JPS6322875B2 - - Google Patents
Info
- Publication number
- JPS6322875B2 JPS6322875B2 JP54094602A JP9460279A JPS6322875B2 JP S6322875 B2 JPS6322875 B2 JP S6322875B2 JP 54094602 A JP54094602 A JP 54094602A JP 9460279 A JP9460279 A JP 9460279A JP S6322875 B2 JPS6322875 B2 JP S6322875B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- pipe
- bubbles
- water conduit
- conduit
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 28
- 239000004094 surface-active agent Substances 0.000 claims description 10
- 238000000926 separation method Methods 0.000 claims description 8
- 239000002351 wastewater Substances 0.000 claims description 8
- 238000005187 foaming Methods 0.000 claims description 7
- 239000006260 foam Substances 0.000 claims description 5
- 239000010865 sewage Substances 0.000 description 9
- 238000010586 diagram Methods 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000012190 activator Substances 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Degasification And Air Bubble Elimination (AREA)
- Physical Water Treatments (AREA)
Description
【発明の詳細な説明】
本発明は、水中に含まれる界面活性剤を効率良
く発泡せしめて、分離、除去する装置に関するも
のである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for efficiently foaming, separating, and removing surfactants contained in water.
下水、工場排水等、廃棄物となつた水中には、
人の生活活動あるいは、生産工程から排出された
界面活性剤を多量に含む例が多い。この活性剤
は、有機物の一般的処理法である。「生物酸化」
では分解が困難で、水処理を行なう上で、極めて
取扱いが面倒である。界面活性剤の除去方法とし
ては、活性炭を用いる方法が一般に用いられてい
るが、PH、温度、当該活性剤の分子量などによつ
てて吸着特性が変る上に、コスト的に極めて高い
ものになつてしまう。 In waste water such as sewage and factory wastewater,
Many cases contain large amounts of surfactants discharged from human activities or production processes. This activator is a common method for treating organic matter. "Biological oxidation"
However, it is difficult to decompose and is extremely difficult to handle for water treatment. As a method for removing surfactants, a method using activated carbon is generally used, but the adsorption characteristics vary depending on the pH, temperature, molecular weight of the active agent, etc., and the cost is extremely high. I end up.
本発明は、界面活性剤含有水に気泡を生じさ
せ、活性剤を水中から発泡分離させようとするも
のである。 The present invention aims to generate bubbles in surfactant-containing water to foam and separate the surfactant from the water.
以下に図を参照して、本発明の実施例の装置及
びその操作、処理について詳述する。第1図は装
置の要部配置図、第2図はその処理状況を示す。
1は界面活性剤を含有した汚水を導く導管で該導
管1は発泡タンク2に接続され、発泡タンク2の
全部には発泡成長のための継管31・32を接続
し、継管31に汚水が吸入される際、第2図に示
すように空気が巻き込まれ汚水と空気の混合によ
つて発泡作用が生じる。 DESCRIPTION OF THE PREFERRED EMBODIMENTS An apparatus according to an embodiment of the present invention, its operation, and processing will be described in detail below with reference to the drawings. FIG. 1 is a layout diagram of the main parts of the device, and FIG. 2 shows its processing status.
Reference numeral 1 denotes a conduit for guiding wastewater containing a surfactant, and the conduit 1 is connected to a foaming tank 2. All of the foaming tank 2 is connected with joint pipes 3 1 and 3 2 for foam growth. When sewage is sucked into 1 , air is drawn in as shown in Figure 2, and the mixture of sewage and air causes a foaming effect.
継管31内を汚水が通過する際、気泡は該継管
31内にて成長し大きくなる。 When wastewater passes through the pipe 3 1 , air bubbles grow and become larger within the pipe 3 1 .
成長した気泡を含んだ汚水は継管31の一端か
ら導管4に導かれ、導管4は継管31とほぼ垂直
に下方に伸長されており、分離タンク5内に接続
されたバルブ(チーズ)6にて分離水と気泡とに
分離する。バルブ6には導水管7と気泡管8が接
続されており、導水管7を経て分離タンク5に溜
つた分離水は排水管9から排水取水される。 The sewage containing the grown bubbles is led from one end of the pipe 3 1 to the pipe 4 , which extends downward almost perpendicularly to the pipe 3 1 . ) Separate into separated water and bubbles in step 6. A water conduit 7 and a bubble pipe 8 are connected to the valve 6, and the separated water accumulated in the separation tank 5 via the water conduit 7 is drained and taken from a drain pipe 9.
バルブ6、導水管7、気泡管8の接続状態は第
4図の如くであり、バルブ6の処に落下した汚水
は更に気泡を発泡させ、傾斜角(α=15゜±5゜が
好都合であつた。)を利用して水は下方に流れ導
水管7内に流れ込んで分離タンク5内に溜まる。 The connection state of the valve 6, water conduit 7, and bubble pipe 8 is as shown in Fig. 4, and the sewage that falls at the valve 6 further generates bubbles, and the angle of inclination (α = 15° ± 5° is convenient). ), the water flows downward into the water conduit 7 and accumulates in the separation tank 5.
バルブ6に落下した成長した気泡は汚水の落下
力による圧力等で気泡管8内を進み、分岐点10
にて残つた水は導水管11を経て分離タンク5内
に溜まる。 The grown bubbles that have fallen into the valve 6 advance through the bubble tube 8 due to the pressure caused by the falling force of the sewage, and reach a branch point 10.
The remaining water passes through the water conduit 11 and accumulates in the separation tank 5.
そして界面活性剤を含んだ気泡は導水管11の
上部に進み、第5図に示す気泡導管12の出口か
ら消泡タンク13内に押し出される。14は消泡
剤収納タンクでポンプ15にて吸引し、管16を
経て消泡タンク13に消泡剤を注入して消泡を行
う。第4図に示す、A・B・C部には15゜±5゜程
度の傾斜角を設けることにより、水分と気泡分の
分離作用が良く行なえることがわかつた。更に第
5図に示す、気泡導管12の傾斜角βを適宜変え
ることにより、水滴と泡の分離を行うことがで
き、βの角度によつて水滴と泡の分離比率を変え
ることができる。即ち、βを零にすると泡の量は
多いがそれに含まれる水滴も多くなり、角度をつ
けるごとに泡の量が少なくなるとともにそれ以上
に水滴が少なくなり任意角度にて泡のみを排出
し、水滴は導水管11に注入されるようになる。 The bubbles containing the surfactant then proceed to the upper part of the water conduit 11 and are pushed out into the defoaming tank 13 from the outlet of the bubble conduit 12 shown in FIG. Reference numeral 14 denotes a defoaming agent storage tank, which is suctioned by a pump 15 and is injected into the defoaming tank 13 through a pipe 16 to defoam. It has been found that by providing an inclination angle of approximately 15°±5° in portions A, B, and C shown in FIG. 4, the water and air bubbles can be effectively separated. Further, by appropriately changing the inclination angle β of the bubble conduit 12 shown in FIG. 5, water droplets and bubbles can be separated, and the separation ratio of water droplets and bubbles can be changed by changing the angle β. In other words, if β is set to zero, the amount of bubbles will be large, but the amount of water droplets included will also increase, and as the angle increases, the amount of bubbles will decrease and the number of water droplets will decrease further, allowing only the bubbles to be discharged at any angle. Water droplets are injected into the water conduit 11.
本発明に係る界面活性剤除去装置を用いてレン
ズ加工排水を処理したところ、従来COD値(化
学的酸素要求量)3.4ppmであつたものが本装置
によれば134〜250ppmとなり、TOC値(有機炭
素量)は7ppm程度のものが100〜200ppmの濃縮
水として抜出すことが出来た。 When lens processing wastewater was treated using the surfactant removal device according to the present invention, the conventional COD value (chemical oxygen demand) of 3.4 ppm became 134 to 250 ppm with this device, and the TOC value ( The amount of organic carbon (organic carbon content) was about 7 ppm, but it was possible to extract it as concentrated water with a concentration of 100 to 200 ppm.
第1図は本発明の実施例の一つの装置の例を示
す配置図。第2図は第1図の装置の操作、処理状
態を示す説明図。第3図は第2図の発泡タンク内
での汚水と空気の混入の様子を示す説明図。第4
図は第2図のバルブ6附近の管の配管の様子及び
汚水、気泡の分離模様を示す説明図。第5図は第
2図の分岐点10附近の気泡と水滴の様子を示す
説明図。
1…汚水導管、2…発泡タンク、31,32…導
管(中継管)、5…分離タンク、7,11…導水
管。
FIG. 1 is a layout diagram showing an example of an apparatus according to an embodiment of the present invention. FIG. 2 is an explanatory diagram showing the operation and processing status of the apparatus shown in FIG. 1. FIG. 3 is an explanatory diagram showing how sewage and air are mixed in the foaming tank shown in FIG. 2. Fourth
The figure is an explanatory diagram showing the state of the piping in the vicinity of the valve 6 in Fig. 2 and the separation pattern of sewage and air bubbles. FIG. 5 is an explanatory diagram showing the state of bubbles and water droplets near the branching point 10 in FIG. 2. 1... Sewage conduit, 2... Foaming tank, 3 1 , 3 2 ... Conduit (relay pipe), 5... Separation tank, 7, 11... Water conduit pipe.
Claims (1)
に前記汚水に空気を取り入れる継管を設け、 前記継管に発泡成長用継管を接続して分離タン
ク内に導き、 前記分離タンク内に前記発泡成長用継管と略平
行に導水管を設け、 前記発泡成長用継管と前記導水管の間を前記導
水管方向への上向き傾斜角を保つて気泡管を接続
し、 前記導水管の上端側を消泡タンクに導びくよう
に構成したことを特徴とする水中の界面活性剤除
去装置。[Scope of Claims] 1. A foaming tank containing wastewater containing a surfactant is provided with a joint pipe for introducing air into the wastewater, and a foam growth joint pipe is connected to the joint pipe to lead the wastewater into a separation tank, A water conduit is provided in the separation tank substantially parallel to the foam growth joint, and a vial is connected between the foam growth joint and the water conduit while maintaining an upward slope in the direction of the water conduit. . An underwater surfactant removal device, characterized in that the upper end side of the water conduit pipe is configured to lead to a defoaming tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9460279A JPS5617680A (en) | 1979-07-25 | 1979-07-25 | Removing apparatus for surfactant in water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9460279A JPS5617680A (en) | 1979-07-25 | 1979-07-25 | Removing apparatus for surfactant in water |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5617680A JPS5617680A (en) | 1981-02-19 |
JPS6322875B2 true JPS6322875B2 (en) | 1988-05-13 |
Family
ID=14114796
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9460279A Granted JPS5617680A (en) | 1979-07-25 | 1979-07-25 | Removing apparatus for surfactant in water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5617680A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63209701A (en) * | 1987-02-24 | 1988-08-31 | Mamoru Suzuki | Method and device for removing water |
JP2015136903A (en) * | 2014-01-24 | 2015-07-30 | 株式会社Screenホールディングス | Liquid storage device, liquid storage method, and ink jet recorder |
PL422632A1 (en) * | 2017-08-25 | 2019-03-11 | Zachodniopomorski Uniwersytet Technologiczny W Szczecinie | Method for decreasing foaming of wastewater that contains non-ionic surfactants |
PL422633A1 (en) * | 2017-08-25 | 2019-03-11 | Zachodniopomorski Uniwersytet Technologiczny W Szczecinie | Method for decreasing foaming of wastewater that contains anionic surfactants |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4936151A (en) * | 1972-08-08 | 1974-04-03 | ||
JPS5315798U (en) * | 1976-07-21 | 1978-02-09 |
-
1979
- 1979-07-25 JP JP9460279A patent/JPS5617680A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4936151A (en) * | 1972-08-08 | 1974-04-03 | ||
JPS5315798U (en) * | 1976-07-21 | 1978-02-09 |
Also Published As
Publication number | Publication date |
---|---|
JPS5617680A (en) | 1981-02-19 |
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