JPS58219940A - Adsorbing material for organic substance - Google Patents

Adsorbing material for organic substance

Info

Publication number
JPS58219940A
JPS58219940A JP10157182A JP10157182A JPS58219940A JP S58219940 A JPS58219940 A JP S58219940A JP 10157182 A JP10157182 A JP 10157182A JP 10157182 A JP10157182 A JP 10157182A JP S58219940 A JPS58219940 A JP S58219940A
Authority
JP
Japan
Prior art keywords
water
adsorption
hollow
adsorbent
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.)
Pending
Application number
JP10157182A
Other languages
Japanese (ja)
Inventor
Zen Katagiri
片桐 禅
Michio Inoue
井上 通生
Hisao Tanaka
久雄 田中
Yoko Nakanishi
洋子 中西
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.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Rayon 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 Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP10157182A priority Critical patent/JPS58219940A/en
Publication of JPS58219940A publication Critical patent/JPS58219940A/en
Pending legal-status Critical Current

Links

Landscapes

  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は水中に溶存あるいは懸濁している有機化合物を
ファンデルワールス力によル吸着する多孔質吸着材に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a porous adsorbent that adsorbs organic compounds dissolved or suspended in water using van der Waals forces.

従来水中に流出した油類を処理するものとして疎水性繊
維成形体等を用いるものがあるが。
Conventionally, hydrophobic fiber moldings and the like have been used to treat oil spilled into water.

これは水上に浮上した油分を吸着するには適しているが
水中に溶解あるい伏懸濁している油分、親水性有機物の
吸着には素材の疎水性がかえって災いして水との接触面
積が減少して高い吸着効果が得られないという欠点を有
している。
This material is suitable for adsorbing oil that has surfaced on the water, but the hydrophobic nature of the material is detrimental to the adsorption of dissolved or suspended oil and hydrophilic organic matter, which reduces the contact area with water. This has the disadvantage that a high adsorption effect cannot be obtained due to the decrease in the amount of adsorption.

また活性炭や三次元架橋構造をとらせた多孔質樹脂もあ
るが、活性炭鉱取扱い時微粉化し易く、水中投入後の回
収が困難であるという欠点を有する。三次元架橋多孔質
樹脂鉱樹脂内に親水基、イオン交換基を導入、該基導入
による樹脂の水溶性の増大の防止のため三次元架橋の導
入等調製に複雑な手法を要し、そのため高価なものにな
るという欠点を有している。
There are also activated carbon and porous resins with a three-dimensional cross-linked structure, but they have the drawback of being easily pulverized when handling activated carbon mines and difficult to recover after being put into water. Introducing hydrophilic groups and ion exchange groups into the three-dimensionally crosslinked porous resin mineral resin.In order to prevent the introduction of these groups from increasing the water solubility of the resin, complicated methods are required for the preparation, such as introducing three-dimensional crosslinks, which makes the resin expensive. It has the disadvantage of becoming a thing.

本発明者らはこれら吸着材の欠点を除き、取扱いの容易
な吸着材の開発に鋭意努力し、ポリオレフィン多孔質中
空繊維を親水化したものが水中の有機物の吸着性能に優
れていることを見出し、本発明に至ったものであるO 即ち従来吸着材を親水化すると親油性物質の吸着能を低
下せしめると考えられていたにもかかわらず、水中に溶
解、懸濁し九有機物の吸着においてポリオレフィン吸着
材を用いる場合鉱ファンデルワールス巌による吸着のた
め親水化してもさほど吸着能嬬低下せず、親水化により
多孔質吸着材の微細な空孔内にまで水分子が侵入し易く
なシ溶存・懸濁している有機物質に接触する機会すなわ
ち有効表面積が格段に増加することにより吸着能が増大
することを見出したものである。即ち本発明は微小空孔
が中空糸内壁面よシ外壁面に相互につながったポリオレ
フィン多孔質中空短繊維からなる吸着材の表面が親水化
されていることを特徴とする水中の疎水性有機物質およ
び親水性有機物質の吸着剤に関するものである。
The present inventors have worked diligently to eliminate the drawbacks of these adsorbents and develop an easy-to-handle adsorbent, and have discovered that polyolefin porous hollow fibers made hydrophilic have excellent adsorption performance for organic matter in water. In other words, although it was conventionally thought that making an adsorbent hydrophilic would reduce its ability to adsorb lipophilic substances, polyolefin adsorption in the adsorption of nine organic substances dissolved and suspended in water. When a porous adsorbent is used, its adsorption capacity does not decrease significantly even if it becomes hydrophilic due to adsorption by van der Waals rock, and by making it hydrophilic, it becomes easier for water molecules to penetrate into the fine pores of the porous adsorbent. It has been discovered that the adsorption capacity is increased by significantly increasing the opportunity to contact suspended organic substances, that is, the effective surface area. That is, the present invention provides a hydrophobic organic substance in water, which is characterized in that the surface of an adsorbent made of porous hollow short fibers of polyolefin in which micropores are interconnected on the inner wall surface and the outer wall surface of the hollow fibers is made hydrophilic. and adsorbents for hydrophilic organic substances.

ポリオレフィンとしてはポリエチレン、ポリプロピレン
、ポリテトラフルオロエチレン、およびそれらを主成分
とするコポリマーが好ましく用いられ、たとえばこれら
を溶融紡糸あるいはエマルジョン紡糸焼結し、工程中で
適度な延伸を与えることによっても、ミクロフィルが引
き裂かれて側壁中に微細な細孔群を賦与した中空糸を得
ることができる。該方法によって中空糸として、微細孔
が繊維長方向に配列したミクロフィブリルとミクロフィ
ブリルをこれとハヌ直角に連結した結節部から形成され
た多数の短冊状空孔でl)、該微小空孔が中空糸内壁面
よシ外壁面に相互につながった積層構造を有する中空糸
を得ることができる。
As polyolefins, polyethylene, polypropylene, polytetrafluoroethylene, and copolymers containing these as main components are preferably used. The fill can be torn to yield hollow fibers with fine pores in the sidewalls. By this method, a hollow fiber is formed by a large number of strip-shaped pores formed from microfibrils in which micropores are arranged in the fiber length direction and knots in which the microfibrils are connected at right angles to the microfibrils. It is possible to obtain a hollow fiber having a laminated structure in which the inner wall surface and the outer wall surface of the hollow fiber are interconnected.

得られる中空糸の平均孔径、空孔率等は種々のものを得
ることができるが、平均孔径としては0.06〜10μ
のものが好ましい。0.06μ以下であると目詰シの可
能性が大きくなシ、有効表面積低下をまねく恐れがある
。親水化された微孔を水が自由に通過するためには10
μ以上である必要はなく、10μ以上の孔径のものでも
本発明の目的に充分使用できるが、表面積がその分低下
する。
The average pore diameter, porosity, etc. of the obtained hollow fibers can vary, but the average pore diameter is 0.06 to 10μ.
Preferably. If it is less than 0.06μ, there is a high possibility of clogging and a decrease in effective surface area. In order for water to freely pass through the hydrophilized micropores, 10
It is not necessary that the pore diameter be 10 μm or more, and pores with a pore size of 10 μm or more can be used satisfactorily for the purpose of the present invention, but the surface area will be reduced accordingly.

嘔うに微孔構造が多数の之クロフィブリルとこれを連結
する結節部から形成され、多数の空孔が相互に連通して
中空糸内壁から外壁に相互につながった積層構造を有し
ている上記膜は微孔内部の表面積が大きいこと、一つが
目詰シしてもその周辺の空孔を経由して内部の空孔まで
”1・ 水が侵入できるので目詰りによる性能低下がないという
特徴がある。
In fact, the microporous structure is formed from a large number of clofibrils and knots that connect them, and the above-mentioned structure has a laminated structure in which a large number of pores communicate with each other and are interconnected from the inner wall of the hollow fiber to the outer wall. The membrane has a large surface area inside the micropores, and even if one becomes clogged, water can penetrate into the inner pores through the surrounding pores, so there is no performance deterioration due to clogging. There is.

該中空糸の形状れ任意であるが、内径100〜500A
1肉厚10〜100μ、空孔率20〜90チ、表面積1
0〜100ジ/fであることが好ましい。
The shape of the hollow fiber is arbitrary, but the inner diameter is 100 to 500A.
1 wall thickness 10~100μ, porosity 20~90cm, surface area 1
It is preferable that it is 0 to 100 di/f.

中空短繊維の繊維長は任意であるが、被処理水中に懸濁
させて用いる場合には1〜500mの繊維長であるもの
が好ましい。これよシ長い短繊維をすだれ状、吹き流し
状に成形した吸着材であってもよく、中空短繊維をウェ
ブ状にし接着したもの、任意の形状の織物も用いること
ができる。
The fiber length of the hollow short fibers is arbitrary, but when used suspended in water to be treated, the fiber length is preferably 1 to 500 m. An adsorbent made of longer short fibers shaped into a blind or streamer shape, a web made of hollow short fibers glued together, or a woven fabric of any shape can also be used.

本発明の方法では微小空孔が中空糸内壁面よシ外壁面に
相互につながった多孔質中空糸を用いるが、f過分離で
はないため孔径分布がどのように広くてもまたピンホー
ルが存在していても何ら支障がない。しかも短繊維であ
るため被処理水が繊維開口部を経由して中空糸の内側か
らも膜内面に侵入、接触し、よシ効果的な1着が行われ
るという特徴がある。
The method of the present invention uses a porous hollow fiber in which micropores are interconnected on the inner wall surface and the outer wall surface of the hollow fiber, but since f overseparation is not performed, pinholes still exist no matter how wide the pore size distribution is. There is no problem in doing so. Furthermore, since they are short fibers, the water to be treated enters and contacts the inner surface of the membrane from the inside of the hollow fibers via the fiber openings, resulting in more effective tying.

親水化はポリオレフィンに親和性を有し、かつ水と混合
可能な液体またはその水溶液中核短繊維を浸漬し、該液
体を微細孔内に侵入させることによシ行うことができる
Hydrophilization can be carried out by immersing the core short fibers in a liquid that has an affinity for the polyolefin and is miscible with water or an aqueous solution thereof, and allowing the liquid to enter the micropores.

該液体の例としてはメチルアルコール、エチルアルコー
ル、プロピルアルコール、エチレングリコール等のアル
コール類、各種界面活性剤を挙げることができるが、膜
内への残留、再溶出の可能性を考慮すると低級アルコー
ルを用いることが好ましい。
Examples of such liquids include alcohols such as methyl alcohol, ethyl alcohol, propyl alcohol, and ethylene glycol, and various surfactants; however, considering the possibility of remaining in the membrane and re-elution, lower alcohols are recommended. It is preferable to use

当該中空糸状体の吸着機構は、有機物質とポリオレフィ
ン系高分子物質との間に作用するファン・デル・ワール
ス書胞よるものであって、いわゆる1別による分離方法
とは異なる。それゆえ、対象となる有機物質の種類は、
分子の大きさによって限定されるわけではなく、疎水性
の化学構造(たとえば、アルキル基、エステル基、芳香
環等)を有する物質に対して、よシ一層吸着効果が大と
なる。
The adsorption mechanism of the hollow fibers is based on van der Waals vacuoles that act between the organic substance and the polyolefin polymer substance, and is different from the so-called separation method using one separation. Therefore, the types of organic substances targeted are:
It is not limited by the size of the molecule, and the adsorption effect is even greater for substances having a hydrophobic chemical structure (for example, an alkyl group, an ester group, an aromatic ring, etc.).

次に実施例によりこの発明をさらに具体的に説明する。Next, the present invention will be explained in more detail with reference to Examples.

実施例1 内径260μ、肉厚55μ、空孔率60チ(水銀圧入法
による)および表面積40tn”/fをもち、かつ孔径
0.06〜2μの微小細孔群を有するポリエチレン中空
糸0.7Fを約5〜5111IKに裁断し、エタノール
50−で親水化し、ついで純水で洗浄後、約0.1 p
pmのメチルオレンジ水溶液50mj!を入れた100
1ntビーカー中に加え、ガラス棒で攪拌したところ、
数分でメチルオレンジ水溶液の淡いオレンジ色は消滅し
、そのかわシ、ポリエチレン中空糸は淡黄色に染まった
。この中空糸を1()4ガラスフイルターに移し、メタ
ノール50−で洗浄したところ、当該中空糸の淡黄色は
消え、メチルオレンジは容易に脱着された。
Example 1 Polyethylene hollow fiber 0.7F having an inner diameter of 260μ, a wall thickness of 55μ, a porosity of 60cm (by mercury intrusion method), a surface area of 40tn''/f, and a group of micropores with a pore diameter of 0.06 to 2μ. was cut into approximately 5 to 5111 IK, made hydrophilic with ethanol 50- and then washed with pure water.
pm methyl orange aqueous solution 50mj! 100 with
When added to a 1 nt beaker and stirred with a glass rod,
In a few minutes, the pale orange color of the methyl orange aqueous solution disappeared, and the polyethylene hollow fibers were dyed pale yellow. When this hollow fiber was transferred to a 1()4 glass filter and washed with 50 methanol, the pale yellow color of the hollow fiber disappeared and methyl orange was easily desorbed.

比較のために、ポリエチレン製の市販合成パルプ(三井
ゼラパツク)について上と同様の操作ヲ行ったが、メチ
ルオレンジ水溶液は脱色されなかった。当合成パルプの
形状は、走査型電子顕微鏡写真によれば、幅5μ、長さ
数閣のフィブリルの集合体であり、尚該ポリエチレン中
空糸のような微小細孔群は認。められなかった。
For comparison, the same operation as above was performed on a commercially available synthetic pulp made of polyethylene (Mitsui Zerapack), but the methyl orange aqueous solution was not decolorized. According to a scanning electron micrograph, the shape of this synthetic pulp is an aggregate of fibrils with a width of 5 μm and a length of a few centimeters, and micropore groups like the polyethylene hollow fibers are observed. It did not fit.

このことから、有機物質の吸着に株、本発明のように側
壁中にミクロフィブリルの引き裂きによって生じた微小
細孔を有する中空糸状体が優れていることか明らかであ
る。
From this, it is clear that the hollow filamentous body having micropores created by tearing microfibrils in the side wall as in the present invention is excellent in adsorbing organic substances.

実施例2 内径200μ、肉厚25μ、空孔率50チおよび表面積
50’tn”/fをもち、かつ側壁中に孔・径0.06
〜2μの微小細孔群をもつポリプロピレン中空糸0.5
fについて、実施例1と同様の実験を実施したところ、
ポリプロピレン中空糸は淡黄色に染まシ、メチルオレン
ジ水溶液は脱色された。またこの着色した中空糸をiG
4ガラスフィルターに移し、メタノール50−で洗浄し
たところ、もとの白色に戻った。このことから、当該ポ
リプロ、ピレン中空糸も、有機化合物の吸着・脱着性能
のあることが確認された。
Example 2 It has an inner diameter of 200μ, a wall thickness of 25μ, a porosity of 50cm, a surface area of 50'tn''/f, and a hole/diameter of 0.06 in the side wall.
Polypropylene hollow fiber with ~2μ micropores 0.5
When conducting the same experiment as in Example 1 regarding f,
The polypropylene hollow fiber was dyed pale yellow, and the methyl orange aqueous solution was decolored. In addition, this colored hollow fiber is
When the mixture was transferred to a 4-glass filter and washed with 50 methanol, its original white color returned. From this, it was confirmed that the polypropylene and pyrene hollow fibers also have the ability to adsorb and desorb organic compounds.

実施例5 吸着性能を定量的に把握するために、実施例1において
使用したのと同じポリエチレン中空糸をメタノールで8
時間ソックスレー抽出し、オリゴマー・添加剤を除去す
ると同時に親水化し、純水で洗浄後、長さ1〜Strm
に裁断しくカットファイバと呼ぶ)、内径15trmの
ガラスクロマト管に当該カットファイド2fを充填した
Example 5 In order to quantitatively understand the adsorption performance, the same polyethylene hollow fiber used in Example 1 was soaked with methanol.
After time Soxhlet extraction, removing oligomers and additives and making it hydrophilic at the same time, washing with pure water, the length is 1~Strm.
A glass chromato tube with an inner diameter of 15 trm was filled with the cut fiber 2f.

カットファイバの流出あるいは浮き上がりを防止するた
めに、カットファイバの上下に少量のシリカウールを詰
めた。第1表に示す被吸着物質の稀薄水溶液を各々調製
し、一定流量(0,5d/分)で当該カラムに通し、流
出液をフラクションコレクターで分取し、その吸光度を
自記分光々変針で測定した。得られた結果のうち代表例
を第1図に示す。得られた吸着曲線から破過容量(吸着
材1fあたり有機物質が洩れ出す・ までに吸着された
量、1111/f吸着材)および飽和吸着量(吸着材1
fあたシ吸着されたI−物質の最大量、wg/f吸着材
)を算出し、それらを第1表に示す。このことから、当
該中空糸状体は、種々の有機物質を吸着することが確認
さレタ。さらに、ベンゼン、トルエン、キシレン奮中沙
についても同様の操作を行ない、吸着量れることが確認
されたがこれらは揮発性であるため飽和吸着量、破過容
量の定量は行えなかった。
To prevent the cut fibers from flowing out or floating up, a small amount of silica wool was packed above and below the cut fibers. Prepare dilute aqueous solutions of the adsorbed substances listed in Table 1, pass through the column at a constant flow rate (0.5 d/min), collect the effluent with a fraction collector, and measure its absorbance using a self-recording spectrometer. did. A typical example of the obtained results is shown in FIG. From the obtained adsorption curve, we can determine the breakthrough capacity (the amount of organic matter adsorbed per 1f of adsorbent until it leaks out, 1111/f adsorbent) and the saturated adsorption amount (1f of adsorbent).
The maximum amount of I-substance adsorbed (wg/f adsorbent) was calculated and is shown in Table 1. From this, it was confirmed that the hollow fibers adsorb various organic substances. Furthermore, the same operation was performed for benzene, toluene, and xylene, and it was confirmed that the adsorption amount could be reduced, but since these are volatile, it was not possible to quantify the saturated adsorption amount and breakthrough capacity.

第1表 ポリエチレン中空糸状体の吸着性能Table 1: Adsorption performance of polyethylene hollow fibers

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

第1図はポリエチレン中空糸状体による有機物の吸着曲
線を示す。縦軸線原液の吸光度(DO)に対する処理液
の吸光度(D)の比(D/Do)を示す。
FIG. 1 shows the adsorption curve of organic substances by polyethylene hollow fibers. The vertical axis indicates the ratio (D/Do) of the absorbance (D) of the treatment solution to the absorbance (DO) of the stock solution.

Claims (1)

【特許請求の範囲】[Claims] 1)微小空孔が中空糸内壁面よシ外壁面に相互につなが
ったポリオレフィン多孔質中空短繊維からなる吸着材の
表面が親水化されていることを特徴とする水中の疎水性
有機物質および親水性有機物質の吸着剤
1) A hydrophobic organic substance in water and a hydrophilic material, characterized in that the surface of an adsorbent made of polyolefin porous hollow short fibers in which micropores are interconnected on the inner wall surface and the outer wall surface of the hollow fibers is made hydrophilic. adsorbent for organic substances
JP10157182A 1982-06-14 1982-06-14 Adsorbing material for organic substance Pending JPS58219940A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10157182A JPS58219940A (en) 1982-06-14 1982-06-14 Adsorbing material for organic substance

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10157182A JPS58219940A (en) 1982-06-14 1982-06-14 Adsorbing material for organic substance

Publications (1)

Publication Number Publication Date
JPS58219940A true JPS58219940A (en) 1983-12-21

Family

ID=14304086

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10157182A Pending JPS58219940A (en) 1982-06-14 1982-06-14 Adsorbing material for organic substance

Country Status (1)

Country Link
JP (1) JPS58219940A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102004036070A1 (en) * 2004-07-24 2006-02-16 Mann+Hummel Gmbh Water separator for use in diesel engine fuel system has granular or sintered filter to obtain purified water for environment discharge
US8409446B2 (en) 2009-08-21 2013-04-02 Cummins Filtration Ip, Inc. Automatic draining system to drain fluid from a filter

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52137026A (en) * 1976-04-30 1977-11-16 Toyobo Co Ltd Microporous hollow fibers and their production

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52137026A (en) * 1976-04-30 1977-11-16 Toyobo Co Ltd Microporous hollow fibers and their production

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102004036070A1 (en) * 2004-07-24 2006-02-16 Mann+Hummel Gmbh Water separator for use in diesel engine fuel system has granular or sintered filter to obtain purified water for environment discharge
US8409446B2 (en) 2009-08-21 2013-04-02 Cummins Filtration Ip, Inc. Automatic draining system to drain fluid from a filter

Similar Documents

Publication Publication Date Title
KR930008108B1 (en) Liquid Chromatography Method Using Microporous Hollow Fiber
Mukherjee et al. Novel carbon-nanoparticle polysulfone hollow fiber mixed matrix ultrafiltration membrane: Adsorptive removal of benzene, phenol and toluene from aqueous solution
US4102783A (en) Adsorbent process for oily materials
US5911883A (en) Flow-by solid phase extraction method
JPH09512745A (en) Composite membrane for solid phase extraction and reaction
WO1999000192A1 (en) Fresh air filter
JP2004066153A (en) Organic porous body having selective boron adsorption capability and boron removal module and ultrapure water production apparatus using the same
JP2010227757A (en) Composite separation membrane
BR112016000698B1 (en) HYDROPHILIZED POROUS HOLLOW FIBER MEMBRANE OF VINYLIDENE FLUORIDE, AND ITS PRODUCTION AND USE METHOD
US4431542A (en) Filter and method of producing the same
Wang et al. Fabrication of CMC-g-PAM superporous polymer monoliths via eco-friendly pickering-MIPEs for superior adsorption of methyl violet and methylene blue
GB1599822A (en) Process for the separation of mixtures of liquids which are insoluble in each other
KR970700532A (en) MAGNETIC PARTICLES, A METHOD FOR THE PREPARATION THEREOF AND THEIR USE IN THE PURIFICATION OF SOLUTIONS
JPS58219940A (en) Adsorbing material for organic substance
JPH11156104A (en) Oil water separation filter and its manufacture
Zambianchi et al. Polysulfone hollow porous granules prepared from wastes of ultrafiltration membranes as sustainable adsorbent for water and air remediation
JP7302185B2 (en) Adsorption/absorbent consisting of polyvinyl chloride resin porous beads
JP2000312802A (en) Oil-water separation filter
US8778189B2 (en) Use of an adsorbent for the removal of liquid, gaseous and/or dissolved constituents from a process stream
Khan et al. New insights on role of functionalized nanofibers in wastewater treatment
JP2602632Y2 (en) Liquid phase adsorption filter
JP2018015734A (en) Adsorbent-containing separation membrane and method for manufacturing the same
RU2042634C1 (en) Method for purification of waters against petroleum products
JP2690569B2 (en) Chlorine odor remover
Nakamoto et al. Fibrous mordenite zeolite-polymer composite adsorbents to methylene blue dye