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JPS6151930B2 - - Google Patents

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Publication number
JPS6151930B2
JPS6151930B2 JP10629181A JP10629181A JPS6151930B2 JP S6151930 B2 JPS6151930 B2 JP S6151930B2 JP 10629181 A JP10629181 A JP 10629181A JP 10629181 A JP10629181 A JP 10629181A JP S6151930 B2 JPS6151930 B2 JP S6151930B2
Authority
JP
Japan
Prior art keywords
oil
separation chamber
water
net
water separator
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
Application number
JP10629181A
Other languages
Japanese (ja)
Other versions
JPS588518A (en
Inventor
Kiichi Tanaka
Noboru Gomyo
Hiromichi Shimomura
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.)
Nittan Co Ltd
Original Assignee
Nittan 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 Nittan Co Ltd filed Critical Nittan Co Ltd
Priority to JP10629181A priority Critical patent/JPS588518A/en
Publication of JPS588518A publication Critical patent/JPS588518A/en
Publication of JPS6151930B2 publication Critical patent/JPS6151930B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】[Detailed description of the invention]

この発明は、機械工場、ガソリンスタンド、金
属表面処理工場、食品加工工場等から排出される
含油廃水中の油分を分離・除去、浄化する油水分
離装置に関する。 従来より含油廃水中の油分を回収する装置とし
て、動力を使用せずに油と水の比重差を利用し、
さらに水位差によつて油分を浮上分離する油水分
離装置が知られており、この装置は第1図に示す
ように構成されている。すなわち、前受槽(図示
せず)に貯留した含油廃水を導入する導入口1、
第1の分離室2、溢流孔31を穿設した第2の分
離室3、グラスウールロツク又はラツシヒリング
状のもの等の繊維質を充填した粗粒化装置4、第
3の分離室5、鋼板製の複数の傾斜板6、第4の
分離室7、吸着室8、排出口9とから成つてい
る。なお、第2分離室3と吸着室8との間は、水
位差を与えるためのパイプ10により連結されて
いる。 以上のように構成された従来の油水分離装置に
おいては、水位の変化によつて溢流孔31の調整
板32の位置を調整しなければならない欠点があ
つた。また、粗粒化装置4及び吸着剤を設けた吸
着室8などの複雑な構造のものを必要とし、製
造、メンテナンスにおいて費用がかさむ欠点があ
つた。 この発明は、以上の問題を解決するために考え
られたものであつて、次にこの発明の油水分離装
置を図面に基づいて詳細に説明する。 第2図は、この発明の油水分離装置の一実施例
を示す全体を透視した斜視図、第3図は、透視し
た状態の正面図、第4図は、平面図であつて前受
槽(図示せず)に貯留した含油廃水を導入する導
入口1、第1の分離室2、第2の分離室3、第1
の油捕集槽4、第3の分離室5、傾斜板6、第4
の分離室7、第5の分離室8、第2の油捕集槽
9、排出口10とから成つている。第1の分離室
2、第1の油捕集槽4、第5の分離室8、第2の
油捕集槽9の各区画壁には、それぞれ溢流孔3
1,32,41,81,91が穿設され、これら
の溢流孔にはネツト11が張設されている。これ
らのネツト11はポリテトラフルオロエチレン等
のフツ素系樹脂あるいはシリコーン樹脂の繊維を
網状に形成したものか、または金属製の網にこれ
らの樹脂をコーテイングしたものを用い、溢流孔
31,32,81のネツトは30〜120メツシユの
もの、溢流孔41,91のネツトは120〜150メツ
シユのものを用いるのが好ましい。さらに傾斜板
6は上記ネツト11と同じものであつて20〜40メ
ツシユのものを用い、一定間隔をおいて平行に複
数枚重ねて形成する。これらのネツト11及び傾
斜板6のフツ素系樹脂またシリコーン樹脂は、親
油性で疎水性であるので、油分のみを通す性質を
有している。 なお、第2の分離室3と第4の分離室7との間
は、水位差を与えるためのパイプ13により連結
されている。 以上のように構成されたこの発明の油水分離装
置における油水分離プロセスを説明すると、含油
廃水は導入口1と排出口10の水位差によつて、
上流側から下流側に流れる。導入口1より供給さ
れた含油廃水は、第1の分離室2において、水と
油の比重差により油分が分離浮上し、ネツト11
と溢流孔31を通り第2の分離室3に入る。分離
浮上しなかつた微粒油分を含む水は、第2の分離
室3の下端を潜つて第3の分離室5に入つて上昇
し、ネツト状の傾斜板6間を斜め下方に流下する
が、この時に油分は各傾斜板6間を通過上昇しな
がら粗粒化し、ストークスの原理に従つて第3の
分離室5の上部に浮上し、溢流孔32を通過して
第2の分離室3に流入する。このように第1の分
離室2及び第3の分離室5から第2の分離室3に
流入した油分は、溢流孔41を通過して第1の油
捕集槽4に貯留する。 次に傾斜板6を流下した含油廃水は、仕切板1
2に沿つて上昇し、第4の分離室7に流入する。
この第4の分離室7に流入した含油廃水は、油と
水に分離し、浮上した油分は溢流孔81を通過し
て第5の分離室8に流入し、さらに溢流孔91を
通過して第2の油捕集槽9において貯留する。最
後に水は第5の分離室8の下端を潜つて排出口1
0より排出される。 以上のようにして油は除去されるが、溢流孔3
1,32,41,81,91及び傾斜板6のネツ
ト11は、ゴミなど以外では目詰りすることがな
く、長期間使用することができ、目詰りしても取
りはずして洗浄すればよく、ネツトそのものが破
れない限り交換しなくても済み、保守メンテナン
ス上極めて有利である。なお、ゴミは前受槽にお
いてほとんど除去されているのが通常である。 次にこの発明の油水分離装置を用いて行なつた
実施例を示す。 実施例 1 この発明の油水分離装置に油の含まれていない
水を満して水位を調整した後、原水としてコンプ
レツサードレン廃水を1m3/hrの割合で通水し、
温度20℃で通水1時間後と50時間後における処理
水中の油分濃度を測定した。第1及び第5の分離
室の溢流孔ネツトは、ポリテトラフルオロエチレ
ン繊維で10,30,60,150メツシユのものを交互
に用いた。なお、傾斜板ネツトはいずれも30メツ
シユのポリテトラフルオロエチレン繊維のものを
用いた。その結果を下記表に示す。
The present invention relates to an oil-water separator that separates, removes, and purifies oil from oil-containing wastewater discharged from machine factories, gas stations, metal surface treatment factories, food processing factories, and the like. Traditionally, this device has been used to recover oil from oil-containing wastewater, using the difference in specific gravity between oil and water without using power.
Furthermore, an oil/water separator is known in which oil is floated and separated by a water level difference, and this apparatus is constructed as shown in FIG. That is, an inlet 1 for introducing oil-containing wastewater stored in a pre-receiving tank (not shown);
A first separation chamber 2, a second separation chamber 3 with an overflow hole 31, a coarsening device 4 filled with fibrous material such as glass wool lock or Raschig ring, a third separation chamber 5, and a steel plate. It consists of a plurality of inclined plates 6, a fourth separation chamber 7, an adsorption chamber 8, and a discharge port 9. Note that the second separation chamber 3 and the adsorption chamber 8 are connected by a pipe 10 for providing a water level difference. The conventional oil-water separator configured as described above has a drawback in that the position of the adjustment plate 32 of the overflow hole 31 must be adjusted depending on changes in the water level. Further, it requires a complicated structure such as a coarsening device 4 and an adsorption chamber 8 provided with an adsorbent, which has the disadvantage of increasing manufacturing and maintenance costs. The present invention has been devised to solve the above problems, and the oil/water separator of the present invention will now be described in detail based on the drawings. FIG. 2 is a perspective view of the entire oil-water separator according to an embodiment of the present invention, FIG. 3 is a front view of the oil-water separator according to the present invention, FIG. an inlet 1 for introducing oil-containing wastewater stored in a tank (not shown), a first separation chamber 2, a second separation chamber 3, a first
oil collection tank 4, third separation chamber 5, inclined plate 6, fourth
It consists of a separation chamber 7, a fifth separation chamber 8, a second oil collection tank 9, and a discharge port 10. Each partition wall of the first separation chamber 2, first oil collection tank 4, fifth separation chamber 8, and second oil collection tank 9 has an overflow hole 3.
1, 32, 41, 81, and 91 are drilled, and a net 11 is stretched over these overflow holes. These nets 11 are made of fibers of fluorocarbon resin such as polytetrafluoroethylene or silicone resin formed into a net shape, or metal nets coated with these resins, and overflow holes 31, 32 are used. , 81 are preferably of 30 to 120 mesh, and the overflow holes 41 and 91 are preferably of 120 to 150 mesh. Further, the inclined plates 6 are made of the same material as the net 11 and have a mesh size of 20 to 40, and are formed by stacking a plurality of them in parallel at regular intervals. The fluororesin or silicone resin of the net 11 and the inclined plate 6 is lipophilic and hydrophobic, and thus has the property of allowing only oil to pass through. Note that the second separation chamber 3 and the fourth separation chamber 7 are connected by a pipe 13 for providing a water level difference. To explain the oil-water separation process in the oil-water separator of the present invention configured as described above, oil-containing wastewater is separated by the water level difference between the inlet 1 and the outlet 10.
Flows from upstream to downstream. The oil-containing wastewater supplied from the inlet 1 is separated and floated to the surface in the first separation chamber 2 due to the difference in specific gravity between water and oil.
and enters the second separation chamber 3 through the overflow hole 31. The water containing particulate oil that has not separated and floated to the surface sneaks under the lower end of the second separation chamber 3, enters the third separation chamber 5, rises, and flows diagonally downward between the net-shaped inclined plates 6. At this time, the oil becomes coarse particles as it passes between the inclined plates 6 and rises, floats to the upper part of the third separation chamber 5 according to Stokes' principle, passes through the overflow hole 32, and flows into the second separation chamber 3. flows into. The oil that has flowed into the second separation chamber 3 from the first separation chamber 2 and the third separation chamber 5 in this way passes through the overflow hole 41 and is stored in the first oil collection tank 4 . Next, the oil-containing wastewater flowing down the inclined plate 6 is transferred to the partition plate 1
2 and flows into the fourth separation chamber 7.
The oil-containing wastewater that has flowed into the fourth separation chamber 7 is separated into oil and water, and the oil that has floated to the surface passes through the overflow hole 81 and flows into the fifth separation chamber 8, and further passes through the overflow hole 91. The oil is then stored in the second oil collection tank 9. Finally, the water passes through the lower end of the fifth separation chamber 8 and exits through the outlet 1.
Ejected from 0. Although the oil is removed in the above manner, the overflow hole 3
1, 32, 41, 81, 91 and the net 11 of the inclined plate 6 will not be clogged by anything other than dirt and can be used for a long period of time. There is no need to replace it unless it breaks, which is extremely advantageous in terms of maintenance. Note that most of the dust is usually removed in the pre-receiving tank. Next, examples will be shown in which the oil-water separator of the present invention was used. Example 1 After filling the oil-water separator of the present invention with oil-free water and adjusting the water level, compressor drain wastewater was passed through as raw water at a rate of 1 m 3 /hr,
The oil concentration in the treated water was measured 1 hour and 50 hours after water flow at a temperature of 20°C. For the overflow hole nets of the first and fifth separation chambers, polytetrafluoroethylene fibers of 10, 30, 60, and 150 mesh were used alternately. The inclined plate nets were all made of 30 mesh polytetrafluoroethylene fibers. The results are shown in the table below.

【表】 実施例 2 実施例1と同一条件で、ネツトをシリコーン樹
脂繊維を用いて処理水中の油分濃度を測定した。
その結果を下記表に示す。
[Table] Example 2 The oil concentration in the treated water was measured under the same conditions as in Example 1 using a silicone resin fiber net.
The results are shown in the table below.

【表】 以上の結果から明らかなように、この発明の油
水分離装置は、長時間連続運転しても処理水中の
油分濃度が増えることがない。各分離室のネツト
の網目は、30〜150メツシユ程度のものが最適で
あり、150メツシユ以上では処理水中の油分濃度
が極端に増えることがないが、非常に微粒のゴミ
によつて目詰りするおそれがある。また各油捕集
槽の溢流孔のネツトの網目は油のみを通し水を通
さないことを条件に、上記したように分離室の溢
流孔ネツトより細かいものを使用した方がよい。
傾斜板のネツトは、油をできるだけ大きく粗粒化
して分離浮上させるために、20〜40メツシユと粗
い網目のものが好適である。 以上で説明したように、この発明の油水分離装
置によれば、従来のように水位の変化によつて溢
流孔の調整板を調整することもなく、かつ、ネツ
トそのものが油水分離を行なうフイルターとして
も機能させるようにしたものであるから、保守管
理上極めて有利である。また、油水分離を行ない
油を粗粒化させる傾斜板も、ネツト状に形成する
ことによつて、従来のように粗粒化装置を必要と
しないので、製造上有利である等の優れた効果を
奏するのである。
[Table] As is clear from the above results, the oil-water separator of the present invention does not increase the oil concentration in the treated water even when operated continuously for a long time. The mesh size of each separation chamber is optimally between 30 and 150 meshes; if the mesh size is more than 150 meshes, the oil concentration in the treated water will not increase dramatically, but it will become clogged with very fine particles. There is a risk. Further, it is preferable to use a mesh of the overflow hole of each oil collection tank that is finer than that of the overflow hole of the separation chamber, as described above, on the condition that only oil passes through and water does not pass through.
The net of the inclined plate preferably has a coarse mesh of 20 to 40 mesh in order to coarsen the oil as much as possible and separate and float it. As explained above, according to the oil-water separator of the present invention, there is no need to adjust the adjustment plate of the overflow hole according to changes in water level as in the conventional case, and the net itself is a filter that separates oil and water. It is extremely advantageous in terms of maintenance and management, since it is designed to function as a system. In addition, the inclined plate that separates oil and water and coarsens the oil is formed into a net shape, which eliminates the need for a coarsening device as in the past, resulting in superior effects such as manufacturing advantages. It is played.

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

第1図は従来の油水分離装置を示す透視した状
態の正面図、第2図はこの発明の油水分離装置の
一実施例を示す全体を透視した斜視図、第3図は
透視した正面図、第4図は平面図である。 1…導入口、2・3・5・7・8…分離室、
4・9…油捕集槽、6…傾斜板、10…排出口、
11…ネツト、31・32・41・81・91…
溢流孔。
FIG. 1 is a transparent front view showing a conventional oil-water separator, FIG. 2 is a perspective view showing an embodiment of the oil-water separator of the present invention, and FIG. 3 is a transparent front view. FIG. 4 is a plan view. 1...Inlet, 2, 3, 5, 7, 8... Separation chamber,
4.9...oil collection tank, 6...slanted plate, 10...discharge port,
11...net, 31, 32, 41, 81, 91...
Overflow hole.

Claims (1)

【特許請求の範囲】[Claims] 1 含油廃水の導入口から排出口までの水位差に
より流れが生ずる油水分離装置であつて、上流側
から下流側に沿つて複数の油水分離室と複数の油
捕集槽と平行配列された複数の傾斜板とを配置
し、上記油水分離室及び油捕集槽に穿設された溢
流孔にフツ素系樹脂またはシリコーン樹脂製のネ
ツトを張設し、かつ上記複数の傾斜板を上記ネツ
トで形成してなることを特徴とする油水分離装
置。
1. An oil-water separator in which a flow is generated due to a water level difference between the inlet and the outlet of oil-containing wastewater, which includes a plurality of oil-water separation chambers and a plurality of oil collection tanks arranged in parallel from the upstream side to the downstream side. A net made of fluororesin or silicone resin is stretched over the overflow holes drilled in the oil/water separation chamber and the oil collection tank, and the plurality of inclined plates are connected to the net. An oil-water separator characterized by being formed of.
JP10629181A 1981-07-09 1981-07-09 Apparatus for separating oil and water Granted JPS588518A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10629181A JPS588518A (en) 1981-07-09 1981-07-09 Apparatus for separating oil and water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10629181A JPS588518A (en) 1981-07-09 1981-07-09 Apparatus for separating oil and water

Publications (2)

Publication Number Publication Date
JPS588518A JPS588518A (en) 1983-01-18
JPS6151930B2 true JPS6151930B2 (en) 1986-11-11

Family

ID=14429947

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10629181A Granted JPS588518A (en) 1981-07-09 1981-07-09 Apparatus for separating oil and water

Country Status (1)

Country Link
JP (1) JPS588518A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001219002A (en) * 2000-02-07 2001-08-14 Tc:Kk Liquid separation device

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3229897B2 (en) * 1992-04-13 2001-11-19 三菱電機株式会社 Three-level three-phase inverter device
JP2568838Y2 (en) * 1992-12-24 1998-04-15 リズム時計工業株式会社 Clock display
JP6956978B2 (en) * 2019-06-21 2021-11-02 アサダメッシュ株式会社 Coaressa and oil / water separator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001219002A (en) * 2000-02-07 2001-08-14 Tc:Kk Liquid separation device

Also Published As

Publication number Publication date
JPS588518A (en) 1983-01-18

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