JPH04200601A - Oil/water separating device - Google Patents
Oil/water separating deviceInfo
- Publication number
- JPH04200601A JPH04200601A JP32927190A JP32927190A JPH04200601A JP H04200601 A JPH04200601 A JP H04200601A JP 32927190 A JP32927190 A JP 32927190A JP 32927190 A JP32927190 A JP 32927190A JP H04200601 A JPH04200601 A JP H04200601A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- raw water
- water
- solid matter
- fluidized bed
- 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
Links
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、一般産業廃水の油水分離、船舶のバラスト水
、タンク水、ビルジ水等の処理装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an apparatus for separating oil and water from general industrial wastewater, and for treating ballast water, tank water, bilge water, etc. of ships.
一般に、微小な油滴径の油分を含む排水中からその油分
を除去するのは難かしいため、微小油滴を凝させて、大
きな油滴にしてから浮上分離する方法がとられている。Generally, it is difficult to remove oil from wastewater containing oil with a diameter of minute oil droplets, so a method is used in which the minute oil droplets are condensed into large oil droplets, which are then floated and separated.
(特公昭39−2448号、特公昭45−38873号
公報および「水質汚濁防止の技術と機器」油濁防止(原
調出版))その油滴を凝集させる方法に繊維の充填層や
狭小流路中に油分を含んだ原水を流動させると、微小な
油滴が衝突し、大きな油滴にする粗粒化法という方法が
ある。しかし、この方法は手軽にコンパクトな装置で油
滴を大きくすることが出来るが、原水中に固形物がある
と、それによって、狭小流路が詰ってしまい、処理でき
なくなってしまうという欠点があった。(Japanese Patent Publication No. 39-2448, Japanese Patent Publication No. 45-38873 and "Water Pollution Prevention Techniques and Equipment" Oil Pollution Prevention (Gencho Publishing)) Methods for coagulating the oil droplets include a packed bed of fibers and a narrow channel. There is a method called coarsening, in which when raw water containing oil is made to flow, minute oil droplets collide and form larger oil droplets. However, although this method can easily increase the size of oil droplets using a compact device, it has the disadvantage that if solids are present in the raw water, the narrow channels will be clogged and treatment will not be possible. Ta.
従って、短時間で充填層等を取り替えるか、又は、洗浄
しなければならなかった。Therefore, the packed bed etc. had to be replaced or cleaned in a short time.
従来技術は前述のように充填層や狭小流路に固形物が詰
ってしまい、使用不可能になるため、新しいものに取り
替えるか、あるいは洗浄をするかしなければならなかっ
た。As mentioned above, in the conventional technology, the packed bed or narrow flow path becomes clogged with solid matter, making it unusable and requiring replacement with a new one or cleaning.
本発明の目的は、原水中に固形物が入っていても、目詰
りせず、かつ油滴の凝集効果(衝突効果)もある装置を
提供することにある。An object of the present invention is to provide an apparatus that does not become clogged even if solid matter is contained in the raw water, and that also has the effect of coagulating oil droplets (collision effect).
上述の目的を達成するには、
■ 固形物による目詰りを起こさない為には、固形物を
通過させてやる。To achieve the above objectives, ■ To prevent clogging caused by solids, solids must be allowed to pass through.
■ 微小油滴を凝集させて大きな油滴にするため、水中
の油滴を互いに衝突させる回数を増加させる。■ Increase the number of times oil droplets in water collide with each other in order to coagulate small oil droplets into large oil droplets.
即ち、よい混合状態を作ってやる。In other words, a good mixed state is created.
■、■の目的を達成するため、疎水性の粒子を用いた流
動層中を原水を通過させればその目的が達成できる。In order to achieve the objectives (1) and (2), the objectives can be achieved by passing raw water through a fluidized bed using hydrophobic particles.
流動層とは一般には下方より上方に向かって液体を流動
させ、その中に上昇速度とほぼ等しい速度以上の沈降速
度をもつ粒子を投入してやると、その固体粒子群として
の平均沈降速度と液体の上昇速度がつり合う状態になり
、ある空隙率を保ち、粒子が浮遊化されている状態であ
る。Generally speaking, a fluidized bed is a fluidized bed in which a liquid is made to flow from the bottom to the top, and when particles are introduced into the bed with a settling velocity that is approximately equal to or higher than the rising velocity, the average settling velocity of the solid particles and the liquid's This is a state in which the rising speeds are balanced, a certain porosity is maintained, and the particles are suspended.
従って、この中に他の粒子が入ってくると、沈降速度が
小さければ、粒子層を通過して溢流してゆくし、大きけ
れば下方にたまり分離できる。また、はとんど沈降速度
が等しい粒子の場合は流動層内に保持されるが、空隙率
は、常に、一定に保たれるため、目詰りすることはない
。層高が高くなったら抜き呂してやればよい。このため
、固形物による目詰りはなくなる。次の油滴の衝突であ
るが、流動層の粒子は完全混合と考えることが出来るの
で、ある層高以上の層高をとれば油滴の衝突も十分行な
われる。Therefore, when other particles enter this layer, if the sedimentation speed is low, they will pass through the particle layer and overflow, or if they are large, they will accumulate below and be separated. In addition, particles having almost the same sedimentation velocity are retained in the fluidized bed, but the porosity is always kept constant, so no clogging occurs. If the floor height becomes high, you can remove it. This eliminates clogging caused by solid matter. Regarding the next collision of oil droplets, the particles in the fluidized bed can be considered to be completely mixed, so if the bed height is greater than a certain level, the collision of oil droplets will be sufficient.
本発明の実施例を第1図に基づいて説明する。 An embodiment of the present invention will be described based on FIG.
油分を含んだ原水をコアレッサ4の下部の原水流入口1
より流入させる。すると原水はコアレッサ内を上昇し、
分散部2を通過する際に均一に分散されてコアレッサ内
を上昇するために分散部上部充填された粒子は流動層3
を形成し、そこで原水中の油分は粗粒化され大きな油滴
となり流出口5より油水分離器に逆られ油と水がたやす
く分離される。尚、固形物が流動層の上下に溜るようで
あったら固形物抜き出し口8より抜き出す。The raw water containing oil is passed through the raw water inlet 1 at the bottom of the coalescer 4.
Increase inflow. Then, the raw water rises inside the coalescer,
In order to be uniformly dispersed when passing through the dispersion section 2 and rise in the coalescer, the particles packed in the upper part of the dispersion section are placed in a fluidized bed 3.
There, the oil in the raw water is coarsened into large oil droplets, which are returned to the oil-water separator through the outlet 5, where the oil and water are easily separated. If solid matter accumulates above and below the fluidized bed, it is extracted from the solid matter extraction port 8.
第2図は応用例の一つであるが、コアレッサ4の上部に
油水分離器6をコンパクトに合体化させ一つの装置にし
た例で分離された油7は上部より抜き出される。FIG. 2 shows one application example in which an oil-water separator 6 is compactly integrated into a single device on the upper part of a coalescer 4, and the separated oil 7 is extracted from the upper part.
第3図は比重が1より小さい粒子を使った流動層であり
、原水は上から下に流動する。各部の作用は第1図と同
様である。Figure 3 shows a fluidized bed using particles with a specific gravity of less than 1, and raw water flows from top to bottom. The functions of each part are the same as in FIG.
本発明は、以上説明したように構成されているので以下
の効果がある。Since the present invention is configured as described above, it has the following effects.
■ 原水中の固形物が含まれていても目詰りなどの現象
もおこらず、長時間安定して処理できる。■ Even if the raw water contains solids, clogging and other phenomena do not occur, allowing stable processing for long periods of time.
■ 油滴量子の衝突効率もよく、油の粗粒化も達成され
る。■ Collision efficiency of oil droplets is also good, and oil particles can be coarsened.
以上の効果よりこれを油水分離装置に用いれば固形物を
含む含油排水でも、コンパクトな装置でメンテナンスも
なく、安定して効率良い油水分離が出来る。Based on the above effects, if this is used in an oil-water separator, even oil-containing wastewater containing solids can be stably and efficiently separated with a compact device and without maintenance.
第1図は本発明の一実施例の説明図、第2図は本発明の
装置に油水分離器をコンパクトに一体化装置の説明図、
第3図は流動層用充填粒子が比重1より小さい場合の実
施例の説明図である。
1・・・原水流入口、2・・・分散部、3・・・流動層
、4・・・コアレッサ本体、5・・・流出口、6・・・
油水分離器、系1図FIG. 1 is an explanatory diagram of an embodiment of the present invention, and FIG. 2 is an explanatory diagram of a device that compactly integrates an oil-water separator into the device of the present invention.
FIG. 3 is an explanatory diagram of an example in which the packed particles for a fluidized bed have a specific gravity of less than 1. DESCRIPTION OF SYMBOLS 1... Raw water inlet, 2... Dispersion part, 3... Fluidized bed, 4... Coalescer main body, 5... Outlet, 6...
Oil-water separator, system 1 diagram
Claims (1)
徴とする油水分離装置。1. An oil-water separator characterized by being equipped with a coarsening device that employs a fluidized bed method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32927190A JPH04200601A (en) | 1990-11-30 | 1990-11-30 | Oil/water separating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32927190A JPH04200601A (en) | 1990-11-30 | 1990-11-30 | Oil/water separating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04200601A true JPH04200601A (en) | 1992-07-21 |
Family
ID=18219584
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP32927190A Pending JPH04200601A (en) | 1990-11-30 | 1990-11-30 | Oil/water separating device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH04200601A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110078164A (en) * | 2019-05-06 | 2019-08-02 | 东北石油大学 | Two-stage tandem fluidized bed oil water separator |
| CN117143664A (en) * | 2023-09-14 | 2023-12-01 | 湖北天基生物能源科技发展有限公司 | Biological raw material oil extraction refining device for preparing second-generation biodiesel |
-
1990
- 1990-11-30 JP JP32927190A patent/JPH04200601A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110078164A (en) * | 2019-05-06 | 2019-08-02 | 东北石油大学 | Two-stage tandem fluidized bed oil water separator |
| CN117143664A (en) * | 2023-09-14 | 2023-12-01 | 湖北天基生物能源科技发展有限公司 | Biological raw material oil extraction refining device for preparing second-generation biodiesel |
| CN117143664B (en) * | 2023-09-14 | 2024-02-13 | 湖北天基生物能源科技发展有限公司 | Biological raw material oil extraction refining device for preparing second-generation biodiesel |
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