JPH0275387A - Apparatus for treating waste water containing surfactant - Google Patents

Apparatus for treating waste water containing surfactant

Info

Publication number
JPH0275387A
JPH0275387A JP22466988A JP22466988A JPH0275387A JP H0275387 A JPH0275387 A JP H0275387A JP 22466988 A JP22466988 A JP 22466988A JP 22466988 A JP22466988 A JP 22466988A JP H0275387 A JPH0275387 A JP H0275387A
Authority
JP
Japan
Prior art keywords
liquid
membrane
surfactant
treated
foam
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.)
Pending
Application number
JP22466988A
Other languages
Japanese (ja)
Inventor
Tetsuo Yamaguchi
哲男 山口
Toshio Sawa
俊雄 沢
Shin Tamada
玉田 慎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
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 by Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP22466988A priority Critical patent/JPH0275387A/en
Publication of JPH0275387A publication Critical patent/JPH0275387A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To prevent the leakage of a liquid from a membrane by eliminating a lowering of the surface tension of a liquid to be treated at a membrane part, in an apparatus for treating waste water containing a surfactant and salts, by independently removing the surfactant in an air bubble separator and subsequently treating the treated liquid in a membrane evaporation/concn. apparatus. CONSTITUTION:A liquid to be treated containing a surfactant enters a foam separator 1 to generate foam by the air bubbles blown in said liquid from the bottom part of the foam separator and the foam is accumulated in the upper part of the separator 1. The surfactant in the liquid to be treated is conc. in the foam to be discharged and removed from a conduit 10. The liquid to be treated from which the surfactant is removed in the foam separator 1 is drawn out of a liquid discharge pipe 7 to be heated to predetermined temp. in a heating tank 12 and supplied to the evaporation chamber of a membrane evaporation/conc. apparatus 2 by a pump 14 to be recirculated. Cooling water is supplied and recirculated to the cooling chamber of the membrane evaporation/concn. apparatus from a cooling water tank 15. The steam generated from the evaporation chamber of the membrane evaporation/concn. apparatus 2 is passed through a hydrophobic porous membrane 23 and condensed on a cooling wall to be capable of being recovered as pure water.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、界面活性剤及び塩類を含む水溶液を蒸発濃縮
し、かつ、純度の高い水を得る蒸発濃縮装置、とくに蒸
発面に膜を用いた膜蒸発濃縮装置を組込ん・・だ廃水処
理装置に関する。
Detailed Description of the Invention [Industrial Application Field] The present invention is an evaporative concentration device for evaporating and concentrating an aqueous solution containing a surfactant and salts and obtaining highly pure water, in particular, an evaporative concentration device that uses a membrane on the evaporation surface. The present invention relates to wastewater treatment equipment that incorporates membrane evaporation concentration equipment.

〔従来の技術〕[Conventional technology]

蒸気は通過させるが液体は通過させない性質をもつ疎水
性多孔質膜を蒸発面に用いた膜蒸発濃縮装置2は、塩溶
液からの純水の回収、あるいは、塩溶液自体の濃縮など
への利用が考えられており、既に知られている。第3図
に示すように、膜蒸発濃縮装置は、例えば、特公昭49
−45461号公報に開示されるように、蒸発室20、
凝縮室21及び冷却室22からなり、蒸発室20は疎水
性多孔質膜23で隔離されており、膜壁に相対して空間
を隔てて冷却壁24が設けている。
The membrane evaporation concentrator 2, which uses a hydrophobic porous membrane on the evaporation surface that allows vapor to pass through but not liquid, can be used for recovering pure water from salt solutions or concentrating the salt solution itself. has been considered and is already known. As shown in FIG. 3, the membrane evaporation concentration device is, for example,
As disclosed in Publication No. 45461, an evaporation chamber 20,
It consists of a condensation chamber 21 and a cooling chamber 22, and the evaporation chamber 20 is separated by a hydrophobic porous membrane 23, and a cooling wall 24 is provided opposite to the membrane wall with a space between them.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

ところで、膜蒸発濃縮装置2は、蒸発面+’−疎水性多
孔質膜23を用いていため、被処理液に界面活性剤が含
まれると被処理液の表面張力を低下させるため、膜から
液が漏洩し、その機能を果さないという問題があった。
By the way, since the membrane evaporation concentration device 2 uses the evaporation surface +'-hydrophobic porous membrane 23, if a surfactant is contained in the liquid to be treated, the surface tension of the liquid to be treated will be lowered, so the liquid will be removed from the membrane. There was a problem that the information was leaked and it did not perform its function.

本発明の目的は界面活性剤を含有する廃水を処理可能な
膜蒸発濃縮装置を組込んだ廃水処理装置を提供すること
にある。
An object of the present invention is to provide a wastewater treatment device incorporating a membrane evaporation concentration device capable of treating wastewater containing surfactants.

〔課題を解決するための手段〕[Means to solve the problem]

上記目的は、界面活性剤及び塩類を含む廃水の処理装置
において、まず、気泡分離装置で界面活性剤を除去処理
し、次いで、処理液を膜蒸発濃縮装置で処理することに
より達成される。
The above object is achieved by, in a wastewater treatment apparatus containing surfactants and salts, first removing the surfactant using a bubble separator and then treating the treated liquid using a membrane evaporation concentrator.

〔作用〕[Effect]

本発明の界面活性剤及び塩類を含有する廃水の処理装置
は、まず、泡末分離装置1に導入された被処理液中に気
泡を吹込み界面活性剤を泡末にして廃水の上部に移動す
る。廃水液面に滞留した泡沫を分離すれば廃水中から界
面活性剤を除去できる0次いで、被処理液を膜蒸発濃縮
装置2で処理することにより、塩分を濃縮し、かつ、純
水を回収することができる。
The wastewater treatment device containing surfactants and salts of the present invention firstly blows air bubbles into the liquid to be treated introduced into the foam separator 1 to turn the surfactant into foam and move it to the upper part of the wastewater. do. The surfactant can be removed from the wastewater by separating the foam accumulated on the wastewater surface.Next, by treating the liquid to be treated with the membrane evaporation concentrator 2, the salt content is concentrated and pure water is recovered. be able to.

ところで、界面活性剤を含有した水溶液をそのまま膜蒸
発濃縮装置で処理すると、膜蒸発濃縮装置に用いられた
疎水性多孔質膜から被処理液が漏洩し、その機能を果さ
ない。これは、界面活性剤を含有した水溶液は水溶液の
表面張力が小さくなり、膜の耐水圧を低下させるためで
ある。しかし。
By the way, if an aqueous solution containing a surfactant is treated as it is in a membrane evaporation concentrator, the liquid to be treated will leak from the hydrophobic porous membrane used in the membrane evaporation concentrator, and the device will not perform its function. This is because an aqueous solution containing a surfactant has a lower surface tension, which lowers the water pressure resistance of the membrane. but.

膜の耐水圧は水溶液の表面張力の値により一義的に決ま
らない。すなわち、第2図に示すように。
The water pressure resistance of a membrane is not uniquely determined by the value of the surface tension of the aqueous solution. That is, as shown in FIG.

同じ膜を用いてくり返えして耐水圧を測定すると、その
値を低下する。例えば、界面活性剤のドデシルベンゼン
スルホン酸ナトリウムを35ppm含有した水溶液は表
面張力が47 dyne/ aiであるが、第一回目の
耐水圧は0.94 kg/dであるのに対して、同じ膜
を用いくり返し耐水圧を測定すると四、五回目には0 
、1 kg / aJ程度に低下する。これに対し、純
水は表面張カフ 3 dyne/ cnであり。
If the water pressure resistance is measured repeatedly using the same membrane, the value will decrease. For example, an aqueous solution containing 35 ppm of the surfactant sodium dodecylbenzenesulfonate has a surface tension of 47 dyne/ai, but the water pressure resistance after the first application is 0.94 kg/d, whereas the same membrane When the water pressure is repeatedly measured using
, decreases to about 1 kg/aJ. In contrast, pure water has a surface tension of 3 dyne/cn.

第一回目の耐水圧は1.2kg/fflであり同じ膜を
用い、くり返し耐水圧を測定してで0.85kg/−と
その低下度合は小さい。これは界面活性剤を含有してい
る水溶液は界面活性剤が膜に付着するためにくり返えし
測定の耐水圧が低下するものである。従って、界面活性
剤を含有している水溶液を膜蒸発濃縮装置で処理するに
は、界面活性剤の除去が必要である。
The water pressure resistance at the first time was 1.2 kg/ffl, and when the water pressure resistance was repeatedly measured using the same membrane, it was 0.85 kg/-, which is a small degree of decrease. This is because in an aqueous solution containing a surfactant, the surfactant adheres to the membrane, resulting in a decrease in water pressure resistance when repeatedly measured. Therefore, in order to treat an aqueous solution containing a surfactant in a membrane evaporation concentrator, it is necessary to remove the surfactant.

そこで、界面活性剤を含有している水溶液を泡沫分離装
置で処理し、その残液をくり返えし耐水圧を測定したと
ころ、純水と同じ値となり泡沫分離装置により界面活性
剤の除去ができ、その処理残液は純水と同程度の耐水圧
が得られることを確認した。
Therefore, when an aqueous solution containing a surfactant was treated with a foam separator and the residual liquid was repeatedly measured for water pressure resistance, the value was the same as that of pure water, and the surfactant was removed by the foam separator. It was confirmed that the treated residual liquid had a water pressure resistance comparable to that of pure water.

〔実施例〕〔Example〕

以下、図面を参照して本発明の一実施例を説明する。第
1図は本発明の界面活性剤が塩類を含む廃水の処理装置
を示す。本装置は、被処理液中から界面活性剤を除去す
る泡沫分離装[1、膜蒸発濃縮装置2、被処理液を加熱
循環する系3、冷却水を循環する系4及び膜蒸発濃縮装
置2がらの純水を回収する貯槽5からなる。泡沫分離装
置1は、被処理液の供給6、排出管7、泡沫を発生する
ためのニアコンプレッサ8、分散器9、発生した泡沫を
回収するための導管1o及び泡沫貯槽11からなる。被
処理液の加熱循環系統3は、被処理液の加熱槽12、液
加熱用のヒータ13及び液循環用ポンプ14が設けられ
ている。冷却水の循環系統4には、冷却水槽15、冷却
器16及び冷却水循環ポンプ17が設けられている。
Hereinafter, one embodiment of the present invention will be described with reference to the drawings. FIG. 1 shows a wastewater treatment apparatus in which the surfactant of the present invention contains salts. This device consists of a foam separator [1] that removes surfactants from a liquid to be treated, a membrane evaporation concentration device 2, a system 3 that heats and circulates the liquid to be treated, a system 4 that circulates cooling water, and a membrane evaporation concentration device 2. It consists of a storage tank 5 that collects purified water from the water. The foam separator 1 includes a supply 6 for a liquid to be treated, a discharge pipe 7, a near compressor 8 for generating foam, a disperser 9, a conduit 1o for recovering the generated foam, and a foam storage tank 11. The heating circulation system 3 for the liquid to be treated is provided with a heating tank 12 for the liquid to be treated, a heater 13 for heating the liquid, and a pump 14 for circulating the liquid. The cooling water circulation system 4 is provided with a cooling water tank 15, a cooler 16, and a cooling water circulation pump 17.

次に、本発明の廃水処理装置の動作について説明する。Next, the operation of the wastewater treatment apparatus of the present invention will be explained.

界面活性剤を含んだ被処理液は、まず、泡沫分離装置1
に導入される。被処理液は装置1の底部より吹込まれた
気泡により泡沫を発生し、装置llの上部に泡沫が集積
する。被処理液中の界面活性剤は泡沫中に濃縮されるの
でこれを上部の導管10より排出し、泡沫貯槽11に回
収して除去する。一方、泡沫分離装置1で界面活性剤を
除去した被処理液は底部に設けた液排出管7より抜出し
、液の加熱槽12へ移送する。加熱槽12で所定の温度
にした液はポンプ14で膜蒸発濃縮装置2の蒸発室に供
給されて循環する。また、膜蒸発濃縮装置2の冷却室へ
は冷却水槽15がら冷却水が供給循環されている。そこ
で、膜蒸発濃縮装置では、蒸発室から発生した蒸気は、
疎水性多孔質膜23を通過し、冷却壁で凝縮し、純水と
して回収できる。
The liquid to be treated containing a surfactant is first transferred to a foam separator 1.
will be introduced in The liquid to be treated generates foam due to air bubbles blown into the bottom of the device 1, and the foam accumulates at the top of the device 11. Since the surfactant in the liquid to be treated is concentrated into foam, this is discharged from the upper conduit 10, collected in the foam storage tank 11, and removed. On the other hand, the liquid to be treated from which the surfactant has been removed in the foam separator 1 is extracted from a liquid discharge pipe 7 provided at the bottom and transferred to a liquid heating tank 12. The liquid heated to a predetermined temperature in the heating tank 12 is supplied to the evaporation chamber of the membrane evaporation concentrator 2 by a pump 14 and circulated. Further, cooling water is supplied and circulated to the cooling chamber of the membrane evaporation concentrator 2 from a cooling water tank 15 . Therefore, in membrane evaporation concentrators, the steam generated from the evaporation chamber is
It passes through the hydrophobic porous membrane 23, condenses on the cooling wall, and can be recovered as pure water.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、界面活性剤を含む水溶液に対しても、
その機能を低下させることなく、安定した処理が可能で
ある。
According to the present invention, even for an aqueous solution containing a surfactant,
Stable processing is possible without deteriorating its functionality.

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

第1図は本発明の一実施例の廃水処理装置の系統図、第
2図は疎水性多孔質膜のくり返し耐水圧測定結果を示す
図、第3図は疎水性多孔質を用いた膜蒸発濃縮器の縦断
面図である。 1・・・泡沫分離装置、2・・・膜蒸発濃縮器、23・
・・疎第1図 第2図 λリ 飢0 革ど疋二
Figure 1 is a system diagram of a wastewater treatment equipment according to an embodiment of the present invention, Figure 2 is a diagram showing the results of repeated water pressure resistance measurements of a hydrophobic porous membrane, and Figure 3 is a membrane evaporation using a hydrophobic porous membrane. FIG. 3 is a longitudinal cross-sectional view of the concentrator. 1... Foam separator, 2... Membrane evaporation concentrator, 23.
・・Sparse 1st figure 2nd figure λri hunger 0 leather dohiki 2

Claims (1)

【特許請求の範囲】 1、界面活性剤及び塩類を含有する廃水の処理装置にお
いて、 前記界面活性剤を除去処理する気泡分離装置と、被処理
液の塩分を濃縮し、かつ、純水を回収する蒸発面に疎水
性多孔質膜を用いた膜蒸発濃縮装置とからなることを特
徴とする界面活性剤含有廃水の処理装置。
[Claims] 1. An apparatus for treating wastewater containing surfactants and salts, comprising: a bubble separator for removing the surfactant; and concentrating the salt content of the liquid to be treated and recovering pure water. A device for treating wastewater containing a surfactant, comprising a membrane evaporation concentration device using a hydrophobic porous membrane on the evaporation surface.
JP22466988A 1988-09-09 1988-09-09 Apparatus for treating waste water containing surfactant Pending JPH0275387A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22466988A JPH0275387A (en) 1988-09-09 1988-09-09 Apparatus for treating waste water containing surfactant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22466988A JPH0275387A (en) 1988-09-09 1988-09-09 Apparatus for treating waste water containing surfactant

Publications (1)

Publication Number Publication Date
JPH0275387A true JPH0275387A (en) 1990-03-15

Family

ID=16817360

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22466988A Pending JPH0275387A (en) 1988-09-09 1988-09-09 Apparatus for treating waste water containing surfactant

Country Status (1)

Country Link
JP (1) JPH0275387A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007216084A (en) * 2006-02-14 2007-08-30 Tokyo Rika Kikai Kk Circulation device
CN107428562A (en) * 2015-03-23 2017-12-01 荷兰联合利华有限公司 For reclaiming clean water and the apparatus and method of surfactant concentrate from buck

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007216084A (en) * 2006-02-14 2007-08-30 Tokyo Rika Kikai Kk Circulation device
JP4611220B2 (en) * 2006-02-14 2011-01-12 東京理化器械株式会社 Reflux equipment
CN107428562A (en) * 2015-03-23 2017-12-01 荷兰联合利华有限公司 For reclaiming clean water and the apparatus and method of surfactant concentrate from buck

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