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JPH0225644B2 - - Google Patents
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JPH0225644B2 - - Google Patents

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Publication number
JPH0225644B2
JPH0225644B2 JP61019821A JP1982186A JPH0225644B2 JP H0225644 B2 JPH0225644 B2 JP H0225644B2 JP 61019821 A JP61019821 A JP 61019821A JP 1982186 A JP1982186 A JP 1982186A JP H0225644 B2 JPH0225644 B2 JP H0225644B2
Authority
JP
Japan
Prior art keywords
oil
water
net
separating
separation
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 - Lifetime
Application number
JP61019821A
Other languages
Japanese (ja)
Other versions
JPS62176509A (en
Inventor
Keizo Hara
Shigehiro Imai
Mikio Sato
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.)
Wako Sangyo KK
Idemitsu Petrochemical Co Ltd
Mitsui Zosen KK
Original Assignee
Wako Sangyo KK
Idemitsu Petrochemical Co Ltd
Mitsui Zosen KK
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 Wako Sangyo KK, Idemitsu Petrochemical Co Ltd, Mitsui Zosen KK filed Critical Wako Sangyo KK
Priority to JP1982186A priority Critical patent/JPS62176509A/en
Publication of JPS62176509A publication Critical patent/JPS62176509A/en
Publication of JPH0225644B2 publication Critical patent/JPH0225644B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、水分を含有する油液から水分を分離
する油水分離方法およびその装置に関する。詳し
くは、ナフサの熱分解によつて得られる熱分解油
等から、それに含有する微小なごみを含む水分を
分離する方法およびその装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an oil-water separation method and apparatus for separating water from an oil liquid containing water. More specifically, the present invention relates to a method and an apparatus for separating water containing fine dust from pyrolysis oil obtained by pyrolysis of naphtha.

〔背景技術とその問題点〕[Background technology and its problems]

石油工業や石油化学工業等の分野において、油
液中に含まれる遊離水分を除去することは、極め
て重要な操作である。
In fields such as the petroleum industry and petrochemical industry, removing free water contained in oil liquid is an extremely important operation.

従来、油液中に含まれる遊離水分を除去する方
法としては、その油液を、濾材、具体的にはグラ
スフアイバ等の親水性濾材を多層に巻いたものに
通過させ、油液が濾材の層間を通過する際に、濾
材のもつ固有機能を、液−液間の界面張力、、比
重差等により微量の遊離水分を凝集分離する方法
が知られている。
Conventionally, as a method for removing free water contained in an oil liquid, the oil liquid is passed through a filter medium, specifically, a hydrophilic filter medium such as glass fiber wrapped in multiple layers. A method is known in which a minute amount of free water is coagulated and separated using the unique functions of the filter medium, such as the interfacial tension between liquid and liquid, and the difference in specific gravity, when passing between layers.

しかし、この凝集分離方法は、油液中に含まれ
る微小なごみが濾材を閉塞してしまう結果、短期
間でその分離機能が損なわれる欠点があつた。
However, this agglomeration separation method has the disadvantage that the filter medium is clogged with minute dust contained in the oil liquid, and as a result, its separation function is impaired in a short period of time.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、このような点を改善すべくな
されたもので、油水分離効果に優れ、かつその油
水分離効果を長期間維持できる油水分離方法およ
び装置を提供することにある。
An object of the present invention is to provide an oil-water separation method and apparatus which have an excellent oil-water separation effect and can maintain the oil-water separation effect for a long period of time.

〔問題点を解決するための手段およびその作用〕[Means for solving problems and their effects]

まず、本発明の油水分離方法は、水分を含有す
る油液、例えば、ナフサの熱分解によつて得られ
る熱分解油の油分を、撥水性を有する円筒形状の
網を通過させて、油液中の水分を分離することを
特徴とする。
First, in the oil-water separation method of the present invention, an oil liquid containing water, for example, the oil content of pyrolyzed oil obtained by thermal decomposition of naphtha, is passed through a water-repellent cylindrical net. It is characterized by separating the moisture inside.

また、本発明の油水分離装置は、水分を含有す
る油液から水分を分離する装置において、撥水性
を有する円筒形状の網を含む分離手段と、この分
離手段の網の外周面に前記油液を送液する手段
と、分離手段の網を通過した油液中の油分を集油
する手段と、分離手段の網を通過できない油液中
の水分を集水する手段とを備えたことを特徴とす
る。
The oil-water separator of the present invention is an apparatus for separating water from an oil containing water, and includes a separation means including a cylindrical net having water repellency, and an outer circumferential surface of the net of the separation means for separating water from an oil containing water. A means for sending liquid, a means for collecting oil in the oil liquid that has passed through the net of the separating means, and a means for collecting water in the oil liquid that cannot pass through the net of the separating means. shall be.

以下、本発明を詳述する。 The present invention will be explained in detail below.

まず、本発明において、撥水性を有する網と
は、少なくとも表面に撥水性を備えていればよ
く、例えば、金網に撥水性素材をコーテイング処
理したものも含む。
First, in the present invention, the term "water-repellent net" is sufficient as long as it has water-repellent properties at least on its surface, and includes, for example, a wire net coated with a water-repellent material.

ここで、金網のサイズとしては、油液中の遊離
水分量やごみの粒径および量に応じて適宜選定す
ればよいが、通常、100〜300メツシユが好適であ
る。また、撥水性素材としては、ポリフツ化エチ
レン系樹脂が好適である。
Here, the size of the wire mesh may be appropriately selected depending on the amount of free water in the oil and the particle size and amount of dirt, but 100 to 300 mesh is usually suitable. Further, as the water-repellent material, polyethylene fluoride resin is suitable.

網が撥水性を備えているため、油液中の油分が
網を通過する際、水分は網のもつ撥水性により弾
かれ、ここで油水分離される。撥水性の網によつ
て弾かれた水分は、凝集しながら水滴となり、網
の表面を滑りながら落下する。一方、油液中の微
小のごみは網の表面に捕捉されるが、水滴の落下
に伴つて洗い流されるので、目づまりを起こすこ
とがなく高い油水分離効果を長期間維持させるこ
とができる。
Since the net has water-repellent properties, when the oil in the oil passes through the net, water is repelled by the water-repellent property of the net, and the oil and water are separated here. The water that is repelled by the water-repellent net condenses into water droplets, which fall while sliding on the surface of the net. On the other hand, minute dirt in the oil liquid is captured on the surface of the screen, but is washed away as water droplets fall, so a high oil-water separation effect can be maintained for a long period of time without causing clogging.

なお、撥水性を有する網を円筒形状としたこと
は、送液された油液が網に衝突する際網を変形さ
せるのを防ぐ効果がある上、取り扱いが容易にな
り、特に、網の内側からパンチングメタル等で構
成した有孔の保持筒で保持すれば、強度的にも十
分で、かつ交換が容易なカートリツジとして構成
できる利点がある。なおかつ、目づまりが発生し
たときには、取外し洗浄して再使用できる。
The cylindrical shape of the water-repellent net has the effect of preventing the sent oil from deforming the net when it collides with the net, and also makes it easier to handle. If the cartridge is held by a perforated holding tube made of punched metal or the like, it has the advantage that it has sufficient strength and can be configured as a cartridge that is easy to replace. Moreover, when clogging occurs, it can be removed, cleaned, and reused.

〔実施例〕〔Example〕

第1図は本発明の油水分離装置の一例を示して
いる。同図において、縦長形状の分離塔11の内
部は、上下方向の中央位置より下方位置に設けら
れた仕切壁12により上下の室13,14に仕切
られている。上方の室13の上部側壁には、水分
を含有する油液、例えばナフサの熱分解によつて
得られる熱分解油を導入する油液導入口15が開
口されている。下方の室13の塔底には、油液か
ら水分が分離された油分を取出す油分取出口16
が開口されている。
FIG. 1 shows an example of an oil-water separator according to the present invention. In the figure, the inside of a vertically elongated separation column 11 is partitioned into upper and lower chambers 13 and 14 by a partition wall 12 provided below the center position in the vertical direction. An oil liquid inlet 15 is opened in the upper side wall of the upper chamber 13 to introduce an oil liquid containing water, such as pyrolysis oil obtained by thermal decomposition of naphtha. At the bottom of the lower chamber 13, there is an oil extraction port 16 for extracting oil from which water has been separated from the oil liquid.
is opened.

また、仕切壁12には、下方の室14を貫通し
て上方の室13内に貯つた水分を塔外へ取出す水
分取出管17が設けられているとともに、前記上
方の室13側へ向かつて垂直管18が設けられて
いる。垂直管18の底部は下方の室14に開口さ
れているとともに、垂直管18の上端部には油水
分離手段である分離筒19が締付ナツト20によ
り着脱自在に取付けられている。
Further, the partition wall 12 is provided with a moisture extraction pipe 17 that penetrates the lower chamber 14 and takes out the moisture accumulated in the upper chamber 13 to the outside of the tower, and a moisture extraction pipe 17 that penetrates the lower chamber 14 and takes out the moisture accumulated in the upper chamber 13 to the outside of the tower. A vertical tube 18 is provided. The bottom of the vertical pipe 18 is open to the chamber 14 below, and a separating cylinder 19 serving as oil/water separating means is detachably attached to the upper end of the vertical pipe 18 with a tightening nut 20.

分離筒19は、第2図に示す如く、パンチング
メタル(板に多数の孔を穿設した材料)によつて
構成された円筒形状の有孔の保持筒22と、この
保持筒22に複数の桟23を介して保持筒22の
外周に対して所定間隔に離れかつ囲むように配置
された円筒形状の網21とを備え、垂直管18に
して着脱できるカートリツジ状に構成されてい
る。網21には、例えば100〜300メツシユ程度の
金網に撥水性を有する素材、ここではポリフツ化
エチレン系樹脂をコーテイング処理したものが用
いられている。
As shown in FIG. 2, the separation tube 19 includes a cylindrical-shaped holding tube 22 made of punched metal (a material with many holes punched in a plate), and a plurality of holes in the holding tube 22. It is provided with a cylindrical mesh 21 arranged at a predetermined distance from and surrounding the outer periphery of the holding cylinder 22 via a crosspiece 23, and is configured in the shape of a cartridge that can be attached to and removed from the vertical tube 18. The mesh 21 is made of, for example, a wire mesh of about 100 to 300 meshes coated with a water-repellent material, here a polyfluorinated ethylene resin.

このような装置において、油水導入口15から
分離塔11内へ水分を含む油液が導入されると、
その油液中の油分は、分離塔19の網21および
保持筒22を順次通過した後、垂直管18を伝わ
つて下方の室14に貯えられる。室14内の油分
は、油分取出口16から取り出された後、次の処
理工程へ送られる。
In such an apparatus, when an oil liquid containing water is introduced into the separation column 11 from the oil/water inlet 15,
The oil in the oil liquid sequentially passes through the net 21 and holding cylinder 22 of the separation tower 19, and then travels through the vertical pipe 18 and is stored in the chamber 14 below. After the oil in the chamber 14 is taken out from the oil extraction port 16, it is sent to the next treatment step.

一方、油液中の水分は、油分が網21を通過す
る際、その網21のもつ撥水性により弾かれ、そ
の表面で凝集しながら水滴となり、網21の表面
を滑りながら落下するので、ここで油液中の油分
と水分とが分離される。
On the other hand, when the oil passes through the net 21, the water in the oil is repelled by the water repellency of the net 21, condenses on its surface, becomes water droplets, and falls while sliding on the surface of the net 21. The oil and water in the oil liquid are separated.

この際、油液中に含まれる微小なごみは網21
の表面に捕捉されるが、、水滴が網21の表面を
滑りながら落下するとき、微小なごみも洗い流さ
れるため、目づまりを生じることなく、長期間高
い油水分離効果を維持できる。
At this time, the minute dust contained in the oil liquid is removed from the screen 21.
However, when the water droplets slide down the surface of the net 21, minute dirt is also washed away, so that a high oil-water separation effect can be maintained for a long period of time without causing clogging.

ごみを含んだ水分は、網21の表面を滑りなが
ら流れ落ちた後、上方の室13の底部に貯えら
れ、水分取出口17から適宜取出される。
After the water containing dust flows down the surface of the screen 21, it is stored at the bottom of the upper chamber 13 and taken out from the water outlet 17 as appropriate.

次に、第1図および第2図に示す油水分離装置
を、ナフサの熱分解処理プロセスに適用した例を
第3図について説明する。
Next, an example in which the oil/water separator shown in FIGS. 1 and 2 is applied to a naphtha thermal decomposition process will be described with reference to FIG. 3.

まず、原料であるナフサを熱分解炉31で熱分
解する。熱分解炉31より得られたガスは、二次
反応を防ぐために急冷器32で急冷された後、オ
イル冷却塔33へ導入され、ここで次段の水冷却
塔34からリサイクルされる熱分解油により分解
重油が液化分離される。この分解重油は塔底から
抜出される。
First, naphtha, which is a raw material, is pyrolyzed in a pyrolysis furnace 31. The gas obtained from the pyrolysis furnace 31 is rapidly cooled in a quencher 32 to prevent secondary reactions, and then introduced into an oil cooling tower 33, where the pyrolysis oil is recycled from the next stage water cooling tower 34. The cracked heavy oil is liquefied and separated. This cracked heavy oil is extracted from the bottom of the tower.

オイル冷却塔33の塔頂から抜出されたガス
は、水冷却塔34へ導入され、外部より注入され
る水により熱分解油が液化分離される。この熱分
解油と水との油水混合液は、複数枚の案内板35
により案内されながら、多数の波板を積層した
CPIセパレータ36へ導入され、水と熱分解油と
に分離される。水は塔底から図示しないポンプ等
により抜き出される。なお、ここで生じたスラツ
ジはスラツジチヤンバ36Aに排出される。
The gas extracted from the top of the oil cooling tower 33 is introduced into the water cooling tower 34, where the pyrolysis oil is liquefied and separated by water injected from the outside. This oil-water mixture of pyrolysis oil and water is passed through a plurality of guide plates 35.
A large number of corrugated sheets were laminated while being guided by
It is introduced into the CPI separator 36 and separated into water and pyrolysis oil. Water is extracted from the bottom of the tower by a pump or the like (not shown). Note that the sludge generated here is discharged into the sludge chamber 36A.

一方、CPIセパレータ36で分離された熱分解
油の一部はポンプ等によつて前記オイル冷却塔3
3へリサイクルされるが、残りはクーラ37で冷
却された後、本発明の油水分離装置へ送られ、そ
こで油水分離される。
On the other hand, a part of the pyrolysis oil separated by the CPI separator 36 is transferred to the oil cooling tower 3 by a pump or the like.
However, the remainder is cooled in a cooler 37 and then sent to the oil-water separator of the present invention, where it is separated from oil and water.

この処理プロセスにおいて、水冷却塔34で油
水分離された熱分解油(約85℃)中には、約0.1
重量%の遊離水分と、0.43重量%の熱分解油の飽
和溶解水分とが含まれている。これを、クーラ3
7で約35℃まで冷却すると、熱分解油に対する水
の溶解度が低下し、遊離水分が約0.40重量%、飽
和溶解水分量が0.13重量%となる。約0.40重量%
の遊離水分を含んだ熱分解油を、150メツシユの
撥水性を有する網21を備えた油水分離装置に通
過させる。
In this treatment process, about 0.1
It contains % free water by weight and 0.43% by weight saturated dissolved water of the pyrolysis oil. Cooler 3
7, the solubility of water in the pyrolysis oil decreases to about 0.40% by weight of free water and 0.13% by weight of saturated dissolved water. Approximately 0.40% by weight
The pyrolysis oil containing free water is passed through an oil-water separator equipped with a 150-mesh water-repellent screen 21.

熱分解油中に含まれる微小のごみは、25μ以下
のものが220個/ml、25μより大きいものが15
個/mlであり、その大部分が網21を通過する。
一部の大きいごみは、網21に捕捉されるが、凝
集した水滴が落下するときに洗い流されるので、
油水分離装置の網21は油水分離機能を1年間保
持することができ、その間分離筒19を全く交換
する必要がなかつた。また、油分取出口16の熱
分解油中の遊離水分は0.05重量%以下に減少し
た。
The microscopic debris contained in pyrolysis oil is 220 pieces/ml of particles less than 25μ, and 15 pieces/ml of particles larger than 25μ.
/ml, most of which passes through the net 21.
Some large debris is captured by the net 21, but it is washed away when the aggregated water droplets fall.
The network 21 of the oil-water separator was able to maintain its oil-water separation function for one year, and there was no need to replace the separation tube 19 at all during that time. Furthermore, the free water content in the pyrolysis oil at the oil extraction port 16 was reduced to 0.05% by weight or less.

〔発明の効果〕〔Effect of the invention〕

以上の通り、本発明によれば、油水分離効果に
優れ、かつその油水分離効果を長期間維持できる
油水分離方法および装置を提供することができ
る。
As described above, according to the present invention, it is possible to provide an oil-water separation method and apparatus that have excellent oil-water separation effects and can maintain the oil-water separation effects for a long period of time.

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

第1図は本発明の油水分離装置の一実施例を示
す図、第2図は分離筒を示す図、第3図は本発明
の油水分離装置を用いたナフサの熱分解処理プロ
セスを示すフロー図である。 11……分離塔、15……送液手段としての油
液導入口、16……集油手段としての油分取出
口、17……集水手段としての水分取出口、19
……分離手段としての分離筒、21……網、22
……保持筒。
Fig. 1 is a diagram showing an embodiment of the oil-water separator of the present invention, Fig. 2 is a diagram showing a separation cylinder, and Fig. 3 is a flowchart showing a naphtha pyrolysis treatment process using the oil-water separator of the present invention. It is a diagram. DESCRIPTION OF SYMBOLS 11...Separation tower, 15...Oil liquid inlet as liquid feeding means, 16...Oil extraction port as oil collection means, 17...Moisture extraction port as water collection means, 19
... Separation cylinder as separation means, 21 ... Net, 22
...Holding tube.

Claims (1)

【特許請求の範囲】 1 水分を含有する油液から水分を分離する油水
分離方法において、前記油液中の油分を、有孔の
保持筒で保持され、撥水性素材がコーテイングさ
れた円筒形状の網を通過させて、油液中の水分を
分離することを特徴とする油水分離方法。 2 特許請求の範囲第1項において、前記油液
が、ナフサの熱分解によつて得られる熱分解油で
あることを特徴とする油水分離方法。 3 水分を含有する油液から水分を分離する装置
において、有孔の保持筒と撥水性素材がコーテイ
ングされた円筒形状の網を含む分離手段と、この
分離手段の網の外周面に前記油液を送液する手段
と、分離手段の網を通過した油液中の油分を集油
する手段と、分離手段の網を通過できない油液中
の水分を集水する手段とを備えたことを特徴とす
る油水分離装置。 4 特許請求の範囲第3項において、前記撥水性
を有する網が、金網に前記撥水性素材であるポリ
フツ化エチレン系樹脂をコーテイングしたもので
あることを特徴とする油水分離装置。 5 特許請求の範囲第3項または第4項におい
て、前記分離手段は、パンチングメタルによつて
構成された円筒形状の有孔の保持筒と、この有孔
の保持筒の外周に所定間隔離れて保持された撥水
性素材がコーテイングされた円筒形状の網とから
なることを特徴とする油水分離装置。 6 特許請求の範囲第5項において、前記分離手
段は、水滴の落下に伴う自洗能力をもち、かつ交
換または再使用可能なカートリツジ状に構成され
ていることを特徴とする油水分離装置。
[Scope of Claims] 1. In an oil-water separation method for separating water from an oil containing water, the oil in the oil is held in a perforated holding cylinder and coated with a water-repellent material. An oil-water separation method characterized by separating water from oil by passing it through a net. 2. The oil-water separation method according to claim 1, wherein the oil liquid is a pyrolysis oil obtained by pyrolysis of naphtha. 3. A device for separating water from an oil solution containing water, including a separation means including a perforated holding cylinder and a cylindrical net coated with a water-repellent material, and the oil liquid is applied to the outer peripheral surface of the net of the separation means. A means for sending liquid, a means for collecting oil in the oil liquid that has passed through the net of the separating means, and a means for collecting water in the oil liquid that cannot pass through the net of the separating means. Oil-water separator. 4. The oil-water separator according to claim 3, wherein the water-repellent mesh is a wire mesh coated with a polyfluorinated ethylene resin, which is the water-repellent material. 5. In claim 3 or 4, the separation means includes a cylindrical-shaped holding cylinder with holes made of punched metal, and a holding cylinder with holes arranged at a predetermined distance on the outer periphery of the holding cylinder with holes. An oil/water separation device comprising a cylindrical net coated with a retained water-repellent material. 6. The oil-water separator according to claim 5, wherein the separating means is configured in the form of a cartridge that has a self-cleaning ability as water droplets fall and is replaceable or reusable.
JP1982186A 1986-01-30 1986-01-30 Oil-water separation method and device therefor Granted JPS62176509A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1982186A JPS62176509A (en) 1986-01-30 1986-01-30 Oil-water separation method and device therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1982186A JPS62176509A (en) 1986-01-30 1986-01-30 Oil-water separation method and device therefor

Publications (2)

Publication Number Publication Date
JPS62176509A JPS62176509A (en) 1987-08-03
JPH0225644B2 true JPH0225644B2 (en) 1990-06-05

Family

ID=12009977

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1982186A Granted JPS62176509A (en) 1986-01-30 1986-01-30 Oil-water separation method and device therefor

Country Status (1)

Country Link
JP (1) JPS62176509A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2767768B2 (en) * 1992-06-25 1998-06-18 昭和四日市石油株式会社 Oil-water separator
JP2008110294A (en) * 2006-10-30 2008-05-15 Wako Filter Technology Kk Separator cartridge
CN102416269A (en) * 2011-08-23 2012-04-18 北京航空航天大学 Micro/nano interface separation net and its preparation method and application
CN103316507B (en) * 2013-06-06 2014-12-03 华南理工大学 Super-hydrophilic and underwater-super-oleophobic oil-water separation mesh membrane, and preparation method and application thereof

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS459257Y1 (en) * 1967-01-13 1970-04-30
JPH0665362B2 (en) * 1984-06-14 1994-08-24 旭化成工業株式会社 Separation method

Also Published As

Publication number Publication date
JPS62176509A (en) 1987-08-03

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