JPS62212463A - Production of high-molecular porous article - Google Patents

Production of high-molecular porous article

Info

Publication number
JPS62212463A
JPS62212463A JP5362386A JP5362386A JPS62212463A JP S62212463 A JPS62212463 A JP S62212463A JP 5362386 A JP5362386 A JP 5362386A JP 5362386 A JP5362386 A JP 5362386A JP S62212463 A JPS62212463 A JP S62212463A
Authority
JP
Japan
Prior art keywords
solvent
resin
molding
bath
porous article
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
JP5362386A
Other languages
Japanese (ja)
Inventor
Junji Hosokawa
順二 細川
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.)
Komatsu Ltd
Original Assignee
Komatsu 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 Komatsu Ltd filed Critical Komatsu Ltd
Priority to JP5362386A priority Critical patent/JPS62212463A/en
Publication of JPS62212463A publication Critical patent/JPS62212463A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the titled porous article easily and inexpensively by controlling the pore size and porosity with relatively high accuracy, by dissolving a resin in a solvent, adjusting the viscosity and the concn. of the soln., molding the resulting resin soln., immersing the molding in a specified solvent bath and taking off it. CONSTITUTION:A resin A (e.g., nylon 6, 6) is dissolved in a solvent B (e.g., formic acid) and the viscosity and the concn. of the soln. are suitably adjusted. The resulting resin soln. 3 is molded by a molding means 1 such as an extruder. The molding 6 is immersed in a bath placed in a bath apparatus 2 for solvent extrusion, said bath containing a solvent C which is compatible with the solvent B and does not dissolve the resin A, whereby only the solvent B in the molding 6 is dissolved out and diffused in the solvent C and the resin A is solidified to form a porous article. The molding 6 in the form of the porous article is taken off through a roller 7 to obtain the titled porous article.

Description

【発明の詳細な説明】 産業上の利用分骨 本発明は高分子多孔体の製造方法に関するものである。[Detailed description of the invention] Industrial use bone The present invention relates to a method for producing a porous polymer body.

従来の技術 従来のこの種の製造方法は、 (1)樹脂を溶媒に溶かし、これに非溶剤を加え、成形
後まず溶媒を飛ばし、非溶剤の球径微粒子液を含む薄膜
を作る。ついで高温で非溶剤を除去しその跡を微細孔と
して残す。
2. Prior Art The conventional manufacturing method of this type is as follows: (1) A resin is dissolved in a solvent, a non-solvent is added thereto, and after molding, the solvent is first evaporated to form a thin film containing a liquid of spherical fine particles of the non-solvent. The non-solvent is then removed at high temperature, leaving traces of it as micropores.

(2)  押出し成形後細かいエンボス加工やパンチン
グにて膜面に傷又は穴を付けた後延伸することにより所
要の開裂口を作る。
(2) After extrusion molding, the film surface is scratched or holed by fine embossing or punching, and then stretched to create the required cleavage openings.

(3)  あらかじめある溶剤で溶出除去可能な固形粉
末を樹脂中に混入しておき成形後固形粉末を除去し多孔
体とする。
(3) Solid powder that can be eluted and removed with a certain solvent is mixed into the resin in advance, and after molding, the solid powder is removed to form a porous body.

などがある。and so on.

上記した(+)の類似法としてモノマー又は中程度重合
物中に非溶剤を混ぜ同様の操作もできる。
As a similar method to the above (+), a similar operation can also be performed by adding a non-solvent to the monomer or moderately polymerized product.

発明が解決しようとする問題点 (1) 、 (3)に示す従来技術については、溶媒種
類、濃度、非溶剤(又は固形粉末)種類濃度、樹脂分子
量、温度、樹脂の押出圧などのバロメータが複雑に関係
し合うため一つの製品に対する最適条件を探し出すのが
難しくまた製造管理も非常に難しく、さらにパラメータ
が多すぎるため孔径、気孔率などの細かい制御が難しい
ものであった。
Regarding the conventional techniques shown in Problems (1) and (3) to be solved by the invention, barometers such as solvent type, concentration, non-solvent (or solid powder) type and concentration, resin molecular weight, temperature, resin extrusion pressure, etc. Because of the complex relationships involved, it is difficult to find the optimal conditions for a single product, and manufacturing management is also extremely difficult.Furthermore, because there are too many parameters, fine control of pore diameter, porosity, etc. is difficult.

また上記(2)の従来技術は孔径の制御が難しくまた意
識的にクラッチを生じさせるため強度が低下する。この
方法はポリプロピレン等一部の樹脂にしか適用できない
という欠点もある。
Further, in the conventional technique (2) above, it is difficult to control the hole diameter and the strength is reduced because a clutch is intentionally generated. This method also has the disadvantage that it can only be applied to some resins such as polypropylene.

前述以外にも高分子多孔体の製造方法はあるが一般的に
、 ■ 製品製造上、パラメータが多いので細かいコントロ
ールが難しく又製造管理もやっかいである。
There are other methods for producing porous polymers other than those described above, but in general: (1) Since there are many parameters in product production, detailed control is difficult and production management is troublesome.

■ 各製品についての最適条件を探すのが難しく多くの
製品群を持ちにくい。
■ It is difficult to find the optimal conditions for each product and it is difficult to have many product groups.

■ 樹脂の成形工程と孔を作る工程を一緒にできない。■ It is not possible to do the resin molding process and the hole making process at the same time.

という共通の欠点がある。There is a common drawback.

発明の目的 本発明は上記の事情に鑑みなされたもので、高分子多孔
体の製造上のパラメータが極めて少なくなり、このパラ
メータの減少により孔径、気孔率の制御を比較的精度よ
く行うことができるばかりか高分子多孔体の成形と孔形
成が同時に行え得る高分子多孔体の製造方法を提供する
ことを目的とする。
Purpose of the Invention The present invention has been made in view of the above circumstances, and the number of parameters for manufacturing porous polymer materials is extremely reduced, and by reducing these parameters, the pore diameter and porosity can be controlled with relative precision. Moreover, it is an object of the present invention to provide a method for producing a porous polymer body in which molding of the porous polymer body and pore formation can be performed simultaneously.

問題点を解決するための手段及び作用 上記の目的を達成するために本発明は、樹脂Aを溶媒B
で溶解して成る溶解侮脂3を成形手段により成形した後
、この成形体6を、溶媒Bと相溶性があり且つ樹脂Aを
溶解しない溶剤Cの浴中に浸し、溶媒Bを樹脂A間より
浴中に拡散押出するようにしたものである。
Means and Effects for Solving the Problems In order to achieve the above objects, the present invention provides a method for replacing resin A with solvent B.
After molding the dissolved fat 3 by a molding means, the molded body 6 is immersed in a bath of a solvent C that is compatible with the solvent B and does not dissolve the resin A, and the solvent B is mixed between the resin A and the resin A. It is designed to be diffused and extruded into a bath.

実施例 以下、本発明の実施例を図面に基づいて説明する。図面
中1は押出機、2は溶媒押出用浴装置である。
Embodiments Hereinafter, embodiments of the present invention will be described based on the drawings. In the drawings, 1 is an extruder, and 2 is a solvent extrusion bath device.

前記押出機!にはあらかじめ粘度、濃度が調整された溶
解樹脂3(例えば、(樹脂Aとしてナイロン6.6)+
(溶媒Bとしてぎ酸))が供給しである。
Said extruder! The molten resin 3 whose viscosity and concentration have been adjusted in advance (for example, (nylon 6.6 as resin A)
(formic acid as solvent B)) is supplied.

また溶媒押出用浴装置2内には溶剤C(例えば水)が入
れである。
The solvent extrusion bath device 2 also contains a solvent C (for example, water).

前記押出機1の作動によりこれの先端の金型5によりシ
ート状に成形された溶解樹脂3より成る成形体6は直ち
に溶媒押出用浴装置2内の溶剤Cの浴中に浸される。こ
の溶剤Cは溶解樹脂3中の溶媒Bとは相溶性が良いが溶
解樹脂3中の樹脂Aと化学変化を起こしたり溶かしたり
することは一切ない。
When the extruder 1 is operated, the molded body 6 made of the melted resin 3 formed into a sheet by the mold 5 at the tip of the extruder 1 is immediately immersed in the bath of the solvent C in the bath device 2 for solvent extrusion. This solvent C has good compatibility with the solvent B in the dissolved resin 3, but does not cause any chemical change or dissolve the resin A in the dissolved resin 3.

そこで溶媒押出用浴装置2に浸された溶解樹脂3のうち
溶媒Bだけが溶剤Cの浴中に拡散して行く。
Then, of the dissolved resin 3 immersed in the solvent extrusion bath device 2, only the solvent B diffuses into the solvent C bath.

溶解樹脂3の溶媒Bの分子すがあった箇所に溶剤Cの分
子Cあるいは拡散した溶媒Bの分子すが入9込む。濃度
は溶媒B(溶剤Cであるので表面の溶媒Hの分子すはほ
とんどすべてが溶剤Cの分子Cと入れかわる。このよう
にして表面より少しづつ内部の溶媒Bの分子すが分子C
と入れ変って行き、最後はすべてが分子Qと入れかわる
(第2図参照)。
Molecules C of solvent C or molecules of diffused solvent B are inserted into the portions of dissolved resin 3 where molecules of solvent B were present. The concentration is determined by the concentration of solvent B (since it is solvent C, almost all of the molecules of solvent H on the surface are replaced with molecules C of solvent C. In this way, the molecules of solvent B inside the surface gradually change to molecules C.
, and finally all of them are replaced with molecule Q (see Figure 2).

この過程において、初めはゾル状であった樹脂Aは溶媒
Hの拡散により徐々に自由を失なって行き、ついには完
全に固化し樹脂Aに対し何ら影響力のない溶剤Cを孔内
に含む多孔体になる。
In this process, resin A, which was initially in a sol state, gradually loses its freedom due to the diffusion of solvent H, and finally solidifies completely and contains solvent C, which has no influence on resin A, in the pores. It becomes porous.

このようにして多孔体になされた成形体6は四−ラフに
引き取られて行く。
The molded body 6 formed into a porous body in this manner is taken up in a four-rough manner.

上記した高分子多孔体の製造方法において任意の孔径、
気孔率に対し、溶解樹脂3の濃度、粘度が決まる。
In the above-described method for producing a porous polymer, any pore size,
The concentration and viscosity of the dissolved resin 3 are determined based on the porosity.

また必要により第2の溶剤や粘度調整剤、固体状粉末な
どを添加してもよい。
Further, if necessary, a second solvent, a viscosity modifier, a solid powder, etc. may be added.

上記した高分子多孔体の製造方法で製造される高分子多
孔体の形状はシートに限らずチューブ状や異形でも良い
し、成形手段は押出成形に限らず浸漬成形でもよい。
The shape of the porous polymer body produced by the method for producing a porous polymer body described above is not limited to a sheet, but may be a tube shape or an irregular shape, and the shaping means is not limited to extrusion molding, but may also be dip molding.

すなわち第3図乃至第5図に示すように溶解樹@3の浴
中にステンレス棒8を挿入した後これを浴中から引き出
してステンレス棒8の局面に溶解樹脂3を膜状に耐着さ
せる。
That is, as shown in FIGS. 3 to 5, a stainless steel rod 8 is inserted into a bath of melted resin @ 3 and then pulled out of the bath to allow the melted resin 3 to stick to the surface of the stainless steel rod 8 in a film form. .

このステンレス棒8を溶剤Cの浴中に浸たし、溶解樹脂
3中の溶媒Bを拡散させ溶媒Bの分子すを溶剤Cの分子
Cと入れ替えるようにしてもよい。
This stainless steel rod 8 may be immersed in a bath of solvent C to diffuse the solvent B in the dissolved resin 3 and replace the molecules of solvent B with the molecules C of solvent C.

このようにすることにより多孔質チューブを製造するこ
とができる。第6図に多孔質チューブの断面を示す。第
4図より微細な均一な孔径の多孔部9が解かる。
By doing so, a porous tube can be manufactured. FIG. 6 shows a cross section of the porous tube. From FIG. 4, it can be seen that the porous portion 9 has fine and uniform pore diameters.

発明の効果 以上詳述したように、本発明に係る高分子多孔体の製造
方法は、樹脂Aを溶媒Bで溶解して成る溶解樹脂3を成
形手段により成形した後、この成形体6を、溶媒Bと相
溶性があり且つ樹脂Aを溶解しない溶剤Cの浴中に浸し
、溶媒Bを樹脂A間より浴中に拡散押出するよ5にした
ことを特徴とするものである。
Effects of the Invention As detailed above, in the method for producing a porous polymer according to the present invention, after molding the melted resin 3 obtained by dissolving resin A in solvent B using a molding means, this molded body 6 is It is characterized in that it is immersed in a bath of solvent C that is compatible with solvent B and does not dissolve resin A, and that solvent B is diffused and extruded from between resin A into the bath.

したがって、高分子多孔体は樹脂と適当な溶媒を決めれ
ば溶媒濃度、溶解樹脂粘度によりほぼ決まる。
Therefore, once a resin and a suitable solvent are selected, the porous polymer material is determined approximately by the solvent concentration and the viscosity of the dissolved resin.

このように高分子多孔体の製造上のパラメータが極めて
少なくなるしこのパラメータの減少により孔径、気孔率
の制御を比較的精度よく行うことができる。
In this way, the number of parameters for manufacturing the porous polymer material is extremely reduced, and by reducing these parameters, the pore diameter and porosity can be controlled with relative precision.

また高分子多孔体の成形と孔形成が同時に行え得るし高
分子多孔体の孔の孔径が表面から内部にかけて均一にな
るし、加熱などする必要がなく省エネルギー化になる。
Furthermore, the molding of the porous polymer and the formation of pores can be performed simultaneously, the pore diameter of the porous polymer becomes uniform from the surface to the inside, and there is no need for heating, resulting in energy savings.

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

第1図は本発明一実施例の説明図、第2図は高分子多孔
体の分子交換モデルの説明図、@3図乃至第5図は本発
明の他の実施例の説明図、第6図は高分子多孔体の断面
図である。 3は溶解樹脂、6は成形体、Aは樹脂、Bは溶媒、Cは
溶剤。
Fig. 1 is an explanatory diagram of one embodiment of the present invention, Fig. 2 is an explanatory diagram of a molecular exchange model of a porous polymer body, @Figs. 3 to 5 are explanatory diagrams of other embodiments of the present invention, and Fig. 6 The figure is a cross-sectional view of a porous polymer body. 3 is a dissolved resin, 6 is a molded article, A is a resin, B is a solvent, and C is a solvent.

Claims (1)

【特許請求の範囲】[Claims] 樹脂Aを溶媒Bで溶解して成る溶解樹脂3を成形手段に
より成形した後、この成形体6を、溶媒Bと相溶性があ
り且つ樹脂Aを溶解しない溶剤Cの浴中に浸し、溶媒B
を樹脂A間より浴中に拡散押出するようにしたことを特
徴とする高分子多孔体の製造方法。
After molding the melted resin 3 made by dissolving resin A in solvent B using a molding means, this molded body 6 is immersed in a bath of solvent C that is compatible with solvent B and does not dissolve resin A.
A method for producing a porous polymer material, characterized in that the material is diffused and extruded from between resin A into a bath.
JP5362386A 1986-03-13 1986-03-13 Production of high-molecular porous article Pending JPS62212463A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5362386A JPS62212463A (en) 1986-03-13 1986-03-13 Production of high-molecular porous article

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5362386A JPS62212463A (en) 1986-03-13 1986-03-13 Production of high-molecular porous article

Publications (1)

Publication Number Publication Date
JPS62212463A true JPS62212463A (en) 1987-09-18

Family

ID=12948033

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5362386A Pending JPS62212463A (en) 1986-03-13 1986-03-13 Production of high-molecular porous article

Country Status (1)

Country Link
JP (1) JPS62212463A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000006616A1 (en) * 1998-07-30 2000-02-10 3M Innovative Properties Company Process and apparatus for removing impurities from polymers

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000006616A1 (en) * 1998-07-30 2000-02-10 3M Innovative Properties Company Process and apparatus for removing impurities from polymers
US6160086A (en) * 1998-07-30 2000-12-12 3M Innovative Properties Company Process for removing impurities from polymers

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