JPS59130506A - Oil-water separating device - Google Patents

Oil-water separating device

Info

Publication number
JPS59130506A
JPS59130506A JP616683A JP616683A JPS59130506A JP S59130506 A JPS59130506 A JP S59130506A JP 616683 A JP616683 A JP 616683A JP 616683 A JP616683 A JP 616683A JP S59130506 A JPS59130506 A JP S59130506A
Authority
JP
Japan
Prior art keywords
oil
chamber
water
fluidized bed
medium
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
JP616683A
Other languages
Japanese (ja)
Inventor
Mitsuo Nakajima
光夫 中島
Satoshi Yanaka
谷中 智
Takuji Kato
加藤 卓爾
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.)
HOWA SHOJI KK
Toyota Motor Corp
Original Assignee
HOWA SHOJI KK
Toyota Motor Corp
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 HOWA SHOJI KK, Toyota Motor Corp filed Critical HOWA SHOJI KK
Priority to JP616683A priority Critical patent/JPS59130506A/en
Publication of JPS59130506A publication Critical patent/JPS59130506A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To separate efficiently an oil from water with a compact device by providing an oil floating chamber to the top of a tower-shaped vessel, and flowing an oil-containing water from the lower side to the highest part and extracting the oil from the upper side and the water from the middle part, in constituting a titled device. CONSTITUTION:A titled device is constituted of an oil-containig water introducing chamber 1 having an introducing hole 11, a water discharging chamber 3 having a discharging hole 31, an oil content collecting chamber 4 in which a packing material 41 is arranged, and an oil floating chamber 5. An oil-containg water is fed into the chamber 1 through a pipe 12 by a pump, and is flowed into the chamber 2 through a filter 21. Here, granular medium is mixed with the water while being fluidized, and the oil content is adsorbed on the surface of the medium to grow a coarse particle. The coarse oil content separates from the medium and enters the chamber 5 after passing through a filter 22 and a water introducing passage 6. Then the oil content moves upward, and the treated water enters the chamber 4 and is discharged from a discharging pipe 31 after the residual oil content is removed by the packing material 41.

Description

【発明の詳細な説明】 本発明は水中に分1iりする微細な油分を取り除く油水
分離装置に関りるものである。油水分離装置としては、
遠心分離装置等で水と油を分離する装置、あるいは、油
を含む水を静置したり層流状態で静かに流し、油分の自
然浮上を持ち水面に浮き上って来る油分を取り除く装置
等が知られている。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an oil-water separator that removes minute oil particles from water. As an oil/water separator,
A device that separates water and oil using a centrifugal separator, or a device that allows oil-containing water to stand still or flows quietly in a laminar flow state, allowing oil to naturally float to the surface and removing the oil that rises to the surface of the water. It has been known.

しかし、遠心分離装置の場合には、水中に固形の有用成
分が分散している場合には、油と共に有用な固形成分ま
で分離される。又、油分の自然浮上を持つ装置では、効
率が比較的低いという問題がある。」−記した装置に対
して、さらに、最近になっては、親水性樹脂と新油性樹
脂とで構成される粒状の媒体を用い、水中に分散り−る
微細な油分を媒体の表面に吸着させ、その表面で油分を
粗大化し、粗大化した油分を分離させ、水中の油分を粗
大化させる媒体が知られている。この油分粗大化媒体は
通常流動床状態で使用され、効率よく水中に微細に分散
する油分を吸着粗大化さゼている。
However, in the case of a centrifugal separator, if solid useful components are dispersed in water, the useful solid components are separated along with the oil. Furthermore, devices with natural floating of oil have a problem of relatively low efficiency. In addition to the device described above, recently, a granular medium composed of a hydrophilic resin and a new oil-based resin has been used to adsorb fine oil particles dispersed in water onto the surface of the medium. There is known a medium that coarsens the oil content on its surface, separates the coarsened oil content, and coarsens the oil content in water. This oil coarsening medium is usually used in a fluidized bed state, and efficiently adsorbs and coarsens finely dispersed oil in water.

本発明のg首はこの油分粗大化媒体を用いた油水分離装
置に関するものである。
The g head of the present invention relates to an oil/water separation device using this oil coarsening medium.

即ち、本発明の油水分前装置は、塔状’r−その下方よ
り上方に、導入孔をもつ油水導入室、流1riJI床室
、水尋出孔をもつ排水室、油分捕集室の上方に油導出孔
をもつ油浮上室をもち、上記流動床室はその1喘と下端
に、各々設【プられたフィルタで区画され、かつ該流動
床室には親水性樹脂と新油性樹脂とで構成された粒状の
油分吸着粗大化媒体が流動状態で配置され、上記流動床
室の上方フィルタと」−記排水室とは底板で水密的に封
鎖され、かつこの底板を貫通し、上方フィルタの上方と
上記油浮上室とを連通づる導水路が形成され、上記油分
捕集室には充填材が配置された構造をもち、油を含む水
が油水導入室より下方フrルタを通って流動床室に入り
、該流動床室C′油が油分吸着粗大化媒体に吸着され粗
大化されて分離し、粗大化された油を含む水が上方フィ
ルタを通り、さらに導水路を通って油浮上室に入り、こ
の油浮上室で油を浮上させ、油のみを油導出孔より排出
し、水を下方に流し、油分捕集室を通り、水中に残った
油を充填材の表面に吸着させて取り除き、さらに下方に
流れて排水室に入り、この排水室より水心出孔tこ排出
されるように構成されたことを特徴とするものである。
That is, the oil/water pre-equipment of the present invention has a tower-shaped 'r--from the bottom to the upper side, an oil/water introduction chamber having an introduction hole, a flow 1riJI floor chamber, a drainage chamber having a water outlet hole, and an oil collecting chamber above the column. The fluidized bed chamber has an oil flotation chamber with an oil outlet hole at the top, and the fluidized bed chamber is partitioned by filters installed at the bottom end and the bottom end of the fluidized bed chamber, and the fluidized bed chamber contains a hydrophilic resin and a new oil-based resin. A granular oil-absorbing coarsening medium composed of is arranged in a fluidized state, and the upper filter of the fluidized bed chamber and the drainage chamber are watertightly sealed off by a bottom plate, and penetrate through this bottom plate, and pass through the upper filter. A water conduit is formed that communicates the upper part with the oil flotation chamber, and a filler is placed in the oil collection chamber, so that water containing oil flows from the oil-water introduction chamber through the lower filter. The oil in the fluidized bed chamber C' is adsorbed by the oil adsorption coarsening medium, coarsened and separated, and the water containing the coarsened oil passes through the upper filter and further passes through the water conduit to absorb the oil. Enters the flotation chamber, floats the oil in this oil flotation chamber, discharges only the oil from the oil outlet hole, flows the water downward, passes through the oil collection chamber, and the oil remaining in the water is adsorbed on the surface of the filler material. It is characterized in that it is configured such that the water is removed, flows further downward, enters a drainage chamber, and is discharged from the drainage chamber through a center outlet hole.

本発明の装置においでは塔状で、ぞの最上部に油浮上室
を設【ノ、処理される水が筒の下方にり最上部に登り、
最上部より更に下方に流れ、処理された水が塔の中程よ
り取り出され処理水中に含まれる油分の流れを可能な限
り上方に流し、上方より油分を取り出づ構成とし、装置
自体を非常にコンパクトにしたところに特色がある。
The apparatus of the present invention is shaped like a tower and has an oil flotation chamber at the top of the tower.
The treated water flows further downward from the top, the treated water is taken out from the middle of the tower, the oil contained in the treated water is allowed to flow upward as much as possible, and the oil is taken out from above. Its distinctive feature is that it is compact.

本発明の油水分離装置の油水導入室は、底部あるいは側
壁部に導入孔をもち、上方に開口部をbつ構成をとる。
The oil and water introduction chamber of the oil and water separator of the present invention has an introduction hole in the bottom or side wall and has two openings at the top.

この間口に流動床室の下方フィルタが設しプられている
。この油水導入室は下方フィルタ仝面に等しい水圧が作
用り−るために設(プられる。なJ3、下方フィルタの
通過抵抗が比較的大きい場合には、油水導入宅内にお(
〕る処理水の流れ等により、下方フィルタに作用する圧
ノjが部分的に異なっても悲影管は少ない。
A lower filter of the fluidized bed chamber is installed in this opening. This oil/water introduction chamber is designed so that equal water pressure acts on the surface of the lower filter.
Even if the pressure acting on the lower filter differs partially due to the flow of treated water, etc., there will be fewer tragedian tubes.

流動床室は導入される処理水により!l1体が流動化し
、処理水どの接触を高め、処理水中の油分を効率に<媒
体表面に吸着させる役割をもつ。この流動床ηアは下方
フィルタと上方フィルタの間の4ゞとして区画され、こ
の流動床室では処理水は下より上に流れ、媒体は流れる
処理水中に1下してただよう。油分の吸着に時間がかか
る場合には処理水の流速を下げるとか、両フィルタ聞の
距離を贈り。
Due to the treated water introduced into the fluidized bed room! It has the role of fluidizing the l1 body, increasing contact with the treated water, and efficiently adsorbing the oil in the treated water onto the surface of the medium. This fluidized bed ηa is defined as 4° between the lower filter and the upper filter, in which the treated water flows from the bottom to the top, and the medium is suspended in the flowing treated water. If it takes time for oil to be absorbed, reduce the flow rate of the treated water or increase the distance between the two filters.

4【J3、媒体の比重は、処理水の比!F1流速に合わ
せて調節する必要があり、流動状態では媒体が両フCル
タ間で全体的に分散しているようにづる。
4 [J3, The specific gravity of the medium is the ratio of the treated water! It is necessary to adjust the F1 flow rate so that the medium is completely dispersed between both filters in the flowing state.

排水室はその下方の油分捕集室内を処理水が均一に流れ
るように覆るためのもので、排水抵抗による処理水の流
れが油分捕集室に影響を与えないためのものである。
The purpose of the drainage chamber is to cover the oil collection chamber below so that the treated water flows uniformly, and to prevent the flow of treated water due to drainage resistance from affecting the oil collection chamber.

油分捕集¥は、粗大油分が油滓」−室にd3Gプる渦流
等の異常流れにより、浮上せず、処理水にまぎれて流下
覆るものを捕集Jる室である。この油分捕集室には油分
を捕集する充l眞材が配置される。
The oil collection chamber is a chamber that collects coarse oil that does not rise to the surface due to abnormal flows such as eddy currents that flow into the chamber, but gets mixed up with the treated water and falls over. A filling material for collecting oil is arranged in this oil collecting chamber.

油滓、F室は粗大化された油分を水ど分11111す゛
る至である。この室では導水路より粗大化された油分を
含む処理水が宝の上方にb y=らされ、油はそのまま
下方に、油分を含まない水が下方に流れる。
The soapstock and chamber F contain 11111 of the coarsened oil and water. In this chamber, the treated water containing coarsened oil is directed upward from the water conduit, the oil flows downward as it is, and the water without oil flows downward.

なお、処理水中を浮上りる油分の浮上速度より起い速度
で処理水が下降づ゛るように、処理水の流速、あるいは
室の断面積を変える必要がある。この装置においては処
理水中の水は最下部より、即ち、油水導入室J、り流動
床室、油滓」−室とj?1状の装置を上昇し、油浮上室
で方向反転し、下方に流れ、油分捕集室、排水室と流れ
る。−万、油の流れは油水導入室、流動床室と上りに流
′!1、この流動床室で油は粗大化される。そし゛(さ
らに上方に流れC油浮上室に送られ、この油滓」−空C
粗大化された油は油浮上室の上方に集まる。更に水と其
に部分的に油分捕集室に紛れ込む油分は、油分j11)
集室でそこに充填された充填材の表面に衝突し、充填拐
に吸着され、充JtyI材C吸肴凝集されて粗大化し、
粗大した油分は、水の流れに抗して上方に浮上し油滓」
1空に入り、更に油浮上室の上方に束まる。
Note that it is necessary to change the flow rate of the treated water or the cross-sectional area of the chamber so that the treated water descends at a higher speed than the floating speed of the oil components floating in the treated water. In this device, the water in the treated water is introduced from the bottom, ie, the oil-water introduction chamber J, the fluidized bed chamber, the soapstock chamber and the chamber J? The oil rises through the 1-shaped device, reverses direction in the oil flotation chamber, flows downward, and flows to the oil collection chamber and drainage chamber. -The oil flows upward from the oil/water introduction chamber to the fluidized bed chamber! 1. Oil is coarsened in this fluidized bed chamber. Then, the soapstock flows further upward and is sent to the C oil floating chamber.'' - Empty C
The coarsened oil collects above the oil flotation chamber. Furthermore, the oil that partially mixes with the water in the oil collection chamber is oil j11).
In the collecting chamber, the material collides with the surface of the filling material filled there, is adsorbed by the filling material, and becomes coarse as the material C absorbs and aggregates.
The coarse oil resists the flow of water and floats upwards, forming an oil slag.
1 into the sky, and further bunches above the oil flotation chamber.

このように油分は常に筒の上方に移動づる構成とされて
いる。
In this way, the oil always moves upwards in the cylinder.

このように水油水分離装置では、各室を−L[Zに配置
し、かつ油分を常に上方に流す構成としている。このた
め装置自体がコンパクトとなり、油分の分離効果も高く
なる。
In this way, the water/oil/water separator has a configuration in which each chamber is arranged at -L[Z, and oil always flows upward. Therefore, the device itself becomes compact and the oil separation effect becomes high.

また水油水分閃1装置は油水分離に当り、添加剤を必要
とけず、油分のみを除去できるため水以外に有用成分を
含む処理水からの油分除去に適している。
Furthermore, the water-oil-water flash 1 apparatus does not require any additives and can remove only oil during oil-water separation, so it is suitable for removing oil from treated water that contains useful components other than water.

以下、実施例により説明する。Examples will be explained below.

第1表              第2表COO<化
学的酸素要求m) :同上 SS(懸濁物rf1>        :同上ht+分
            :同上固形分       
    :同上 本発明の実施例に示づ油水分#l装置の側面図を第1図
に1K111Ii面図を第2図に示す。
Table 1 Table 2 COO<Chemical oxygen demand m): Same as above SS (Suspension rf1>: Same as above ht+min: Same as above Solid content
1K111Ii side view is shown in FIG. 1, and FIG. 2 is a side view of the oil/water #l apparatus shown in the embodiment of the present invention.

この油水分装置は処理水を導入でる導入孔11をもち、
最下部に設けられ油水導入室1、その上方に段t)られ
た流動床室2、さらにその上方に設置ノられ油分の除去
された水を排出りる重水導出孔31をもつ排水空3、さ
らにその上方に設置ノられ充填材41が配置された油分
捕集室4、イして最1部に設(プられた油浮上室5を有
する。 Lの流動床室2とと1目乎上空5とは導水路6
で連結されている。なお、流動床室2とiJl水窄3ど
はイ1切板32で水密的に区画されている。また、流動
床全2はその上端と下端にフィルタ21.22が設りら
れ、)ん動床室2に配置される油分粗大化媒体の粒子を
流動床v2内にとどめるとともに、処理水を自由(こ通
過できる構成としでいる。なお、油浮上室5の=L方に
(J粗大化し−C凝集した油分を取り除く油導出[」5
1が設【)Iうれでいる。油導出口51J:すill出
される油分は送油管52より油タンク(図示け?J′)
に送られる。油分捕集室/1. K1配rされてる充填
材/1.1としては、水の流通抵抗が比較的少なく、か
つ、接触面積の大ぎい布状(゛、かつ、パイプ形状に成
形されIζζダラシリング採用されている。また流動床
室2内には親水性のアクリル系樹脂と親油性のゴム成分
とを含む直径5〜(3n1m、、良さ3〜4mmの粒状
媒体が挿入されている。
This oil/water device has an introduction hole 11 through which treated water can be introduced,
An oil water introduction chamber 1 provided at the bottom, a fluidized bed chamber 2 arranged in stages above it, and a drainage chamber 3 installed above it having a heavy water outlet hole 31 for discharging water from which oil has been removed. Further, there is an oil collection chamber 4 installed above the chamber 4 in which a filler 41 is arranged, and an oil floating chamber 5 installed in the first part. The sky 5 is the headrace waterway 6
are connected. Note that the fluidized bed chamber 2 and the iJl water tube 3 are partitioned watertightly by a cutting plate 32. In addition, filters 21 and 22 are installed at the upper and lower ends of the entire fluidized bed 2 to keep the particles of the oil coarsening medium placed in the perturbation bed chamber 2 within the fluidized bed v2, and to free the treated water. (The structure is such that it can pass through.In addition, in the =L direction of the oil floating chamber 5, there is an oil outlet [5
1 is set [)I am happy. Oil outlet 51J: The oil is discharged from the oil tank (see figure ?J') from the oil feed pipe 52.
sent to. Oil collection chamber/1. The filling material /1.1 arranged in K1 is a cloth-like material with relatively low water flow resistance and a large contact area, and is formed into a pipe shape and adopted as an Iζζ Darashi ring. A granular medium containing a hydrophilic acrylic resin and a lipophilic rubber component and having a diameter of 5 to 3 nm and a thickness of 3 to 4 mm is inserted into the fluidized bed chamber 2.

この油水分離装置は、水ポンプ(図示せず)により処理
水が送水管12から導入孔11を通り油水導入室1に送
りこまれ、その送水圧力により油水導入室1からフィル
タ21の網目を通って処理水が流動床室2内に導入され
ると、流動床室2内に配設されノこ粒状の媒体が処理水
の水流に押されて流動床室2内で流動し処理水と完全に
交りあう。
In this oil-water separator, treated water is sent from a water pipe 12 through an introduction hole 11 to an oil-water introduction chamber 1 by a water pump (not shown), and the water is sent from the oil-water introduction chamber 1 through a mesh of a filter 21 by the water pressure. When the treated water is introduced into the fluidized bed chamber 2, the saw granular medium disposed in the fluidized bed chamber 2 is pushed by the water flow of the treated water and flows in the fluidized bed chamber 2, completely mixing with the treated water. Intersect.

この状態で処理水中に含;(、れる油分は媒体の表面に
接触し、表面に吸着され、媒体表面で粗大化づる。粗大
化した油分は媒体の表面の所々に顔を出している親水性
の樹脂の作用により媒体より分−1し離れる。この結果
処理水中には微小な油分が減少し、粗大化されて大ぎく
なった油分が存在するようになる。この流動床室2から
上方のフィルタ22を通り、粗大化しlζ油分を含む処
理水の力が導水路6を通って油浮上室5に送られる。油
浮上室5では、粗大化し!、二部が上方に移行してその
一1部に集まる。油分を除去された処理水(。上方向を
変え(油滓、J室5を下方に移1FIJリ−る。そして
油分捕集室4に入り処理水中に残存する油分は充填月4
1の表面に衝突して除去され、はぼ処理水のみどなって
排水室3に送られる。この排水室3から水害出孔31を
通り、送水管32により貯蔵槽(図示せず)に送られる
In this state, the oil contained in the treated water comes into contact with the surface of the medium, is adsorbed to the surface, and becomes coarse on the surface of the medium. Due to the action of the resin, it is separated from the medium by 1 minute.As a result, the minute oil content in the treated water decreases, and the oil content becomes coarse and large. The force of the treated water, which has become coarse and contains lζ oil, passes through the filter 22 and is sent through the water conduit 6 to the oil flotation chamber 5.In the oil flotation chamber 5, the coarsened! The treated water from which oil has been removed is collected in 1 part. Change the upward direction (move the soapstock, J chamber 5 downwards and 1 FIJ leak.Then, it enters the oil collection chamber 4 and the remaining oil in the treated water is filled. Month 4
The treated water collides with the surface of the container 1 and is removed, and the treated water is sent to the drainage chamber 3 as a slurry. From this drainage chamber 3, water passes through a water damage outlet 31 and is sent to a storage tank (not shown) via a water pipe 32.

なa3、本実施例の油水分#を装置を用いて、処理水中
の油分のみを除去した結果を説明づる。
A3. The results of removing only the oil in the treated water using the oil/water # apparatus of this example will be explained.

処理水としてはアルミホイール製造1稈のダイカス(−
マシンのビット内に溜った塗型液廃液から浮」二部を分
出11シた、微細な油分が分散した処理水を用いた。
As treated water, aluminum wheel manufacturing single culm die cast (-
Two parts of the floating mold solution collected in the bit of the machine were separated and treated water containing fine oil particles dispersed therein was used.

本実施例の装置で処理づる前の処理水の4(l状を第1
表に示す。この処理水を1分間5リツ1ヘルの割合で処
理し、油分を除去した。油分除去後の処理水の性状を第
2表に示す。第2表より塗型液の有効成分である黒鉛粒
子を除去することなく、また、他に成分を添加づ−るこ
となく油分のみが効果的に除去されているのがわかる。
The treated water before being treated with the apparatus of this example is
Shown in the table. This treated water was treated at a rate of 5 liters and 1 hour for 1 minute to remove oil. Table 2 shows the properties of the treated water after oil removal. It can be seen from Table 2 that only the oil was effectively removed without removing the graphite particles, which are the active ingredients of the coating liquid, and without adding any other ingredients.

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

図は本発明の実施例に示した油水分離装置を示し、第1
図はぞの側面図、第2図はで−の4i11断面図である
。 1・・・油水導入室     2・・・流動床室3・・
・JJI水室       4・・・油分捕集室5・・
・油滓上空 Qh Fl出願人  トヨタ自動車株式会社同    
豊和商事株式会社 代理人  弁理士  大川 宏 同   弁理士  藤谷 修 同   弁理士  九山明夫 第1図 32
The figure shows an oil-water separator according to an embodiment of the present invention.
The figure is a side view, and the second figure is a 4i11 cross-sectional view. 1... Oil/water introduction chamber 2... Fluidized bed chamber 3...
・JJI water chamber 4...Oil collection chamber 5...
・Summer Qh Fl Applicant: Toyota Motor Corporation
Howa Shoji Co., Ltd. Agent Patent attorney Hirodo Okawa Patent attorney Shudo Fujitani Patent attorney Akio Kuyama Figure 1 32

Claims (1)

【特許請求の範囲】[Claims] (1)塔状でその下方より上方に、導入孔をbつ油水導
入室、流動床室、水導出孔をもつ排水室、油分捕集室、
上方に油導出孔をもつ油浮上室をもち、 上記流動床室はそのL端と下端に、各々設Gノられたフ
ィルタで区画され、かつ該流動床室には親水性樹脂と新
油性樹脂とで構成された粒状の油分吸着粗大化媒体が流
動状態で配置され、1記流動床掌の上方フィルタと上記
排水室とは底板で水密的に封鎖され、かっこの底板を貫
通し、下方フィルタの上方と上記油浮上室とを連通覆る
導水路が形成され、 上記油分捕集室には充rt祠が配置さ41だ構造をもち
、 油を含む水が油水導入室より下方フィルタを通って流動
床室に入り、該流動床室で油が油分吸着粗大化媒体に吸
着され粗大化されて分離し、粗大化された油を含む水が
」一方フィルタを通り、さらに導水路を通って油浮上室
に入り、この油浮上室で油を浮上させ、油のみを油導出
孔にり排出し、水を下方に流し、油分捕集室を通り、水
中に残った油を充填材の表面に吸着させて取り除き、さ
らに下方に流れて排水室に入り、この排水室より水心出
孔に排出されるJ、うに構成されたことを特徴とする油
水分離装置。
(1) A tower-shaped oil-water introduction chamber with two introduction holes from the bottom to the top, a fluidized bed chamber, a drainage chamber with water outlet holes, an oil collection chamber,
The fluidized bed chamber has an oil floating chamber with an oil outlet hole in the upper part, and the fluidized bed chamber is divided by filters installed at the L and lower ends thereof, and the fluidized bed chamber contains a hydrophilic resin and a new oil-based resin. A granular oil-adsorbing coarsening medium consisting of 1) is arranged in a fluidized state, and the upper filter of the fluidized bed palm and the drainage chamber are watertightly sealed by a bottom plate, and the lower filter passes through the bottom plate of the bracket. A water conduit is formed that communicates with and covers the upper part of the oil floating chamber, and the oil collecting chamber has a structure in which a filling tank is arranged so that water containing oil flows from the oil-water introduction chamber through the lower filter. The oil enters the fluidized bed chamber, and in the fluidized bed chamber, the oil is adsorbed by the oil adsorption coarsening medium, coarsened, and separated, and the water containing the coarsened oil passes through a filter, and then passes through a water conduit to absorb the oil. Enter the floating chamber, float the oil in this oil floating chamber, discharge only the oil through the oil outlet hole, let the water flow downward, pass through the oil collection chamber, and the oil remaining in the water will be brought to the surface of the filler. An oil/water separator characterized in that the water is adsorbed and removed, flows further downward into a drainage chamber, and is discharged from the drainage chamber to a central outlet hole.
JP616683A 1983-01-18 1983-01-18 Oil-water separating device Pending JPS59130506A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP616683A JPS59130506A (en) 1983-01-18 1983-01-18 Oil-water separating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP616683A JPS59130506A (en) 1983-01-18 1983-01-18 Oil-water separating device

Publications (1)

Publication Number Publication Date
JPS59130506A true JPS59130506A (en) 1984-07-27

Family

ID=11630944

Family Applications (1)

Application Number Title Priority Date Filing Date
JP616683A Pending JPS59130506A (en) 1983-01-18 1983-01-18 Oil-water separating device

Country Status (1)

Country Link
JP (1) JPS59130506A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04107349U (en) * 1991-02-26 1992-09-16 ミサワホーム株式会社 Wall panel steady rest jig
JP2008237265A (en) * 2007-03-26 2008-10-09 Mizuno Corp Track and field spike shoes

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04107349U (en) * 1991-02-26 1992-09-16 ミサワホーム株式会社 Wall panel steady rest jig
JP2008237265A (en) * 2007-03-26 2008-10-09 Mizuno Corp Track and field spike shoes

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