JPS61414A - Separation method - Google Patents

Separation method

Info

Publication number
JPS61414A
JPS61414A JP12066484A JP12066484A JPS61414A JP S61414 A JPS61414 A JP S61414A JP 12066484 A JP12066484 A JP 12066484A JP 12066484 A JP12066484 A JP 12066484A JP S61414 A JPS61414 A JP S61414A
Authority
JP
Japan
Prior art keywords
water
liquid
phase
separation
fibers
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.)
Granted
Application number
JP12066484A
Other languages
Japanese (ja)
Other versions
JPH0665362B2 (en
Inventor
Kazuto Oue
一人 大植
Toshiyuki Kondo
敏之 近藤
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.)
Asahi Kasei Corp
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry Co Ltd
Asahi Kasei Kogyo 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 Asahi Chemical Industry Co Ltd, Asahi Kasei Kogyo KK filed Critical Asahi Chemical Industry Co Ltd
Priority to JP59120664A priority Critical patent/JPH0665362B2/en
Publication of JPS61414A publication Critical patent/JPS61414A/en
Publication of JPH0665362B2 publication Critical patent/JPH0665362B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To separate a liquid held under a phase separation state to water with high separation efficiency, by selectively permeating said liquid by using a fibrous structure having water repellency. CONSTITUTION:A fibrous structure comprising a polytetrafluoroethylene fiber or a polypropylene fiber and having water repellency is used and, by utilizing such a property that said fibrous structure has capacity for selectively permeating only a liquid held under a phase separation state to water such as mixtures of various hydrocarbon compounds such as various paraffinic hydrocarbons, for example, n-pentane or petroleum ether, said liquid is separated from water. By this method, because liquid permeability is high as compared with a film like microporous membrane, separation efficiency under atmospheric pressure is obtained at a level having no problem from a practical aspect.

Description

【発明の詳細な説明】 く技術分野〉 本発明は水と相分離状態にある液体を水から分離する方
法に関する。さらに詳しくは、撥水性を有する繊維構造
体を用い、該繊維構造体が水と相分離状態にある液体の
みを選択的に透過する能カケもつことを利用して水と該
液体とを分離する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION Technical Field The present invention relates to a method for separating a liquid that is in a phase-separated state from water. More specifically, water and the liquid are separated by using a water-repellent fibrous structure and utilizing the ability of the fibrous structure to selectively permeate only a liquid that is phase-separated from water. Regarding the method.

〈従来技術〉 従来、水に不相溶な油や有機溶剤などの液体と水が混合
している液相からの油や有機溶剤と水との分離方法とし
ては、(1)油水混合相を加熱し蒸留したり、遠心力を
利用して物理的に分離する方法:(2)油水混合相に乳
化破壊剤や凝集剤を加えて化学的に分離する方法;(3
)油相のみを選択的に吸着する吸着剤を用いる吸着分離
方法;(4)これらの方法を適宜選択併用する分離方法
などが採用されている。しかしながら、いずれの方法に
おいても、分離が完全に出来なかったシ、コストがかか
る等の欠点を有していた。
<Prior art> Conventionally, methods for separating water from oil or organic solvents from a liquid phase in which water is mixed with liquids such as oils or organic solvents that are incompatible with water include (1) separating an oil/water mixed phase; Physical separation method using heating and distillation or centrifugal force: (2) Chemical separation method by adding a demulsifier or flocculant to the oil-water mixed phase; (3)
) An adsorption separation method using an adsorbent that selectively adsorbs only the oil phase; (4) A separation method in which these methods are selectively used in combination as appropriate. However, both methods have drawbacks such as not being able to perform complete separation and being costly.

また、最近では油水混合相に磁性微粉末を供給し、磁界
を利用して油相のみを移動させて、油水混合相から分離
する磁界分離方法も提案されている。この方法は、油相
が多量に含まれていたシ、油相が分散媒の状態となって
存在していると、高価な磁性微粉末の添加量が著しく増
えるうえ、油相と磁性微粉末を十分に接触させるのに多
くの攪拌エネルギーを必要とする。また、この磁性微粉
末は、油相から回収しても再利用がむずかしいなど実用
上問題があった。
Recently, a magnetic field separation method has also been proposed in which magnetic fine powder is supplied to an oil-water mixed phase and only the oil phase is moved using a magnetic field to separate it from the oil-water mixed phase. This method contains a large amount of oil phase, and if the oil phase exists in the form of a dispersion medium, the amount of expensive magnetic fine powder added will increase significantly, and the oil phase and magnetic fine powder It takes a lot of stirring energy to bring them into sufficient contact. Further, this magnetic fine powder has practical problems such as difficulty in reusing it even if it is recovered from the oil phase.

また、更に高分子微多孔膜による膜分離技術についても
、瀘過、透析、電気透析による方法が知られているが、
いずれの場合も液の透過性が小さい為分離効率が悪く、
また装置を大型化しなければならないという欠点がある
Furthermore, as for membrane separation technology using microporous polymer membranes, methods using filtration, dialysis, and electrodialysis are known.
In either case, the separation efficiency is poor due to low liquid permeability.
Another drawback is that the device must be larger.

〈発明が解決する問題点〉 本発明者らは、かかる従来技術のもつ欠点に鑑み、水と
相分離状態にある液体を水から分離するに際し、液体の
透過性が大きく、分離効率の高い分離技術について検討
した結果、本発明に到達した。
<Problems to be Solved by the Invention> In view of the shortcomings of the prior art, the present inventors have developed a separation method that has high liquid permeability and high separation efficiency when separating a liquid that is in a phase-separated state from water. As a result of studying the technology, we have arrived at the present invention.

〈問題点を解決するための手段〉 本発明に係る分離方法は、水と相分離状態にある液体を
分離するに際し、4通水性を有する繊維構透体を用いて
該液体全選択的に透過せしめる事を% g!1.とする
<Means for Solving the Problems> In the separation method according to the present invention, when separating a liquid that is in a phase-separated state from water, the liquid is selectively permeable using a fiber structure having four permeability. % g! 1. shall be.

本発明でいう「相分離状塵」とは、水相が液体相中に分
散しているか、あるいは液体相が水相中に分散している
か、または、全体がただ一つの界面を挾んで2層に分離
されているなど、2相の物(理的分散の形態を問わす、
水相と液体相が共存しているものをいう。従って、本発
明では、最初から相分離状態にあるものだけでなく、均
一溶液に水への溶解度か低くかつ注目する液体への溶解
度が大きい溶媒を添加して相分離状態にしたものや、水
に酸化合物が分散している状態の溶液に水への溶解度が
低く、かつ注目する化合物への溶解度の大きい溶媒を添
加して相分離状態にしたものも含着れる。
"Phase-separated dust" as used in the present invention refers to dust in which an aqueous phase is dispersed in a liquid phase, or a liquid phase is dispersed in an aqueous phase, or the entire dust is divided into two parts with only one interface between them. Two-phase substances, such as those separated into layers (regardless of the form of physical dispersion,
A substance in which an aqueous phase and a liquid phase coexist. Therefore, in the present invention, not only those that are in a phase-separated state from the beginning, but also those that have been made into a phase-separated state by adding a solvent that has low solubility in water and high solubility in the liquid of interest to a homogeneous solution, and Also included is a solution in which an acid compound is dispersed, and a solvent that has low solubility in water and high solubility for the compound of interest is added to form a phase-separated state.

本発明において特に好適に分離出来る液体としては水に
実質的に溶解しない液体であシ、かつ液体の表面張力が
55 dyne/C1n以下のものが挙げられる。表面
張力が40 dyne/crn以下の液体はよシーI’
M分離効率がよい。これら液体の代表的例としてi、i
、n −A!ンタン、n−ヘキサン、n−ヘプタン、n
−オクタン、n−デカン等の各種パラフィン系炭化水素
1右油エーテル、リグロイン、ガソリン、灯油1石油ナ
フサ等の各種炭化水素化合物の混合m、ベンゼン、トル
エン、キシレン等の芳香族炭化水素fヒ合物、シクロペ
ンタン、シクロヘキサンで代表される脂環式炭化水素化
合物、各種鉱物油、植物油、動物油、各種エーテル、ケ
トン。
In the present invention, particularly suitable liquids that can be separated include those that are substantially insoluble in water and have a surface tension of 55 dyne/C1n or less. Liquids with a surface tension of 40 dyne/crn or less are safe.
Good M separation efficiency. Typical examples of these liquids are i, i
,n-A! n-tane, n-hexane, n-heptane, n
- Mixtures of various paraffinic hydrocarbons such as octane and n-decane, etc. 1) Mixtures of various hydrocarbon compounds such as ether, ligroin, gasoline, and kerosene (1) petroleum naphtha, and aromatic hydrocarbons such as benzene, toluene, and xylene. alicyclic hydrocarbon compounds represented by cyclopentane and cyclohexane, various mineral oils, vegetable oils, animal oils, various ethers, and ketones.

エステル、アルコール、フェノールE等7>E挙げられ
る。
Examples include 7>E such as ester, alcohol, and phenol E.

本発明でいう「撥水性を有する繊維構造体」とは、JI
S −L −1092B法で測定した耐水圧が100咽
H20以上、好ましくは200 tan H20〜20
00 ttm H2Oのものをいう。耐水圧のレベルは
分離操作の条件によシ必要に応じ通常10001000
0Wの範囲内で適宜選定すればよい。
The "fiber structure having water repellency" as used in the present invention refers to JI
Water pressure resistance measured by S-L-1092B method is 100 tan H20 or higher, preferably 200 tan H20 to 20
00 ttm H2O. The level of water pressure resistance is usually 10001000 depending on the conditions of separation operation.
It may be selected appropriately within the range of 0W.

本発明の繊維構造体の形態は織布、編布、不織布、マッ
ト状、フェルト状、シート状のいずれでもよく単糸デニ
ールか細いものやフィブリル化した繊維を使用したり、
高密度織物の如き高密度化したものが高耐水圧が得られ
易い点で好適に使用される。液透過性においては編布、
不織布、シート状の形態のものが同じ耐水圧下でもすぐ
れておシ、特に本発明においては、高耐水圧が得られ易
く液透過性の高い繊維構造体として、単糸繊度が1デニ
ール以下の繊維からなる不織布、シート状物が挙けられ
る。
The fiber structure of the present invention may be in the form of woven fabric, knitted fabric, non-woven fabric, mat, felt, or sheet. Single denier or thin fibers or fibrillated fibers may be used.
Highly densified materials such as high-density fabrics are preferably used because they can easily provide high water pressure resistance. In terms of liquid permeability, knitted fabric,
Non-woven fabrics and sheet-like fabrics are excellent even under the same water pressure resistance, and in particular, in the present invention, fibers with a single filament fineness of 1 denier or less are used as fiber structures that can easily obtain high water pressure resistance and have high liquid permeability. Examples include nonwoven fabrics and sheet-like materials made of

本発明の繊維構造体を構成する繊維としては、ポリエチ
レンテレフタレート、ポリエチレンテレフタレート・ア
ジヘ−)、、]?リポリエチレンテレフタレートソフタ
レート、ポリエチレンテレフタレート・セパケート、ポ
リエチレンテレフタレート・ドデカンジオエート、ポリ
ブチレンテレフタレートなどのポリエステル系共重合体
の繊維、ポリへキサメチレンアジノ4ミド、ポリへキザ
メチレンセパカミド、ポリへキサメチレンデカミド、ポ
リへキサメチレンへキサミド、ポリカプラミド。
Examples of the fibers constituting the fiber structure of the present invention include polyethylene terephthalate, polyethylene terephthalate, etc. Fibers of polyester copolymers such as polyethylene terephthalate sophthalate, polyethylene terephthalate sepacate, polyethylene terephthalate dodecanedioate, polybutylene terephthalate, polyhexamethylene azino 4mide, polyhexamethylene sepacamide, polyhexane Methylenedecamide, polyhexamethylenehexamide, polycapramide.

ポリオクタミド、ポリノナミド、ポリデカミド。Polyoctamide, polynonamide, polydecamide.

ポリドデカミド、ポリテトラミドなどのポリアミドの繊
維、ポリアミド・イミド繊維、芳香族ポリアミド繊維、
Iリパラエチレンオキシペンゾエートなどのポリエステ
ルエーテルの繊維、ポリ塩化ビニル、ポリ塩化ビニリデ
ン、ポリフッ化ビニリデン、ポリテトラフルオロエチレ
ンなどのハロゲン含有重合体の繊維、ポリプロピレン、
ポリエチレンなどのポリオレフィンの繊維、各種アクリ
ル繊維、再生セルロース、アセテート、木綿、麻、絹。
Polyamide fibers such as polydodecamide and polytetramid, polyamide/imide fibers, aromatic polyamide fibers,
Fibers of polyester ethers such as I-liparaethylene oxypenzoate, fibers of halogen-containing polymers such as polyvinyl chloride, polyvinylidene chloride, polyvinylidene fluoride, polytetrafluoroethylene, polypropylene,
Polyolefin fibers such as polyethylene, various acrylic fibers, regenerated cellulose, acetate, cotton, linen, and silk.

羊毛などが挙げられる。これらの繊維は単独まだは組み
合せて使用される。
Examples include wool. These fibers may be used alone or in combination.

撥水性を有する繊維構造体の具体例としては、ポリテト
ラフルオロエチレン繊維、ポリプロピレン繊維、ポリエ
チレン繊維等の疎水性繊維からなる構造体、あるいは繊
維構造体に撥水加工を施こす事によシ撥水性を付与した
構造体が挙げられる。
Specific examples of water-repellent fiber structures include structures made of hydrophobic fibers such as polytetrafluoroethylene fibers, polypropylene fibers, and polyethylene fibers, or structures made of hydrophobic fibers such as polytetrafluoroethylene fibers, polypropylene fibers, and polyethylene fibers, or structures that are water-repellent by applying water-repellent treatment to the fiber structures. Examples include structures that have aqueous properties.

繊維構造体の撥水加工は通常の方法で行えはよく、例え
ば、アクリル酸パーフルオロアルコールなどのフッソ系
樹脂、ジメチルシリコーンなどのシリコーン系樹脂、−
′?ラフイン系樹脂、ワックス系樹脂等の公知の撥水加
工剤を、原糸製造時あるいは繊維構造体に・ぞディング
、浸漬、スプレー、吸尽等の方法で付与させればよい。
Water-repellent treatment of the fiber structure can be carried out using conventional methods, such as fluorocarbon resins such as acrylic acid perfluoroalcohol, silicone resins such as dimethyl silicone, -
′? A known water repellent agent such as a rough-in resin or a wax resin may be applied to the fiber structure at the time of manufacturing the yarn or by a method such as dipping, dipping, spraying, or exhaustion.

更に必要に応じ、撥水加工剤を付与した後、熱処理を行
なえばよい。
Further, if necessary, heat treatment may be performed after applying a water repellent agent.

本発明にかける分離方法は特に限足されるものではなく
、バッチ式又は連続式で縦型、横型、多段型等の各種p
過方式が適用+11il能である。分前装置の一例を第
1し1に示す。同図において、水およ(。、によ□4分
離4.ア、あ、お体よ。1合液(1)。
The separation method applied to the present invention is not particularly limited, and various types of separation methods such as batch type or continuous type, vertical type, horizontal type, multi-stage type, etc.
The above method is applicable +11il function. An example of the portioning device is shown in Figure 1. In the same figure, water and (., □ 4 separation 4. A, ah, body. 1 mixture (1).

うち、後者の液体は鉛直方向繊維構造体(2)および必
要に応じて支持体(3)に支持された水平方向繊維構造
体(2)′f!:選択的に透過させ、弁(5)を開いて
回収する。
Of these, the latter liquid flows through the vertical fiber structure (2) and optionally the horizontal fiber structure (2)'f! supported on the support (3). : Selectively permeate, open valve (5) and collect.

分離濾過効率の面からは流過面積を多くする様に繊維構
造体をジャバラ状にして濾過器に装着するのが好ましい
。更に繊維構造体の耐水圧よシ低い圧において加圧濾過
を行なう事もできる。また、攪拌しながら濾過してもよ
い。特に本発明の分離方法はフィルム状の微多孔膜に比
べ液透過性が高いため通常、常圧で実用的に問題のない
レベルの分離効率が得られる。
From the standpoint of separation and filtration efficiency, it is preferable to attach the fiber structure to the filter in a bellows shape so as to increase the flow area. Furthermore, pressure filtration can also be performed at a pressure lower than the water pressure of the fibrous structure. Alternatively, it may be filtered while stirring. In particular, since the separation method of the present invention has higher liquid permeability than a film-like microporous membrane, a separation efficiency of a practically acceptable level can usually be obtained at normal pressure.

〈発明の効果〉 本発明によれば、水と相分離状態にある液体を高い分離
効率をもって、分離することができる。
<Effects of the Invention> According to the present invention, a liquid in a phase-separated state from water can be separated with high separation efficiency.

この分離技術の適用分野は非常に広く、石油、化学、自
動車、電気、電子、印刷、ゴム、紙、フィルム、繊維、
プラスチック、人工皮革、ドライクリーニング、医薬品
1食品、金属と産業界のあらゆる分野での水と相分離状
態にある液体の分離に適用が可能でおる。例えば、石油
精製工程中での水の分離、ガソリンスタンドの水混合液
からの分離、自動車ガソリン中の水の分離、灯油中の水
の分離2石油系ドライクリーニングの水の分離等に利用
出来る。
The application fields of this separation technology are very wide, including petroleum, chemicals, automobiles, electricity, electronics, printing, rubber, paper, film, textiles, etc.
It can be applied to the separation of liquids that are phase separated from water in all industrial fields such as plastics, artificial leather, dry cleaning, pharmaceuticals, foods, and metals. For example, it can be used to separate water in petroleum refining processes, from water mixtures at gas stations, from automobile gasoline, from kerosene, and from petroleum-based dry cleaning.

〈実施例〉 以下、実施例について本発明を更に詳しく説明する。<Example> Hereinafter, the present invention will be explained in more detail with reference to Examples.

実施例−1 メルトブロー法に上って平均繊度0,05デニールの極
細繊維からなる目付40/j/rn2のポリエチレンテ
レフタレートのランダムウェッブを得た。
Example 1 A random web of polyethylene terephthalate having a basis weight of 40/j/rn2 and consisting of ultrafine fibers having an average fineness of 0.05 denier was obtained by a melt blowing method.

このウェッブをカレンダー加工し、撥水加工剤としてポ
ロンMR4重量係水溶液(信越化学社製)に浸漬し、マ
ングルにて絞シ率100%で均一に絞液し、100℃で
3分の予備乾燥後180℃で1分間熱処理を行なった。
This web was calendered, immersed in Poron MR4 weight water solution (manufactured by Shin-Etsu Chemical Co., Ltd.) as a water repellent agent, squeezed uniformly with a mangle at a squeezing rate of 100%, and pre-dried at 100°C for 3 minutes. After that, heat treatment was performed at 180° C. for 1 minute.

得られた不織布の耐水圧をJIS−L1092B法で測
定した結果650咽H20を示した。
The water pressure resistance of the obtained nonwoven fabric was measured according to the JIS-L1092B method, and the result was 650 H20.

棟だ、比較的のだめに撥水加工を施していない不織布に
ついて測定した結果耐水圧80 mm H2Oであった
。この2秤類の不織布を用い下記に示す水と相分離状態
にある液体の分離を試みた。
However, the water pressure resistance was 80 mm H2O when measured on a non-woven fabric that had not been treated with a water-repellent finish. Using these two types of nonwoven fabrics, an attempt was made to separate a liquid that is in a phase-separated state from water as shown below.

(、)  水100CC中にエチルエーテル500Cが
混合分散した液体、 (b)  水100m中にトルエン100ωを混合した
液体 (c)水1. OO工中に灯油5occt−混合した液
体分離方法としては第1図の如き分離装置を作成し分離
操作を行なった。
(,) A liquid in which 500C of ethyl ether is mixed and dispersed in 100CC of water. (b) A liquid in which 100Ω of toluene is mixed in 100m of water. (c) Water 1. As a method for separating the liquid mixed with 5 oct of kerosene during the OO work, a separation device as shown in Fig. 1 was prepared and the separation operation was performed.

分離効率の評価として濾過速度を求めた。また、分離性
卵として、漣過後の液体を一昼夜放置した後相分離して
いるかを調べだ。すなわち、十分な振動を与えたときに
完全に分離出来ているものは混濁することはないが水が
溶解度以上に混入している場合は白濁を起こす現象を利
用し分離性能を調べた。それらの結果は第1表に示す・
以下余白 第1表から明らかなように、撥水性を有する繊維構造体
を使用した本発明による分離は、流過速度が大きく、非
常に分離性能に優れていることがわかる。
Filtration rate was determined as an evaluation of separation efficiency. In addition, as a separable egg, the liquid after rinsing was allowed to stand for a day and night, and then it was examined to see if the phases separated. In other words, separation performance was investigated using the phenomenon that when sufficient vibration is applied, a sample that is completely separated will not become cloudy, but if water is mixed in at a level higher than the solubility level, it will become cloudy. The results are shown in Table 1.
As is clear from Table 1 below, it can be seen that the separation according to the present invention using a water-repellent fibrous structure has a high flow rate and extremely excellent separation performance.

実施例−2 メルトゾロ−法によって単繊維繊度が0.02デニール
の極細繊維からなる目付50g/m2のポリプロピレン
のランダムウェッブを得た。
Example 2 A random web of polypropylene having a basis weight of 50 g/m2 and consisting of ultrafine fibers having a single fiber fineness of 0.02 denier was obtained by the melt-sollow method.

このウェッブを用いてJIS L −1092B法によ
る耐水圧が95 tan H2O,150mm H2O
,250mm H2Oとなる様に加圧加工を施した。こ
の試料を用いエチルアセテートの中に水が混合分散して
いるものの濾過を実施例−1と同様に行なった。
Using this web, the water pressure resistance according to JIS L-1092B method is 95 tan H2O, 150mm H2O
, 250 mm H2O. Using this sample, ethyl acetate containing water mixed and dispersed was filtered in the same manner as in Example-1.

*流過液のエチルアセテート中の水の濃度を島津製作所
ガスクロマトグラフィーGC4CMe用いて測定し、濾
過時の温度における水の溶解能以上に水が含まれている
か否かで分離性をみた。
*The concentration of water in the ethyl acetate of the effluent was measured using a Shimadzu gas chromatography GC4CMe, and the separability was determined by whether water was contained in an amount greater than the water solubility at the temperature during filtration.

第2表から明らかな様に耐水圧が°100 tran 
H20未満のlIc維構造体の場合にはエチルアセテー
トと水の分離は不可であったがそれ以上の耐水圧を示し
た本発明の繊維構造体を用いた分離においてはすぐれた
分離性を示した。
As is clear from Table 2, the water pressure resistance is °100 tran.
In the case of the lIc fiber structure of less than H20, it was impossible to separate ethyl acetate and water, but the separation using the fiber structure of the present invention, which showed higher water pressure resistance, showed excellent separation performance. .

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

第1図は本発明の分離方法の実施に用いる装置の一例を
示したものである。 (1)水および水と相分離状態にある液体との混合液、
(2)繊維構造体、(3)支持体、(4)弁。 第1図
FIG. 1 shows an example of an apparatus used to carry out the separation method of the present invention. (1) A liquid mixture of water and a liquid in a phase-separated state,
(2) fibrous structure, (3) support, (4) valve. Figure 1

Claims (1)

【特許請求の範囲】[Claims] 水と相分離状態にある液体を分離するに際し、撥水性を
有する繊維構造体を用いて該液体を選択的に透過する事
を特徴とする分離方法。
A separation method characterized in that, when separating a liquid that is in a phase-separated state from water, the liquid is selectively permeated using a water-repellent fibrous structure.
JP59120664A 1984-06-14 1984-06-14 Separation method Expired - Fee Related JPH0665362B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59120664A JPH0665362B2 (en) 1984-06-14 1984-06-14 Separation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59120664A JPH0665362B2 (en) 1984-06-14 1984-06-14 Separation method

Publications (2)

Publication Number Publication Date
JPS61414A true JPS61414A (en) 1986-01-06
JPH0665362B2 JPH0665362B2 (en) 1994-08-24

Family

ID=14791844

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59120664A Expired - Fee Related JPH0665362B2 (en) 1984-06-14 1984-06-14 Separation method

Country Status (1)

Country Link
JP (1) JPH0665362B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62176509A (en) * 1986-01-30 1987-08-03 Idemitsu Petrochem Co Ltd Oil-water separation method and device therefor
US10350166B2 (en) 2009-07-29 2019-07-16 Foamix Pharmaceuticals Ltd. Non surface active agent non polymeric agent hydro-alcoholic foamable compositions, breakable foams and their uses

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5112462A (en) * 1974-07-21 1976-01-31 Somar Mfg YUSUIBUNRIROKATAI

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5112462A (en) * 1974-07-21 1976-01-31 Somar Mfg YUSUIBUNRIROKATAI

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62176509A (en) * 1986-01-30 1987-08-03 Idemitsu Petrochem Co Ltd Oil-water separation method and device therefor
US10350166B2 (en) 2009-07-29 2019-07-16 Foamix Pharmaceuticals Ltd. Non surface active agent non polymeric agent hydro-alcoholic foamable compositions, breakable foams and their uses

Also Published As

Publication number Publication date
JPH0665362B2 (en) 1994-08-24

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