JPS61271006A - Ultrafiltration membrane - Google Patents

Ultrafiltration membrane

Info

Publication number
JPS61271006A
JPS61271006A JP11313785A JP11313785A JPS61271006A JP S61271006 A JPS61271006 A JP S61271006A JP 11313785 A JP11313785 A JP 11313785A JP 11313785 A JP11313785 A JP 11313785A JP S61271006 A JPS61271006 A JP S61271006A
Authority
JP
Japan
Prior art keywords
membrane
lipid
porous
ultrafiltration membrane
anionic
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
JP11313785A
Other languages
Japanese (ja)
Inventor
Takehiro Yamamoto
健博 山本
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.)
Nok Corp
Original Assignee
Nok 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 Nok Corp filed Critical Nok Corp
Priority to JP11313785A priority Critical patent/JPS61271006A/en
Publication of JPS61271006A publication Critical patent/JPS61271006A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To obtain ultrafiltration membrane having fouling resistance by impregnating high molecular porous membrance with anionic dimolecular film of lipid. CONSTITUTION:After immersing a porous membrane comprising polysulfone etc. in a soln. dissolving a lipid of anionic dialkyl phosphate. etc., the membrane is washed with water. Thus, an ultrafiltration membrane holding a lipid in the form of dimolecular structure in the pores of the porous membrane is obtd. Since negative charge is given to the membrane, deposition of filtered substances to the surface of the membrane is prevented during filtration of negatively charged emulsified liquid, etc. Amphoteric electroyte such as protein, etc. can be filtered at above the isoelectric point.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、限外口過膜に関する。更に詳しくは、耐汚染
性の限外口過膜に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to an ultraporous membrane. More specifically, the present invention relates to a stain-resistant ultrafiltration membrane.

〔従来の技術〕[Conventional technology]

限外口過膜を用いての油水分離では、時間の経過と共に
口過物質の付着が起り、それによって透水量の低下が生
じる。一般に、透水量の回復手段としては、ボール、気
泡、水流などによる機械的洗浄、薬液による化学的洗浄
および逆洗が用いられる。しかしながら、このような手
段では、洗浄中口過は中断されることになるので、全体
として口過効率は低下する。また、洗浄によって生じた
液を、処理することも必要である。
In oil-water separation using an ultrafiltration membrane, filtration substances adhere over time, resulting in a decrease in water permeation rate. In general, mechanical cleaning using balls, air bubbles, water flow, etc., chemical cleaning using chemicals, and backwashing are used to restore water permeation. However, with such means, the oral filtration is interrupted during washing, and the overall oral filtration efficiency is reduced. It is also necessary to treat the liquid produced by cleaning.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

こういった問題点から、最近では膜自体を修飾すること
でs離基を設け、口過物と同符号の荷電を生じさせるこ
とにより、膜面への付着を防ぐという研究がなされるよ
うになってきている。
Due to these problems, recent research has been conducted to prevent adhesion to the membrane surface by modifying the membrane itself to create an s-leaving group and creating a charge with the same sign as that of the oral product. It has become to.

本発明者は、かかる観点から検討を進めた結果、特定の
アニオン性膜を高分子多孔質膜に含浸させることにより
、耐汚染性の限外口過膜を得ることができた。
As a result of conducting studies from this viewpoint, the present inventor was able to obtain a stain-resistant ultrafiltration membrane by impregnating a porous polymer membrane with a specific anionic membrane.

〔問題点を解決するための手段〕および〔作用〕従って
、本発明は耐汚染性の限外口過膜に係り、この限外口過
膜は、高分子多孔質膜にアニオン性の脂質2分子膜を含
浸させてなる。
[Means for Solving the Problems] and [Operation] Accordingly, the present invention relates to a stain-resistant ultra-permeable membrane, which comprises a porous polymer membrane containing an anionic lipid 2. It is impregnated with a molecular membrane.

高分子多孔質膜としては、ポリスルホン、ポリフッ化ビ
ニリデン、芳香族ポリアミド、ポリプロピレン、酢酸セ
ルロース、ポリカーボネートなど各種高分子材料の多孔
質膜材料であって、約0.001〜1μ閣の孔径を有す
る限外口過膜を形成し得るような孔径のものが用いられ
る。
Porous polymeric membranes include porous membrane materials of various polymeric materials such as polysulfone, polyvinylidene fluoride, aromatic polyamide, polypropylene, cellulose acetate, and polycarbonate, as long as they have a pore size of about 0.001 to 1 μm. A material with a pore size that can form an external membrane is used.

これらの多孔質膜材料に含浸される脂質としては、アニ
オン性のリン酸ジアルキルエステルまたはスルホコハク
酸ジアルキルエステルなどが用いられる。これらの脂質
は、それをドデカン、オクタン、ヘキサン、シクロヘキ
サンなどの直鎖状または脂環状炭化水素溶媒に溶かし、
多孔質膜に含浸させることにより、2分子膜構造をとっ
て膜の微孔中に保持される。
As the lipid impregnated into these porous membrane materials, anionic phosphoric acid dialkyl esters, sulfosuccinic acid dialkyl esters, etc. are used. These lipids can be prepared by dissolving them in linear or alicyclic hydrocarbon solvents such as dodecane, octane, hexane, cyclohexane, etc.
By impregnating it into a porous membrane, it assumes a bilayer membrane structure and is retained in the micropores of the membrane.

〔発明の効果〕〔Effect of the invention〕

高分子多孔質膜の微孔中にアニオン性の脂質2分子膜を
含浸させ、膜に負の荷電をもたせることにより、負の荷
電を有する乳化液などの口過において効果を発揮する。
By impregnating an anionic lipid bilayer membrane into the micropores of a porous polymer membrane and imparting a negative charge to the membrane, it is effective in passing negatively charged emulsions and the like.

また、たん白質のような両性電解質についても、負にな
る条件、即ち等重点以上で用いることができる。更に、
きれいに配向した2分子膜構造のアニオン性脂質を含浸
させることにより、荷電密度が上がり、その口過効果も
一層高められることになる。
Furthermore, ampholytes such as proteins can also be used under conditions where they become negative, that is, at equal or higher concentrations. Furthermore,
By impregnating the anionic lipid with a neatly oriented bilayer membrane structure, the charge density increases and the mouth-cleaning effect is further enhanced.

〔実施例〕〔Example〕

次に、実施例について本発明を説明する。 Next, the present invention will be explained with reference to examples.

実施例 ポリスルホン(UCC社製品P−1700)を15重量
%、ポリビニルピロリドン(分子量約750,000)
 1重量%をそれぞれ含有するジメチルホルムアミド溶
液を、0.2mm厚のスペーサーを用いてガラス板上に
キャストし、水を凝固浴に用いた乾湿式法により凝固さ
せ、純水透過係数10.2aj/aLhr−kg/aJ
、分画分子量20,000のポリスルホン多孔質膜(厚
さ約0.1ms+)を得た。
Example 15% by weight of polysulfone (UCC product P-1700), polyvinylpyrrolidone (molecular weight approximately 750,000)
Dimethylformamide solutions each containing 1% by weight were cast on a glass plate using a 0.2 mm thick spacer, and coagulated by a dry-wet method using water as a coagulation bath, resulting in a pure water permeability coefficient of 10.2 aj/ aLhr-kg/aJ
A polysulfone porous membrane (thickness approximately 0.1 ms+) with a molecular weight cut-off of 20,000 was obtained.

これとは別に、オキシ塩化リンとその3倍当量のドデシ
ルアルコールをベンゼン中で還流させ、20時間反応後
放冷、アルカリ処理および再結晶を行ない、CtZのリ
ン酸ジアルキルエステルを得た。
Separately, phosphorus oxychloride and three equivalents of dodecyl alcohol were refluxed in benzene, and after reaction for 20 hours, the mixture was allowed to cool, treated with an alkali, and recrystallized to obtain a dialkyl phosphate ester of CtZ.

この脂質の3%ドデカン溶液に、前記ポリスルホン多孔
質膜を60℃で10分間浸漬する。その後、液温を室温
迄層してから多孔質膜を取出し、水洗して、目的とする
限外口過膜を得た。
The polysulfone porous membrane is immersed in this 3% dodecane solution of lipid at 60° C. for 10 minutes. Thereafter, the liquid temperature was allowed to reach room temperature, and then the porous membrane was taken out and washed with water to obtain the desired ultrafiltration membrane.

得られた限外口過膜の透過性を調べるために、連続式の
平膜型セルを用いて透過試験を行なった。
In order to examine the permeability of the obtained ultrafiltration membrane, a permeation test was conducted using a continuous flat membrane cell.

口過液としては乳化油切削剤(ユシロ化学製品ニジロー
ケンEC−5を150倍量の水に分散させたもの)を用
い、初期および150時間後の透水量ならびにその比を
求めた。
An emulsified oil cutting agent (Yushiro Chemical Products Nijiroken EC-5 dispersed in 150 times the amount of water) was used as the mouth fluid, and the water permeation amount at the initial stage and after 150 hours and the ratio thereof were determined.

初期透水量  (A)   6.3aJ/a#−hr−
kg/aJ150時間後透水量(B )   4.2a
#/a#−hr−kg/a#同比(B/AX100) 
   66.7%比較例 実施例で用いられたポリスルホン多孔質膜それ自体につ
いて、同様の透過試験を行なった。
Initial water permeability (A) 6.3aJ/a#-hr-
kg/aJ Water permeability after 150 hours (B) 4.2a
#/a#-hr-kg/a# same ratio (B/AX100)
66.7% Comparative Example A similar permeation test was conducted on the polysulfone porous membrane itself used in the example.

初期透水量  (A)   7.2a(/a&−hr−
kg/aJ150時間後透水量(B)   2.9cd
/a#−hr−kg/aJ同比(B/AX100)  
  40.3%以上の実施例および比較例の結果から1
本発明に係る限外口過膜は、初期透水量こそやや低いが
Initial water permeability (A) 7.2a (/a&-hr-
kg/aJ Water permeability after 150 hours (B) 2.9 cd
/a#-hr-kg/aJ same ratio (B/AX100)
1 from the results of Examples and Comparative Examples of 40.3% or more
Although the ultrafiltration membrane according to the present invention has a rather low initial water permeation rate.

口過時間の経過による透水量の低下がかなり抑えられ、
耐汚染性にすぐれていることが分る。なお、実施例およ
び比較例共、透過液は全有機炭素量(TOC)の測定で
、98%以上の排除率を示した。
The decrease in water permeability due to passage of time is considerably suppressed,
It is found that it has excellent stain resistance. In addition, in both Examples and Comparative Examples, the permeated liquid showed an exclusion rate of 98% or more when measured for total organic carbon content (TOC).

Claims (1)

【特許請求の範囲】 1、高分子多孔質膜にアニオン性の脂質2分子膜を含浸
させてなる限外ロ過膜。 2、脂質がリン酸ジアルキルエステルである特許請求の
範囲第1項記載の限外ロ過膜。 3、脂質がスルホコハク酸ジアルキルエステルである特
許請求の範囲第1項記載の限外ロ過膜。
[Claims] 1. An ultrafiltration membrane formed by impregnating a porous polymer membrane with an anionic lipid bilayer membrane. 2. The ultrafiltration membrane according to claim 1, wherein the lipid is dialkyl phosphate. 3. The ultrafiltration membrane according to claim 1, wherein the lipid is a dialkyl sulfosuccinate.
JP11313785A 1985-05-28 1985-05-28 Ultrafiltration membrane Pending JPS61271006A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11313785A JPS61271006A (en) 1985-05-28 1985-05-28 Ultrafiltration membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11313785A JPS61271006A (en) 1985-05-28 1985-05-28 Ultrafiltration membrane

Publications (1)

Publication Number Publication Date
JPS61271006A true JPS61271006A (en) 1986-12-01

Family

ID=14604493

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11313785A Pending JPS61271006A (en) 1985-05-28 1985-05-28 Ultrafiltration membrane

Country Status (1)

Country Link
JP (1) JPS61271006A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5152894A (en) * 1989-02-02 1992-10-06 Hoechst Aktiengesellschaft Semipermeable membrane made from a homogeneously miscible polymer blend
US5279847A (en) * 1990-04-11 1994-01-18 Morinaga Milk Industry Co., Ltd. Methods for producing emulsions, low-fat spread and oil-in-water-in-oil type spread
CN111792742A (en) * 2019-09-29 2020-10-20 中国科学院生态环境研究中心 Method for strengthening anti-pollution capacity of nanofiltration membrane through multistage collaborative filtration

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5152894A (en) * 1989-02-02 1992-10-06 Hoechst Aktiengesellschaft Semipermeable membrane made from a homogeneously miscible polymer blend
US5279847A (en) * 1990-04-11 1994-01-18 Morinaga Milk Industry Co., Ltd. Methods for producing emulsions, low-fat spread and oil-in-water-in-oil type spread
CN111792742A (en) * 2019-09-29 2020-10-20 中国科学院生态环境研究中心 Method for strengthening anti-pollution capacity of nanofiltration membrane through multistage collaborative filtration
CN111792742B (en) * 2019-09-29 2022-05-17 中国科学院生态环境研究中心 Method for strengthening anti-pollution capacity of nanofiltration membrane through multistage collaborative filtration

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