010】[0010]
【実施例】図1は、実施例の排水処理装置を示してい
る。図において、1は蒸発槽、2はドライクリーニング
機の溶剤回収回路に設けられた水分離器であり、この水
分離器2の水タンク3と蒸発槽1との間に、ポンプ5を
備える排水導入通路4が連結されている。FIG. 1 shows a wastewater treatment apparatus according to an embodiment. In the figure, reference numeral 1 denotes an evaporating tank, 2 denotes a water separator provided in a solvent recovery circuit of a dry cleaning machine, and a drain having a pump 5 between the water tank 3 and the evaporating tank 1 of the water separator 2. The introduction passage 4 is connected.
【0011】蒸発槽1の上部には、排水の蒸発用の空気
が導入される空気吹出し口6と、蒸発ガスの排出口7が
設けられ、この排出口7に連結する排出通路8に、吸引
用ブロア9が設けられている。上記空気吹出し口6の下
方には、蒸気供給管10が接続するヒータ11が配置さ
れ、吹出し口6から吹出した空気を加熱して蒸発槽1内
に供給するようになっている。In the upper part of the evaporating tank 1, there are provided an air outlet 6 for introducing air for drainage evaporation and an outlet 7 for evaporative gas. Blower 9 is provided. A heater 11 connected to a steam supply pipe 10 is disposed below the air outlet 6 so as to heat the air blown out from the outlet 6 and supply the air into the evaporation tank 1.
【0012】また、蒸発槽1の下部には、導入された排
水を加熱するための加熱手段12が設けられている。こ
の加熱手段12は、加熱板13と、その下側に組込まれ
る蒸気管14とから成り、その蒸気管14に、蒸気供給
源(図示省略)と接続する蒸気供給通路15が電磁開閉
弁16を介して接続されている。A heating means 12 for heating the introduced waste water is provided below the evaporating tank 1. The heating means 12 comprises a heating plate 13 and a steam pipe 14 installed below the heating plate 13. A steam supply passage 15 connected to a steam supply source (not shown) has an electromagnetic on-off valve 16 in the steam pipe 14. Connected through.
【0013】また、蒸発槽1の下部には、貯留された排
水の温度を検出する温度検出器17が設けられ、その温
度検出器17が、上記電磁開閉弁16の開閉を制御する
制御器18に接続されている。この制御器18は、外部
から溶剤の種類に応じて共沸点温度を任意に入力できる
ようになっており、その共沸点温度と温度検出器17で
検出された排水温度とを比較し、排水温度が共沸点以下
の適当な温度を越えると電磁開閉弁16を閉じ、排水温
度が上記温度より一定値以上下がると電磁開閉弁16を
開くように設定されている。A temperature detector 17 for detecting the temperature of the stored waste water is provided below the evaporating tank 1, and the temperature detector 17 is a controller 18 for controlling the opening and closing of the electromagnetic on-off valve 16. It is connected to the. The controller 18 can arbitrarily input the azeotropic point temperature from the outside according to the type of the solvent. The controller 18 compares the azeotropic point temperature with the waste water temperature detected by the temperature detector 17, and calculates the waste water temperature. When the temperature exceeds a suitable temperature equal to or lower than the azeotropic point, the electromagnetic on-off valve 16 is closed, and when the drainage temperature falls below the above-mentioned temperature by a certain value or more, the electromagnetic on-off valve 16 is opened.
【0014】また、蒸発槽1の内部には、蒸発槽内を上
下に区分けする水平な隔離板19が設けられ、その隔離
板19の一端が排出口7の下方に臨んでいる。また、隔
離板19の他端には、その隔離板19に対して直角方向
に下方に延びる仕切板20が取付けられている。Further, inside the evaporating tank 1, a horizontal separating plate 19 for dividing the inside of the evaporating tank into upper and lower parts is provided, and one end of the separating plate 19 faces below the discharge port 7. At the other end of the separator 19, a partition plate 20 extending downward in a direction perpendicular to the separator 19 is attached.
【0015】この実施例は上記のような構造であり、排
水処理を行なう場合は、蒸発槽1内に、仕切板20と液
面との間に小さなすき間21ができる位置まで排水を導
入する。This embodiment has the above-described structure, and when performing drainage treatment, drainage is introduced into the evaporation tank 1 to a position where a small gap 21 is formed between the partition plate 20 and the liquid surface.
【0016】この状態で、吹出し口6より空気を導入す
ると共に、加熱手段12の蒸気管14に蒸気を供給す
る。吹出した空気は、ヒータ11で加熱された後、仕切
板20と液面の間のすき間21から隔離板19の内部に
吹出され、排水を蒸発させる。In this state, air is introduced from the outlet 6 and steam is supplied to the steam pipe 14 of the heating means 12. Blowing air, after being heated by the heater 11, blown out from the gap 21 between the partition plate 20 and the liquid level inside the separator 19, Ru evaporated drainage.
【0017】この排水の蒸発と、加熱手段12による加
熱により、排水の表面から蒸発ガスが発生し、その蒸発
ガスが隔離板19によって排出口7まで導かれ、外部に
放出される。[0017] and evaporation of the waste water, by applying <br/> heat Ru good to the heating means 12, vapor is generated from the surface of the waste water, the vapor is led to the discharge port 7 by the separator 19, to the outside Released.
【0018】上記の作動において、排水温度が上昇し、
水と溶剤の共沸点以下の適当な温度を越えようとする
と、温度検出器17からの信号により制御器18が電磁
開閉弁16を閉じ、加熱手段12への蒸気の供給を止め
る。逆に、排水温度が共沸点より一定値以上下がると、
制御器18が電磁開閉弁16を開放して蒸気が加熱手段
12に導入され、排水の加熱が再開されるこのため、排
水は、共沸点以下の一定の温度範囲で加熱かつ排水の蒸
発が行なわれることになり、共沸現象が防止され、安定
した蒸発効率を得ることができる。In the above operation, the temperature of the waste water rises,
When the temperature exceeds an appropriate temperature equal to or lower than the azeotropic point of water and the solvent, the controller 18 closes the electromagnetic on-off valve 16 by a signal from the temperature detector 17 and stops the supply of steam to the heating means 12. Conversely, when the temperature of the waste water falls below the azeotropic point by a certain value or more,
Controller 18 steam opens the solenoid valve 16 is introduced into the heating means 12, because this heating the waste water is restarted, drainage, heating and drainage at a constant temperature range of the azeotropic point vapor
Originating become Rukoto performed azeotropic phenomenon is prevented, it is possible to obtain a stable evaporation efficiency.
【0019】<実験例> 溶剤としてパークロロエチレン(共沸点;88℃)を使
用し、その溶剤から水分離器2において水を分離し、溶
剤(パークロロエチレン)濃度が200ppm以下の排
水を蒸発槽1に導入した。この状態で、排水温度を60
℃に保った状態で蒸発させた場合、排出口7における蒸
発ガス中の溶剤濃度は、2〜3ppmの範囲であった。<Experimental Example> Using perchlorethylene (azeotropic point; 88 ° C.) as a solvent, water was separated from the solvent in a water separator 2, and wastewater having a solvent (perchlorethylene) concentration of 200 ppm or less was evaporated. It was introduced into tank 1. In this state, the drain temperature is set to 60
When the solvent was evaporated while being kept at ° C, the concentration of the solvent in the evaporated gas at the outlet 7 was in the range of 2 to 3 ppm.
【0020】これに対して、上記と同じ排水を排水温度
90℃で蒸発させた場合、蒸発ガス中の溶剤濃度は、数
百〜数千ppmまで上昇した。On the other hand, when the same wastewater was evaporated at a wastewater temperature of 90 ° C., the concentration of the solvent in the evaporated gas increased to several hundred to several thousand ppm.
【0021】なお、上記の実施例では、蒸発槽1に活性
炭吸着槽等の溶剤吸着装置を取付けていないが、排水導
入通路4又は排出通路8に活性炭吸着槽を接続し、排出
される溶剤の総量を抑えるようにしてもよい。In the above embodiment, a solvent adsorption device such as an activated carbon adsorption tank is not installed in the evaporating tank 1, but an activated carbon adsorption tank is connected to the drainage introduction passage 4 or the discharge passage 8 so that the discharged solvent can be removed. The total amount may be suppressed.
【0022】また、排水の蒸発用空気を加熱するヒータ
11は、空気吹出し口6の内側に設けてもよい。The heater 11 for heating the evaporating air of the waste water may be provided inside the air outlet 6.
【0023】さらに、排水の加熱手段12は、図示した
蒸気加熱に限らず、電気加熱などの他の加熱方法を採用
することができる。Furthermore, the heating means 12 for the waste water is not limited to the steam heating shown in the figure, but may employ another heating method such as electric heating.
【0024】[0024]
【効果】以上のように、この考案は、排水の温度を検出
し、加熱による排水温度を一定に制御するようにしたの
で、共沸現象が防止され、蒸発ガスにおける溶剤濃度を
低く一定の割合で蒸発させることができ、環境性に優れ
た排水処理を行なうことができる。[Effect] As described above, the present invention detects the temperature of the waste water and controls the temperature of the waste water by heating to a constant value, so that the azeotropic phenomenon is prevented and the solvent concentration in the evaporative gas is reduced to a certain rate. And the wastewater can be treated with excellent environmental properties.
【図1】実施例の排水処理装置を示す概略図FIG. 1 is a schematic diagram showing a wastewater treatment apparatus according to an embodiment.
1 蒸発槽 4 排水導入通路 6 空気吹出し口 7 排出口 12 加熱手段 16 電磁開閉弁 17 温度検出器 18 制御器 DESCRIPTION OF SYMBOLS 1 Evaporation tank 4 Drainage introduction passage 6 Air outlet 7 Outlet 12 Heating means 16 Electromagnetic on-off valve 17 Temperature detector 18 Controller
Claims (1)
路を連結し、その蒸発槽の上部に排水の蒸発用空気の吹
出し口と蒸発ガスの排出口を設け、上記蒸発槽の下部に
は排水の加熱手段と、排水温度を検出する温度検出器と
を設け、その温度検出器の検出信号により排水温度を共
沸点以下に加熱するように上記排水の加熱手段の作動を
制御する制御手段を備えたドライクリーニング機の排水
処理装置。1. A connecting the introduction passage of the waste water separated from SOLVENTS the evaporation tank, provided the outlet and outlet of vapor evaporation air drainage on top of the evaporation tank, the lower portion of the evaporation tank
Co is a heating means of the drainage, the <br/> a temperature detector for detecting the effluent temperature is provided, a drainage temperature by the detection signal of the temperature detector
A waste water treatment apparatus for a dry cleaning machine, comprising: a control means for controlling the operation of the heating means for the waste water so as to heat the water to a temperature below the boiling point .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1991102535U JP2526978Y2 (en) | 1991-12-12 | 1991-12-12 | Wastewater treatment equipment for dry cleaning machines |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1991102535U JP2526978Y2 (en) | 1991-12-12 | 1991-12-12 | Wastewater treatment equipment for dry cleaning machines |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0551289U JPH0551289U (en) | 1993-07-09 |
JP2526978Y2 true JP2526978Y2 (en) | 1997-02-26 |
Family
ID=14329982
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1991102535U Expired - Lifetime JP2526978Y2 (en) | 1991-12-12 | 1991-12-12 | Wastewater treatment equipment for dry cleaning machines |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2526978Y2 (en) |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0710717Y2 (en) * | 1988-11-29 | 1995-03-15 | 三菱重工業株式会社 | Wastewater purification device |
-
1991
- 1991-12-12 JP JP1991102535U patent/JP2526978Y2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH0551289U (en) | 1993-07-09 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR101813360B1 (en) | Vapor supplying apparatus, vapor drying apparatus, vapor supplying method, and vapor drying method | |
JPH0568290B2 (en) | ||
US4281465A (en) | Method and apparatus for the recovering of solvents in dry cleaning units | |
JP2526978Y2 (en) | Wastewater treatment equipment for dry cleaning machines | |
EP0577563B1 (en) | Method and apparatus for the removal of residues of chlorinated solvent from contact waters formed during the drying stage in machines for the dry-cleaning of garments | |
JP4530472B2 (en) | Organic solvent recovery device and recovery method | |
JP3657425B2 (en) | Organic solvent recovery method and recovery device | |
JPH0729989Y2 (en) | Wastewater treatment equipment for dry cleaning machines | |
JP2005125252A (en) | Evaporative concentration method and evaporative concentration apparatus | |
JPH0422811Y2 (en) | ||
JPH0639834Y2 (en) | Wastewater purification device | |
JPS60236694A (en) | Drycleaner | |
JP2000018162A (en) | Oily water separator | |
JPH06198101A (en) | Evaporating concentrator | |
JP2955067B2 (en) | Operation control method for waste water treatment equipment discharged from desulfurization unit | |
JP3254025B2 (en) | Empty-fire prevention still | |
KR102253752B1 (en) | Apparatus for concentrating vacuum evaporation with stable maintenance of water level | |
JP5871308B2 (en) | Low boiling point solvent recovery method and apparatus | |
KR200169676Y1 (en) | Dryer for semiconductor wafer | |
KR100481030B1 (en) | Non-odor sludge drying system using closed system | |
JPH05192650A (en) | Treatment of processing waste liquid of nonsilver salt photosensitive material and treating device | |
JPH11649A (en) | Apparatus for treating oil-containing waste water | |
JPH0422810Y2 (en) | ||
KR0130727B1 (en) | Waste water treatment apparatus by aeration and ozone | |
JPS6239837Y2 (en) |