JPH04200601A - Oil/water separating device - Google Patents

Oil/water separating device

Info

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
Application number
JP32927190A
Other languages
Japanese (ja)
Inventor
Susumu Horiuchi
進 堀内
Hiroaki Okajima
岡島 裕明
Nobuatsu Hayashi
林 伸厚
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 JP32927190A priority Critical patent/JPH04200601A/en
Publication of JPH04200601A publication Critical patent/JPH04200601A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain an oil/water separating device which does not clog even if solid matter is included in raw water and has an oil-droplet flocculating effect by providing a coarse-graining device adopting a fluidized bed type. CONSTITUTION:When oil containing raw water is made to flow in from a raw water inlet 1 on the lower part of a coalescer 4, the raw water is risen in the coalescer 4 and passed through a dispersing part 2, and is dispersed uniformly. As a result, particles filling upper zone of the dispersing part 2 form a fluidized bed 3. In this bed, the oil contents of the raw water are made coarse grains to form large oil droplets. The raw water containing these droplets is bed from an outlet 5 to an oily water separator where oil is easily separated from water. Further, if the solid matter deposits above and below the fluidized bed, it is discharged from solid matter outlets 8. As a result, the raw water can be treated stably and without a phenomenon such as clogging for a long time even if it contains the solid matter. In addition, the oil droplets collide with each other effectively and oil coarse-graining can be attained.

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.

〔従来の技術〕[Conventional technology]

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.

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

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).

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

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.

〔作用〕[Effect]

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.

〔実施例〕〔Example〕

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.

〔発明の効果〕〔Effect of the invention〕

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.

【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)

【特許請求の範囲】[Claims] 1、流動層方式を採用した粗粒化装置を設けたことを特
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.
JP32927190A 1990-11-30 1990-11-30 Oil/water separating device Pending JPH04200601A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (3)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
US5522999A (en) Water clarification method
CA2529839C (en) Vertical gas induced flotation cell
NO20031021D0 (en) Combined degassing and flotation tank
CN111039434A (en) Oily sewage treatment process and system
US2565343A (en) Liquid separation
EP2539287B1 (en) Ballast flocculation and sedimentation water treatment system with simplified sludge recirculation, and process therefor
SE500004C2 (en) Method and apparatus for separating gas bubbles and granular filter media from a filtrate which has passed a filter bed
CA1144110A (en) Process and apparatus for separating solids from suspensions of influent
CN114538639B (en) A pretreatment system and method for oily wastewater before biochemical treatment
JP3676208B2 (en) Solid-liquid separation tank
AU2004296266B2 (en) Flotation separator
RU2220007C2 (en) Separator intake hole
JP2001137743A (en) Apparatus for cleaning and recovering coolant
JP2003144805A (en) Oil-water separator
JPH05154476A (en) Membrane filter
JPH04200601A (en) Oil/water separating device
US4804471A (en) Oil-water separator
JP2892604B2 (en) Method and apparatus for dissolved air flotation and similar gas-liquid contact operations
Arnold Design concepts for offshore produced-water treating and disposal systems
KR100418172B1 (en) The oil-water seperating system and seperating method
RU2008062C1 (en) Settler for cleaning sewage waters
JPS56147687A (en) Cyclone type sewage purifying device
SU1255161A1 (en) Method of separating fine-dispersed mixes
US4903899A (en) Separator
CN117964180B (en) Oilfield produced water treatment system and treatment method