JPH09314127A - Concentration method of water-soluble oil wastewater - Google Patents

Concentration method of water-soluble oil wastewater

Info

Publication number
JPH09314127A
JPH09314127A JP15288296A JP15288296A JPH09314127A JP H09314127 A JPH09314127 A JP H09314127A JP 15288296 A JP15288296 A JP 15288296A JP 15288296 A JP15288296 A JP 15288296A JP H09314127 A JPH09314127 A JP H09314127A
Authority
JP
Japan
Prior art keywords
water
oil
concentrating
liquid
concentrated
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
JP15288296A
Other languages
Japanese (ja)
Inventor
Mamoru Kanekawa
護 金川
Toshihiro Oshima
稔弘 大島
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.)
Swing Corp
Original Assignee
Ebara Engineering Service Co 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 Ebara Engineering Service Co Ltd filed Critical Ebara Engineering Service Co Ltd
Priority to JP15288296A priority Critical patent/JPH09314127A/en
Publication of JPH09314127A publication Critical patent/JPH09314127A/en
Pending legal-status Critical Current

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  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

(57)【要約】 【課題】 水溶性油排水を濃縮限界ぎりぎりまで濃縮し
て減容化を確実にし、濃縮工程中での突沸発生をも防止
する。 【解決手段】 含油排水4を濃縮缶6に循環流させ濃縮
缶6中で加熱蒸気9によって加熱蒸留させて水蒸気10
と缶内液18とに分離させると共に、缶内液18のエマ
ルジョンをオイルインウォータ型からウォータインオイ
ル型に濃縮して濃縮液17として濃縮缶外に導出させる
水溶性油排水を濃縮するものであって、前記濃縮液の粘
度を粘度検出器15によって検知して濃縮限界で濃縮缶
6から濃縮液17を排出することで濃縮工程に突沸現象
がなく限度ぎりぎりまで減容化し、水溶性油排水処分を
経済的に行うことができる。
(57) [Abstract] [PROBLEMS] Concentrating water-soluble oil wastewater to the limit of concentration to ensure volume reduction and preventing bumping in the concentration process. SOLUTION: The oil-containing wastewater 4 is circulated to a condensing can 6 and is heated and distilled by a heated steam 9 in the condensing can 6 to obtain steam 10.
And the in-can liquid 18 are separated from each other, and the emulsion of the in-can liquid 18 is concentrated from an oil-in-water type to a water-in-oil type to concentrate the water-soluble oil drainage to be discharged as a concentrated liquid 17 out of the concentrated can. Therefore, the viscosity of the concentrate is detected by the viscosity detector 15 and the concentrate 17 is discharged at the concentration limit to reduce the volume to the limit without bumping phenomenon in the concentration process. Disposal can be done economically.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、金属切削油排水、
機械部品洗浄排水、金属加工排水等の水溶性含油排水を
加熱蒸留して濃縮し、濃厚含油排水とする排水量を減容
化処理するための濃縮方法に関するものである。
TECHNICAL FIELD The present invention relates to a metal cutting oil drainage,
The present invention relates to a concentration method for heat-distilling and concentrating water-soluble oil-containing wastewater such as machine parts cleaning wastewater and metalworking wastewater to reduce the volume of wastewater to be made into rich oil-containing wastewater.

【0002】[0002]

【従来の技術】従来から排水を加熱して排水中の水分を
蒸発させて含水率を低下し濃縮処理することが知られて
おり多用されている。またこの濃縮工程において、特定
の油含有水での処理に限れば濃縮液の比重や水分などの
測定によって濃縮処理を制御することも考えられる。
2. Description of the Related Art Conventionally, it has been known and widely used to heat waste water to evaporate the water in the waste water to reduce the water content and to perform a concentration treatment. Further, in this concentrating step, it is also conceivable to control the concentrating process by measuring the specific gravity and water content of the concentrated liquid, as long as it is limited to the treatment with a specific oil-containing water.

【0003】[0003]

【発明が解決しようとする課題】ところが、排水中には
各種の油分が混合されているため、その測定が煩雑で正
確な測定ができなく、誤差の多いものであったために濃
縮限界まで濃縮しないで許容値範囲で濃縮作業をやめて
しまうために減容化が十分満足できるものではなく事後
処分に多大の経費がかかって問題が多かった。しかも濃
縮缶内で缶内液の水分が蒸発し濃縮が進んで缶内液中の
油分が濃くなるとある時点からエマルジョンの型が変わ
り、エマルジョン粒の中の水が加熱されて蒸気に変わっ
て膨張し、エマルジョン粒の周りの油の膜を破裂させて
突沸現象を起し、缶内に缶内液が飛び散って缶内液の油
ミストが水蒸気側に飛散混合して水質汚染となり、せっ
かく分離した水分の水質を低下する欠点があった。本発
明は、これら従来の欠点を排除しようとするもので、水
溶性油排水を濃縮限界ぎりぎりまで濃縮して減容化を確
実にし、濃縮工程中での突沸発生をも防止して含油排水
の経済的処理を可能にする濃縮方法を提供することを目
的とするものである。
However, since various oil components are mixed in the wastewater, the measurement is complicated and accurate measurement cannot be performed, and there are many errors, so that the concentration is not reached to the concentration limit. Since the concentration work was stopped within the allowable range, the volume reduction was not sufficiently satisfactory, and the post-disposal was very expensive and there were many problems. Moreover, when the water in the can is evaporated and the oil in the can becomes thicker in the concentrated can, the emulsion type changes from a certain point, and the water in the emulsion particles is heated to steam and expands. Then, the film of oil around the emulsion particles was ruptured to cause a bumping phenomenon, the in-can liquid was scattered inside the can, and the oil mist in the can liquid was scattered and mixed on the water vapor side, resulting in water pollution and separation. There was a defect that the water quality of the water was deteriorated. The present invention is intended to eliminate these conventional drawbacks, by concentrating the water-soluble oil wastewater to the limit of the concentration to ensure volume reduction, and also prevent the occurrence of bumping during the concentration process to remove oil-containing wastewater. It is an object of the present invention to provide a concentration method that enables economical treatment.

【0004】[0004]

【課題を解決するための手段】本発明は、含油排水を濃
縮缶に循環流させ濃縮缶中で加熱蒸気によって加熱蒸留
させて水蒸気と缶内液とに分離させると共に、缶内液の
エマルジョンをオイルインウォータ型からウォータイン
オイル型に濃縮して濃縮液として濃縮缶外に導出させる
水溶性油排水濃縮方法において、前記濃縮液の粘度を粘
度検出器によって検知して濃縮限界で濃縮缶から濃縮液
を排出するものである。
According to the present invention, oil-containing wastewater is circulated through a concentrating can and heated and distilled by heating steam in the concentrating can to separate it into steam and a liquid in the can. In a water-soluble oil drainage concentrating method of concentrating from oil-in-water type to water-in-oil type and discharging it as a concentrate to the outside of the concentrating can, the viscosity of the concentrating liquid is detected by a viscosity detector and concentrated from the concentrating can at the concentration limit The liquid is discharged.

【0005】[0005]

【発明の実施の形態】本発明の実施形態では、含油排水
はオイルセパレータ、あるいはコワレッサーを通して浮
上油と水溶性油排水に分離され、分離された浮上油は貯
油槽に貯留され、一方、水溶性油排水は濃縮缶に送り入
れる。この濃縮缶には循環ポンプが設置され循環液配管
によって缶内液を循環させ、循環液配管の途中に粘度計
の粘度検出器を設置しておき、水溶性油排水は濃縮缶の
中で加熱蒸気によって加熱蒸留されて水蒸気と缶内液に
分離される。そして、水蒸気は真空ポンプでコンデンサ
に吸引され、該コンデンサにて冷却水で冷却され凝縮水
として流出する。この凝縮水は清澄水であり油分は全く
含まれていない。一方缶内液は水分が蒸発して行くため
だんだんと濃縮される。水分が蒸発し濃縮が進んで缶内
液中の油分が濃くなると、ある時点からエマルジョンの
型はオイルインウォーター型からウォーターインオイル
に変わり、その粘度は油の粘度に近くなる。すなわち、
ある時点から缶内液の粘度は0.5cpから5〜10c
p以上に急激に上昇する。それと同時に濃縮缶の中でウ
ォーターインオイルのエマルジョン粒は粒の中の水が加
熱されて蒸気に変わって膨張し、粒の周りの油の膜を破
裂させ、突沸を起こすようになるので、前記粘度検出器
で濃縮液の粘度が1〜5cpに達したら直ちに濃縮液弁
を開いて濃縮缶から濃縮液を排出する。この結果、濃縮
限界ぎりぎりまで濃縮缶内の水溶性油排水を濃縮でき
る。すなわち、粘度によって濃縮限界まで濃縮でき効率
のよい水溶性油排水の濃縮処理が可能である。
BEST MODE FOR CARRYING OUT THE INVENTION In the embodiment of the present invention, oil-containing wastewater is separated into a floating oil and a water-soluble oil wastewater through an oil separator or a coalescer, and the separated floating oil is stored in an oil storage tank, while The oil drainage is sent to a concentration can. A circulating pump is installed in this condensing can to circulate the liquid inside the can through the circulating liquid pipe, and a viscosity detector of the viscometer is installed in the middle of the circulating liquid pipe, and the water-soluble oil wastewater is heated in the condensing can. It is heated and distilled by steam and separated into water vapor and liquid in the can. Then, the water vapor is sucked into the condenser by the vacuum pump, cooled by the cooling water by the condenser, and flows out as condensed water. This condensed water is clear water and contains no oil. On the other hand, the liquid in the can is gradually concentrated as the water vaporizes. When the water content evaporates and the concentration increases and the oil content in the liquid inside the can becomes thicker, the type of emulsion changes from the oil-in-water type to water-in-oil at a certain point, and its viscosity becomes close to that of oil. That is,
From a certain point, the viscosity of the liquid in the can is 0.5 cp to 5 to 10 c
It rises sharply above p. At the same time, the water-in-oil emulsion particles in the concentrating can expand when water in the particles is heated to change to steam and expand, causing the oil film around the particles to burst and cause bumping. As soon as the viscosity of the concentrate reaches 1 to 5 cp with the viscosity detector, the concentrate valve is opened and the concentrate is discharged from the concentration can. As a result, the water-soluble oil wastewater in the concentrating can can be concentrated to the very limit of the concentration. That is, it is possible to concentrate the water-soluble oil wastewater with high efficiency by concentrating up to the concentration limit depending on the viscosity.

【0006】[0006]

【実施例】本発明の実施例を図1の例で説明すると、含
油排水4を濃縮缶6に循環流させ濃縮缶6中で加熱蒸気
9によって加熱蒸留させて水蒸気10と缶内液18とに
分離させると共に、缶内液18のエマルジョンをオイル
インウォータ型からウォータインオイル型に濃縮して濃
縮液17として濃縮缶外に導出させる水溶性油排水を濃
縮するものであって、前記濃縮液の粘度を粘度検出器1
5によって検知して濃縮限界で濃縮缶6から濃縮液17
を排出し、含油排水4を濃縮缶6に導入するものであ
る。
EXAMPLE An example of the present invention will be described with reference to the example of FIG. 1. The oil-containing wastewater 4 is circulated in a concentrating can 6 and heated and distilled by a heated steam 9 in the concentrating can 6 to produce steam 10 and a liquid 18 in the can. And concentrates the emulsion of the in-can liquid 18 from the oil-in-water type to the water-in-oil type to concentrate the water-soluble oil wastewater to be discharged outside the concentrated can as the concentrated liquid 17. Viscosity of viscosity detector 1
5, the concentration limit is detected and the concentration liquid is changed from the concentration can 6 to the concentration liquid 17
And the oil-containing wastewater 4 is introduced into the condensing can 6.

【0007】この場合、前記粘度検出器15による粘度
検出が濃縮液の循環流路或いは濃縮缶内中で粘度1〜5
cp、好ましくは2〜3cpとなることを検知して濃縮
缶6よりの循環液配管中の濃縮液排出弁16を開き、排
出すると共に、排出後に排出弁16を閉じ、かつ水溶性
油排水弁19を開いて水溶性油排水4を濃縮缶6内に供
給するのがよい。
In this case, the viscosity is detected by the viscosity detector 15 in the circulation channel of the concentrated liquid or in the concentrating can.
cp, preferably 2 to 3 cp is detected, the concentrated liquid discharge valve 16 in the circulating liquid pipe from the condensing can 6 is opened and discharged, and the discharged valve 16 is closed after discharge, and the water-soluble oil drain valve It is preferable to open 19 and supply the water-soluble oil drainage 4 into the concentrating can 6.

【0008】しかして、含油排水1はオイルセパレータ
2、あるいはコワレッサーを通して浮上油3と水溶性油
排水4に分離され、分離された浮上油3は貯油槽5に貯
留され、一方、水溶性油排水4は濃縮缶6に送り入れ
る。この濃縮缶6には循環ポンプ7が設置され循環液配
管8によって缶内液18を循環させ、循環液配管8の途
中に粘度計の粘度検出器15を設置しておき、水溶性油
排水4は濃縮缶6の中で加熱蒸気9によって加熱蒸留さ
れて水蒸気10と缶内液18に分離される。そして、水
蒸気10は真空ポンプ14でコンデンサ11に吸引さ
れ、該コンデンサ11にて冷却水12で冷却され凝縮水
13として流出する。この凝縮水13は清澄水であり油
分は全く含まれていない。一方、缶内液18は水分が蒸
発していくためだんだんと濃縮される。一般に水溶性油
排水はオイルインウォーター型のエマルジョンであり、
その粘度はほとんど水と同じであるが、すなわち50C
で濃縮した場合、当初缶内液の粘度は0.5cp近辺で
あり、水のそれと同じである。しかるに水分が蒸発し濃
縮が進んで缶内液18中の油分が濃くなると、ある時点
からエマルジョンの型はオイルインウォーター型からウ
ォーターインオイルに変わり、その粘度は油の粘度に近
くなる。すなわち、ある時点から缶内液18の粘度は
0.5cpから5〜10cp以上に急激に上昇する。そ
れと同時に濃縮缶6の中でウォーターインオイルのエマ
ルジョン粒は粒の中の水が加熱されて蒸気に変わって膨
張し、粒の周りの油の膜を破裂させ、突沸を起こすよう
になるので、前記粘度検出器15で濃縮液の粘度が1〜
5cpに達したら直ちに濃縮液排出弁16を開いて濃縮
缶6から濃縮液17を排出する。この結果、濃縮限界ぎ
りぎりまで濃縮缶内の水溶性油排水を濃縮できる。すな
わち、粘度によって濃縮限界まで濃縮でき効率のよい水
溶性油排水の濃縮処理が可能である。
Thus, the oil-containing wastewater 1 is separated into the floating oil 3 and the water-soluble oil wastewater 4 through the oil separator 2 or the coiler, and the separated floating oil 3 is stored in the oil storage tank 5, while the water-soluble oil wastewater is discharged. 4 is sent to the concentrated can 6. A circulating pump 7 is installed in the concentrating can 6, and a liquid 18 in the can is circulated by a circulating liquid pipe 8. A viscosity detector 15 of a viscometer is installed in the middle of the circulating liquid pipe 8. Is heated and distilled by the heating steam 9 in the concentrating can 6 to be separated into the steam 10 and the liquid 18 in the can. Then, the water vapor 10 is sucked by the condenser 11 by the vacuum pump 14, cooled by the cooling water 12 by the condenser 11, and flows out as condensed water 13. The condensed water 13 is clear water and contains no oil. On the other hand, the liquid 18 in the can is gradually concentrated as the water vaporizes. Generally, water-soluble oil drainage is an oil-in-water type emulsion,
Its viscosity is almost the same as that of water, ie 50C
When concentrated in, the viscosity of the liquid in the can is initially around 0.5 cp, which is the same as that of water. However, when the water content evaporates and the concentration increases and the oil content in the liquid 18 in the can becomes thick, the emulsion type changes from the oil-in-water type to the water-in oil at a certain point, and the viscosity becomes close to the viscosity of the oil. That is, from a certain point in time, the viscosity of the in-can liquid 18 rapidly increases from 0.5 cp to 5 to 10 cp or more. At the same time, the water-in-oil emulsion grains in the concentrating can 6 are heated by the water in the grains to expand into steam, causing the oil film around the grains to burst and causing bumping. With the viscosity detector 15, the viscosity of the concentrate is 1 to
Immediately after reaching 5 cp, the concentrated liquid discharge valve 16 is opened to discharge the concentrated liquid 17 from the concentrated can 6. As a result, the water-soluble oil wastewater in the concentrating can can be concentrated to the very limit of the concentration. That is, it is possible to concentrate the water-soluble oil wastewater with high efficiency by concentrating up to the concentration limit depending on the viscosity.

【0009】なお、前記水溶性油排水4としては、含油
排水1をオイルセパレータ2或いはコワレッサーを通し
て浮上油3を分離した水溶性油排水4としたものであっ
て、該水溶性油排水4を濃縮缶6に送り込んでバッチ式
または連続式に濃縮缶6の内部液として繰り返し循環ポ
ンプ7で循環させ、濃縮が進み減容化したところで濃縮
液17として導出し事後処分することが配慮されてい
る。
As the water-soluble oil drainage 4, the oil-containing drainage 1 is a water-soluble oil drainage 4 in which the floating oil 3 is separated through an oil separator 2 or a coalescer, and the water-soluble oil drainage 4 is concentrated. It is considered that the solution is sent to the can 6 and repeatedly circulated as the internal liquid of the concentrating can 6 in a batch or continuous manner by the circulation pump 7, and when the concentration progresses and the volume is reduced, it is discharged as the concentrated liquid 17 and post-disposal.

【0010】図1に示すように水溶性油排水の加熱濃縮
において、粘度検出器15を備えて廃液の濃縮に従って
エマルジョンの形がオイルインウォーター型からウォー
ターインオイル型に変化する点を粘度によって検知し、
濃縮限界まで濃縮できる濃縮装置を用いているが、図2
に示すように水溶性油排水を濃縮した場合、ある点から
急激に粘度が上昇するのと、油排水の種類によって、粘
度が急激に上昇する含水率が種々であることを示すの
で、この点を考慮するのがよい。
As shown in FIG. 1, in heating and condensing water-soluble oil wastewater, a viscosity detector 15 is provided to detect the point where the shape of the emulsion changes from an oil-in-water type to a water-in-oil type according to the concentration of the waste liquid. Then
A concentrator that can concentrate to the limit of concentration is used.
When water-soluble oil wastewater is concentrated as shown in, the viscosity increases sharply from a certain point, and it shows that the water content at which the viscosity sharply increases varies depending on the type of oil wastewater. It is better to consider

【0011】図3の実施例では、前記粘度検出器151
を濃縮缶6の缶底近傍に設け缶内液18の粘度を検知す
るようにした濃縮装置として用いることもできる。な
お、図4の例の如く多重効用缶(二重効用缶、または三
重効用缶)即ち前記濃縮缶6を複数直列に接続した多重
効用濃縮缶を用いた場合、最終濃縮缶の循環液配管また
は濃縮缶に粘度計の粘度検出器151 を設けて水溶性油
排水を濃縮限界まで濃縮するようにしたものや、他の蒸
発装置においても前記粘度検出器151 を設置すること
で、水溶性油排水を濃縮限界まで濃縮できる濃縮装置と
することもできる。
In the embodiment shown in FIG. 3, the viscosity detector 15 1
Can also be used as a concentrating device which is provided near the bottom of the concentrating can 6 and detects the viscosity of the liquid 18 in the can. When a multi-effect can (double-effect can or triple-effect can), that is, a multi-effect concentrator in which a plurality of the concentrating cans 6 are connected in series, is used as in the example of FIG. If the viscosity detector 15 1 of a viscometer is provided in the concentration can to concentrate the water-soluble oil wastewater to the concentration limit, or by installing the viscosity detector 15 1 in other evaporators, It is also possible to use a concentrating device that can concentrate the oil wastewater to the concentration limit.

【0012】[0012]

【発明の効果】本発明は、含油排水を濃縮缶に循環流さ
せ濃縮缶中で加熱蒸気によって加熱蒸留させて水蒸気と
缶内液とに分離させると共に、缶内液のエマルジョンを
オイルインウォータ型からウォータインオイル型に濃縮
して濃縮液として濃縮缶外に導出させる水溶性油排水濃
縮方法において、前記濃縮液の粘度を粘度検出器によっ
て検知して濃縮限界で濃縮缶から濃縮液を排出すること
により、濃縮工程が精度よく検出され油ミストが水蒸気
側に混入することを防ぎ、しかも従来の欠点を排除し
て、水溶性排水を濃縮限界ぎりぎりまで濃縮して減容化
を確実にし、濃縮工程中での突沸発生をも防止して含油
排水の経済的処分をも効率よくでき、水溶性油排水の処
理作業を著しく向上させることができる効果がある。
INDUSTRIAL APPLICABILITY According to the present invention, oil-containing wastewater is circulated through a concentrating can and heated and distilled in the concentrating can with heated steam to separate into water vapor and a liquid in the can, and an emulsion of the liquid in the can is oil-in-water type. In a water-soluble oil drainage concentrating method in which the concentrate is concentrated to waterine oil and discharged as a concentrate to the outside of the concentrator, the viscosity of the concentrate is detected by a viscosity detector, and the concentrate is discharged from the concentrate can at the concentration limit. As a result, the concentration process is accurately detected and oil mist is prevented from mixing into the water vapor side, while eliminating the conventional drawbacks and concentrating the water-soluble wastewater to the limit of concentration to ensure volume reduction. There is an effect that the occurrence of bumping in the process can be prevented, the economical disposal of the oil-containing wastewater can be efficiently performed, and the treatment work of the water-soluble oil wastewater can be significantly improved.

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

【図1】本発明の実施例方法の系統説明図である。FIG. 1 is a system explanatory view of an embodiment method of the present invention.

【図2】濃縮工程での処理液の粘度(cp)と含水率
(重量%)との関係を示す特性線図で、A及びBは水溶
性油排水の異なる種類で粘度が急激に上昇する含水率が
種々であることを示している。
FIG. 2 is a characteristic diagram showing the relationship between the viscosity (cp) of the treatment liquid and the water content (% by weight) in the concentration step, where A and B sharply increase in viscosity with different types of water-soluble oil wastewater. It shows that the water content is various.

【図3】本発明の他の実施例方法の一部の系統説明図で
ある。
FIG. 3 is a system diagram of a part of a method according to another embodiment of the present invention.

【図4】本発明のさらに他の実施例の系統説明図であ
る。
FIG. 4 is a system diagram of still another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1…含油排水 2…オイルセパレータ 3…浮上油 4…水溶性油排水 5…貯油槽 6…濃縮缶 7…循環ポンプ 8…循環液配管 9…加熱蒸気 10…水蒸気 11…コンデンサ 12…冷却水 13…凝縮水 14…真空ポンプ 15,151 …粘度検出器 16…濃縮液排出弁 17…濃縮液 18…缶内液 19…水溶性油排水弁1 ... Oil-containing drainage 2 ... Oil separator 3 ... Floating oil 4 ... Water-soluble oil drainage 5 ... Oil storage tank 6 ... Concentrator 7 ... Circulation pump 8 ... Circulating liquid piping 9 ... Heating steam 10 ... Steam 11 ... Condenser 12 ... Cooling water 13 ... Condensed water 14 ... Vacuum pumps 15 and 15 1 ... Viscosity detector 16 ... Concentrated liquid discharge valve 17 ... Concentrated liquid 18 ... Can liquid 19 ... Water-soluble oil drain valve

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 含油排水を濃縮缶に循環流させ濃縮缶中
で加熱蒸気によって加熱蒸留させて水蒸気と缶内液とに
分離させると共に、缶内液のエマルジョンをオイルイン
ウォータ型からウォータインオイル型に濃縮して濃縮液
として濃縮缶外に導出させる水溶性油排水濃縮方法にお
いて、前記濃縮液の粘度を粘度検出器によって検知して
濃縮限界で濃縮缶から濃縮液を排出することを特徴とす
る水溶性油排水の濃縮方法。
1. An oil-containing wastewater is circulated through a concentrating can, and is heated and distilled by heating steam in the concentrating can to separate into water vapor and a liquid in the can, and an emulsion of the liquid in the can is changed from an oil-in-water type to a water-in oil. In a method for concentrating water-soluble oil wastewater, which is concentrated in a mold and discharged as a concentrated liquid to the outside of a concentrated can, the viscosity of the concentrated liquid is detected by a viscosity detector, and the concentrated liquid is discharged from the concentrated can at the concentration limit. A method for concentrating water-soluble oil wastewater.
【請求項2】 前記粘度検出器による粘度検出が濃縮液
の循環流路或いは濃縮缶内中で粘度1〜5cpとなるこ
とを検知して濃縮缶よりの循環液配管中の排出弁を開閉
制御する請求項1記載の水溶性油排水濃縮方法。
2. The opening / closing control of the discharge valve in the circulating liquid piping from the concentrating can is detected by detecting that the viscosity detected by the viscosity detector has a viscosity of 1 to 5 cp in the concentrating liquid circulation channel or the concentrating can. The method for concentrating water-soluble oil wastewater according to claim 1.
【請求項3】 前記濃縮缶を複数直列に接続した多重効
用濃縮缶を用いた場合、最終濃縮缶に粘度計を設けて水
溶性油排水を濃縮限界まで濃縮するようにした請求項1
または2記載の水溶性油排水濃縮方法。
3. When using a multi-effect concentrator in which a plurality of concentrators are connected in series, a viscometer is provided in the final concentrator to concentrate the water-soluble oil wastewater to the concentration limit.
Alternatively, the water-soluble oil wastewater concentration method described in 2.
JP15288296A 1996-05-27 1996-05-27 Concentration method of water-soluble oil wastewater Pending JPH09314127A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15288296A JPH09314127A (en) 1996-05-27 1996-05-27 Concentration method of water-soluble oil wastewater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15288296A JPH09314127A (en) 1996-05-27 1996-05-27 Concentration method of water-soluble oil wastewater

Publications (1)

Publication Number Publication Date
JPH09314127A true JPH09314127A (en) 1997-12-09

Family

ID=15550189

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15288296A Pending JPH09314127A (en) 1996-05-27 1996-05-27 Concentration method of water-soluble oil wastewater

Country Status (1)

Country Link
JP (1) JPH09314127A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006175428A (en) * 2004-11-25 2006-07-06 Okawara Mfg Co Ltd Mist removal structure in high speed rotary evaporating device, and method for treating oil-containing waste water using the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006175428A (en) * 2004-11-25 2006-07-06 Okawara Mfg Co Ltd Mist removal structure in high speed rotary evaporating device, and method for treating oil-containing waste water using the same

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