JPH0551289U - Wastewater treatment equipment for dry cleaning machines - Google Patents

Wastewater treatment equipment for dry cleaning machines

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Publication number
JPH0551289U
JPH0551289U JP10253591U JP10253591U JPH0551289U JP H0551289 U JPH0551289 U JP H0551289U JP 10253591 U JP10253591 U JP 10253591U JP 10253591 U JP10253591 U JP 10253591U JP H0551289 U JPH0551289 U JP H0551289U
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Japan
Prior art keywords
temperature
solvent
wastewater
heating
heating means
Prior art date
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Application number
JP10253591U
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JP2526978Y2 (en
Inventor
正樹 中井
Original Assignee
富士車輌株式会社
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Priority to JP1991102535U priority Critical patent/JP2526978Y2/en
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  • Physical Water Treatments (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

(57)【要約】 【目的】 溶剤から分離した排水を、ばっ気と加熱によ
って蒸発させる装置において、共沸現象を防止し、蒸発
ガス中の溶剤濃度を減少させる。 【構成】 蒸発槽1に、ばっ気用空気の吹出し口6と、
排水の加熱手段12を設け、その加熱手段12の作動を
制御する電磁開閉弁16に、温度検出器17を接続す
る。温度検出器17の信号により開閉弁16を開閉さ
せ、排水温度を共沸点以下に制御する。
(57) [Abstract] [Purpose] To prevent the azeotropic phenomenon and reduce the concentration of the solvent in the evaporated gas in a device that evaporates the wastewater separated from the solvent by aeration and heating. [Structure] In the evaporation tank 1, an outlet 6 for the air for aeration,
A drainage heating means 12 is provided, and a temperature detector 17 is connected to an electromagnetic opening / closing valve 16 for controlling the operation of the heating means 12. The open / close valve 16 is opened / closed by a signal from the temperature detector 17, and the drainage temperature is controlled to be equal to or lower than the azeotropic point.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】[Industrial applications]

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。 The present invention relates to a wastewater treatment device for evaporating the wastewater of a dry cleaning machine together with the solvent in the wastewater.

【0002】[0002]

【従来の技術】[Prior Art]

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。 In a dry cleaning machine, water contained in clothes is mixed with the solvent during the 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、ばっ気用空気の 吹出し口と排水の加熱手段を設け、排水をばっ気すると共に、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 wastewater treatment device, an evaporation tank into which wastewater is introduced is provided with an outlet for air for aeration and a heating means for the wastewater to aerate the wastewater and raise the temperature of the wastewater by heating. A structure in which water is discharged as evaporative gas to the next step is considered (eg, Japanese Patent Application No. 3-48561 previously proposed by the applicant).

【0004】[0004]

【考案が解決しようとする課題】[Problems to be solved by the device]

ところで、上記のようにばっ気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 that uses both aeration and wastewater heating as described above, evaporating efficiency increases when the wastewater temperature is raised, but on the other hand, when the wastewater temperature rises above the azeotropic temperature of water and solvent, azeotropic Due to the phenomenon, there is a problem that the concentration of the solvent contained in the evaporated gas remarkably increases.

【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。The evaporative gas having such a high solvent concentration cannot completely remove the solvent even if it is then passed through an activated carbon tank or the like to adsorb the solvent component and is released to the outside. There are defects that cause harm problems.

【0006】 そこで、この考案は、上記の問題を解決し、ばっ気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。Therefore, an object of the present invention is to solve the above-mentioned problems and to provide a treatment apparatus capable of suppressing the solvent concentration in evaporative gas to a low level in a structure in which aeration and drainage heating are used together.

【0007】[0007]

【課題を解決するための手段】[Means for Solving the Problems]

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、ばっ気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、排水の加熱手段と排水温度を検出する温度 検出器を設け、その温度検出器の検出信号により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。 In order to solve the above-mentioned problems, the present invention connects an evaporation tank with a passage for introducing wastewater separated from a solvent, and provides an outlet for aeration air and an outlet for evaporated gas at the upper part of the evaporation tank. In the lower part of the evaporation tank, a means for heating waste water and a temperature detector for detecting the waste water temperature are provided, and a control means for controlling the operation of the heating means by a detection signal of the temperature detector is provided. ..

【0008】[0008]

【作用】[Action]

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 waste water is detected and the operation of the heating means is controlled so that the waste water temperature becomes equal to or lower than the azeotropic point. By controlling the heating temperature to be low in this way, the azeotropic phenomenon can be prevented and the concentration of the solvent in the evaporative gas can be reduced.

【0009】[0009]

【実施例】【Example】

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 of the embodiment. In the figure, 1 is an evaporating tank, 2 is a water separator provided in a solvent recovery circuit of a dry cleaning machine, and a drainage equipped with a pump 5 between a water tank 3 of this water separator 2 and the evaporating tank 1. The introduction passage 4 is connected.

【0010】 蒸発槽1の上部には、ばっ気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。At the upper part of the evaporation tank 1, an air outlet 6 for introducing air for aeration and an outlet 7 for the evaporation gas are provided, and a suction passage 8 connected to this outlet 7 is sucked into the suction passage 8. Blower 9 is provided. A heater 11 to which a steam supply pipe 10 is connected is arranged below the air outlet 6 to heat the air blown from the outlet 6 and supply it to the evaporation tank 1.

【0011】 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。Further, a heating means 12 for heating the introduced waste water is provided below the evaporation tank 1. This heating means 12 is composed of a heating plate 13 and a steam pipe 14 installed below the heating plate 13, and a steam supply passage 15 connected to a steam supply source (not shown) is connected to the steam pipe 14 by means of an electromagnetic opening / closing valve 16. Connected through.

【0012】 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 evaporation tank 1, and the temperature detector 17 controls the opening / closing of the electromagnetic opening / closing valve 16. It is connected to the. The controller 18 is designed so that the azeotropic point temperature can be arbitrarily input from the outside according to the type of solvent, and the azeotropic point temperature is compared with the wastewater temperature detected by the temperature detector 17, The electromagnetic on-off valve 16 is closed when the temperature exceeds an appropriate temperature below the azeotropic point, and the electromagnetic on-off valve 16 is opened when the drainage temperature falls below the above temperature by a certain value or more.

【0013】 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 evaporation tank 1, a horizontal separator plate 19 that divides the inside of the evaporation tank into upper and lower parts is provided, and one end of the separator plate 19 faces below the discharge port 7. A partition plate 20 is attached to the other end of the separator plate 19 and extends downward in a direction perpendicular to the separator plate 19.

【0014】 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 wastewater treatment, the wastewater 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. ..

【0015】 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1 4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、排水をばっ気する。In this state, air is introduced from the outlet 6 and steam is supplied to the steam pipe 14 of the heating means 12. The blown air is heated by the heater 11 and then blown into the inside of the separating plate 19 from the gap 21 between the partition plate 20 and the liquid surface to aeration the drainage.

【0016】 このばっ気と、加熱手段12により加熱により、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 。By this aeration and heating by the heating means 12, evaporative gas is generated from the surface of the drainage, and the evaporative gas is guided to the outlet 7 by the separator plate 19 and is discharged to the outside.

【0017】 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とばっ気を受けること 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-mentioned operation, when the temperature of the waste water rises and the temperature exceeds an appropriate temperature below 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, The supply of steam to the heating means 12 is stopped. On the contrary, when the drainage temperature falls below the azeotropic point by a certain value or more, the controller 18 opens the electromagnetic opening / closing valve 16 to introduce the steam into the heating means 12 and restart the heating of the drainage. Since it is heated and aerated in a certain temperature range below the azeotropic point, the azeotropic phenomenon is prevented and stable evaporation efficiency can be obtained.

【0018】 <実験例> 溶剤としてパークロロエチレン(共沸点;65℃)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 でばっ気させた場合、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> Perchlorethylene (azeotropic point: 65 ° C.) is used as a solvent, water is separated from the solvent in a water separator 2, and wastewater having a solvent (perchloroethylene) concentration of 200 ppm or less is evaporated. It was introduced into tank 1. In this state, when aeration was performed while keeping the drainage temperature at 60 ° C., the solvent concentration in the evaporative gas at the outlet 7 was in the range of 2 to 3 ppm.

【0019】 これに対して、上記と同じ排水を排水温度90℃でばっ気させた場合、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 waste water as the above was aerated at a waste water temperature of 90 ° C., the solvent concentration in the evaporation gas increased to several hundreds to several thousands ppm.

【0020】 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-mentioned embodiment, the solvent adsorption device such as the activated carbon adsorption tank is not attached to the evaporation tank 1, but the activated carbon adsorption tank is connected to the drainage introduction passage 4 or the discharge passage 8 to remove the solvent discharged. The total amount may be suppressed.

【0021】 また、ばっ気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。Further, the heater 11 for heating the aeration air may be provided inside the air outlet 6.

【0022】 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。Further, the wastewater heating means 12 is not limited to the steam heating shown in the figure, but other heating methods such as electric heating can be adopted.

【0023】[0023]

【効果】【effect】

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 低くすることができ、環境性に優れた排水処理を行なうことができる。 As described above, according to the present invention, the temperature of waste water is detected and the waste water temperature due to heating is controlled to be constant, so that the azeotropic phenomenon is prevented, the solvent concentration in the evaporative gas can be lowered, and the environment can be reduced. Efficient wastewater treatment can be performed.

【図面の簡単な説明】[Brief description of drawings]

【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 device of an embodiment.

【符号の説明】[Explanation of symbols]

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 Discharge port 12 Heating means 16 Electromagnetic on-off valve 17 Temperature detector 18 Controller

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 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、ばっ気用空気の吹
出し口と蒸発ガスの排出口を設け、上記蒸発槽の下部
に、排水の加熱手段と排水温度を検出する温度検出器を
設け、その温度検出器の検出信号により上記加熱手段の
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. An evaporating tank is connected to a passage for introducing wastewater separated from a solvent, and an outlet for aeration air and an outlet for evaporating gas are provided at the upper part of the evaporating tank, and at the lower part of the evaporating tank. A wastewater treatment apparatus for a dry cleaning machine, comprising a heating means for wastewater and a temperature detector for detecting the temperature of wastewater, and a control means for controlling the operation of the heating means according to a detection signal of the temperature detector.
JP1991102535U 1991-12-12 1991-12-12 Wastewater treatment equipment for dry cleaning machines Expired - Lifetime JP2526978Y2 (en)

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 true JPH0551289U (en) 1993-07-09
JP2526978Y2 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)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02122683U (en) * 1988-11-29 1990-10-08

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02122683U (en) * 1988-11-29 1990-10-08

Also Published As

Publication number Publication date
JP2526978Y2 (en) 1997-02-26

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