JPH10195231A - Production of polyolefin-based porous molding product - Google Patents

Production of polyolefin-based porous molding product

Info

Publication number
JPH10195231A
JPH10195231A JP9013305A JP1330597A JPH10195231A JP H10195231 A JPH10195231 A JP H10195231A JP 9013305 A JP9013305 A JP 9013305A JP 1330597 A JP1330597 A JP 1330597A JP H10195231 A JPH10195231 A JP H10195231A
Authority
JP
Japan
Prior art keywords
polyolefin
water
parts
molding product
soluble polymer
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
JP9013305A
Other languages
Japanese (ja)
Other versions
JP3658618B2 (en
Inventor
Masahide Yamamoto
正秀 山本
Yasuo Namita
靖夫 波田
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.)
Nitto Kogyo Co Ltd
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
Nitto Kogyo 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 Agency of Industrial Science and Technology, Nitto Kogyo Co Ltd filed Critical Agency of Industrial Science and Technology
Priority to JP01330597A priority Critical patent/JP3658618B2/en
Publication of JPH10195231A publication Critical patent/JPH10195231A/en
Application granted granted Critical
Publication of JP3658618B2 publication Critical patent/JP3658618B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain the subject molding product having pores with a large diameter in a good productivity by melting and kneading a polyolefin resin with a water-soluble polymer and a solubilizing agent and molding the kneaded material and removing the water-soluble polymer in the molding product. SOLUTION: (A) A polyolefin resin having preferably 0.1-10 melt index (MI) (e.g. polypropylene resin) in an amount of 35-85 pts.wt. is melted and kneaded with (B) 10-60 pts.wt. water-soluble polymer which is a thermoplastic polymer, preferably having <=10 MI and containing polyvinyl alcohol component and (C) 5-30 pts.wt. solubilizer for solubilizing the components A and B (e.g. a block polymer of a polyolefin and a polyether) to provide a melted mixture. Then, the melted mixture is molded by discharging, e.g. from an extruder to provide a molding product. Then, the molding product is immersed in water and the component B in the molding product is removed by extraction and as necessary, the molding product is dried to provide the objective polyolefin-based porous molding products.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、流体用各種フィルター
に用いるポリオレフィン系多孔質成形体の製造方法に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a polyolefin porous molded article used for various filters for fluids.

【0002】[0002]

【従来の技術】気体や液体の流体用フィルターは、空調
機器や、食品工業、電子産業、廃水処理その他の各種分
野において使用されているが、その流体用フィルターに
は多孔質中空糸や多孔質フィルム等の多孔質成形体を用
いることが行われている。例えばポリ酢酸セルロースや
ポリスルホン等を用いた多孔質中空糸や多孔質フィルム
等は、濾過、限外濾過、透析等の液体処理や気体分離等
の気体処理に利用されている。これらの多孔質成形体の
製造は主として湿式法により行われている。すなわち、
上記ポリマー類を溶剤に溶解した後、ノズル又はダイス
から凝固浴中に吐出し、浸漬して凝固させ、その後凝固
体からこれに含まれる溶剤の揮発分を除去し、中空糸又
は多孔質フィルムとする方法である。この方法は、素材
のポリマーがポリオレフィン樹脂の場合には溶剤に対す
る溶解性を良くすることができず、その混合液は組成が
不均一となり易いため、ノズル又はダイスからその混合
液を吐出することも均一に行われ難く、そのため凝固浴
中で得られる凝固体も不均一になり、そこから除去され
た溶剤の跡に形成される細孔の分布も異なり、均一な多
孔質成形体を得ることができないという問題がある。
2. Description of the Related Art Filters for gas and liquid fluids are used in air conditioners, the food industry, the electronics industry, wastewater treatment and other various fields. Use of a porous molded body such as a film has been performed. For example, a porous hollow fiber or a porous film using cellulose acetate, polysulfone, or the like is used for liquid treatment such as filtration, ultrafiltration, and dialysis, and gas treatment such as gas separation. The production of these porous molded bodies is mainly performed by a wet method. That is,
After dissolving the above polymers in a solvent, it is discharged into a coagulation bath from a nozzle or a die, immersed and coagulated, and then the volatiles of the solvent contained therein are removed from the coagulated body, and a hollow fiber or a porous film and How to In this method, when the polymer of the raw material is a polyolefin resin, the solubility in a solvent cannot be improved, and the mixed liquid tends to have a non-uniform composition, so that the mixed liquid may be discharged from a nozzle or a die. It is difficult to perform uniformly, so the coagulated body obtained in the coagulation bath also becomes non-uniform, the distribution of pores formed in the trace of the solvent removed therefrom is different, and it is possible to obtain a uniform porous molded body. There is a problem that can not be.

【0003】[0003]

【発明が解決しようとする課題】このような問題を解決
できる方法として溶融による成形法がよく用いられてい
る。すなわち、ポリオレフィン樹脂を溶融成形後、延伸
処理することにより非晶部を引き延ばし、その延伸につ
いて行けない組織の弱い部分に短冊状の微細孔を形成さ
せる方法である。しかし、この方法では延伸処理時の温
度、延伸の程度、成形体の膜厚等により微細孔の大きさ
や数、さらにはその分布が異なり、これらを均一にしよ
うとするとこれらの各因子のバランスをとる必要があ
り、そのためには微細孔を0.1μm程度にしかでき
ず、結局、その大きさをあまり大きくできず、成形体の
厚さも制限されるという問題がある。また、ポリオレフ
ィン樹脂を用いた多孔質成形体の他の製造方法として、
液状油を混合したポリオレフィン樹脂の溶融混合物を成
形後、冷却し、溶媒によりその成形体中の液状物を抽出
除去する方法も提案されている。しかし、この方法は液
状油が多過ぎると成形時の材料強度が弱くなり、所望の
強度の成形体が得られないので、液状油の添加量は制限
され、そのため形成される微細孔の孔径も1μmよりは
大きくできないという問題がある。
As a method for solving such a problem, a molding method by melting is often used. That is, this method is a method in which a polyolefin resin is melt-molded and then stretched to stretch an amorphous portion, thereby forming strip-shaped micropores in a weak portion of the structure that cannot be stretched. However, in this method, the size and number of micropores and the distribution thereof vary depending on the temperature at the time of stretching, the degree of stretching, the film thickness of the molded body, and the like. Therefore, there is a problem that the size of the micropores can be reduced to only about 0.1 μm, so that the size of the micropores cannot be increased so much, and the thickness of the compact is limited. Further, as another manufacturing method of a porous molded body using a polyolefin resin,
A method has also been proposed in which a molten mixture of a polyolefin resin mixed with a liquid oil is molded, then cooled, and a liquid material in the molded body is extracted and removed with a solvent. However, in this method, if the amount of the liquid oil is too large, the material strength at the time of molding becomes weak, and a molded body having a desired strength cannot be obtained. There is a problem that it cannot be made larger than 1 μm.

【0004】本発明の第1の目的は、孔径の大きい微細
孔を有するポリオレフィン系多孔質成形体の製造方法を
提供することにある。本発明の第2の目的は、フィル
ム、プレートや中空糸、管状体等において膜厚や太さ等
の成形体形状を幅広く選択することができるポリオレフ
ィン系多孔質成形体の製造方法を提供することにある。
本発明の第3の目的は、条件設定が簡単に行なえ、生産
性がよく、しかも微細孔の大きさ、数や分布が均一なポ
リオレフィン系多孔質成形体の製造方法を提供すること
にある。
A first object of the present invention is to provide a method for producing a polyolefin porous molded article having fine pores having a large pore diameter. A second object of the present invention is to provide a method for producing a polyolefin-based porous molded body, which can widely select a molded body shape such as a film thickness and a thickness in a film, a plate, a hollow fiber, a tubular body, and the like. It is in.
A third object of the present invention is to provide a method for producing a polyolefin-based porous molded body that can easily set conditions, has good productivity, and has a uniform size, number, and distribution of micropores.

【0005】[0005]

【課題を解決するための手段】本発明は、上記課題を解
決するために、(1)、ポリオレフィン樹脂(A)35
〜85重量部、水溶性ポリマー(B)10〜60重量部
及び該(A)成分と(B)成分を相溶させる相溶化剤
(C)5〜30重量部を溶融混合する溶融混合物生成工
程と、該溶融混合物を成形体に成形する成形工程と、該
成形体中の上記(B)成分を水で抽出除去する水溶性ポ
リマー抽出除去工程を有するポリオレフィン系多孔質成
形体の製造方法を提供するものである。また、本発明
は、(2)、水溶性ポリマー(B)がポリビニルアルコ
ール成分を含むポリマーである上記(1)の多孔質成形
体の製造方法、(3)、相溶化剤(C)がポリオレフィ
ンとポリエーテルからなるブロックポリマーである上記
(1)又は(2)のポリオレフィン系多孔質成形体の製
造方法を提供するものである。
According to the present invention, there is provided (1) a polyolefin resin (A) 35 for solving the above-mentioned problems.
A melt-mixing step of melt-mixing the water-soluble polymer (B) with 10 to 60 parts by weight and the compatibilizer (C) with which the component (A) and the component (B) are compatible with each other. And a method for producing a polyolefin-based porous molded article, comprising: a molding step of molding the molten mixture into a molded article; and a water-soluble polymer extraction / removal step of extracting and removing the component (B) in the molded article with water. Is what you do. The present invention also provides (2) the method for producing a porous molded article according to (1), wherein the water-soluble polymer (B) is a polymer containing a polyvinyl alcohol component, (3), wherein the compatibilizer (C) is a polyolefin. The present invention provides a method for producing a polyolefin-based porous molded article according to the above (1) or (2), which is a block polymer composed of a polyether and a polyether.

【0006】次に本発明を詳細に説明する。本発明にお
いて、「ポリオレフィン樹脂(A)」とは、ポリプロピ
レン樹脂、ポリエチレン樹脂等を言い、特に制限はな
い。「ポリオレフィン系多孔質成形体」とはポリオレフ
ィン樹脂を主成分とする多孔質成形体の意味である。成
形作業性からいってMI(メルトインデックス)が0.
1〜10のポリオレフィン樹脂が好ましい。また、本発
明において、「水溶性ポリマー(B)」とは、ある程度
の強度と成形性を有する高分子量の水溶性ポリマーであ
れば特に制限はないが、MIは10以下(大きくて1
0)が好ましい。特に、ポリビニルアルコール成分を含
む熱可塑性ポリマーが好ましい。また、本発明におい
て、「相溶化剤(C)」としては、ポリオレフィン及び
水溶性ポリマーの相溶化を促進するものであれば特に制
限はないが、ポリオレフィンと親水性ポリマーのブロッ
ク型ポリマーであることが好ましい。例えばポリオレフ
ィンとポリエーテルのブロックポリマーが挙げられる。
Next, the present invention will be described in detail. In the present invention, the “polyolefin resin (A)” refers to a polypropylene resin, a polyethylene resin, or the like, and is not particularly limited. “Polyolefin-based porous molded article” means a porous molded article containing a polyolefin resin as a main component. The MI (melt index) is 0.1 in terms of molding workability.
1-10 polyolefin resins are preferred. In the present invention, the “water-soluble polymer (B)” is not particularly limited as long as it is a high-molecular-weight water-soluble polymer having a certain level of strength and moldability.
0) is preferred. In particular, a thermoplastic polymer containing a polyvinyl alcohol component is preferable. In the present invention, the “compatibilizer (C)” is not particularly limited as long as it promotes the compatibilization of the polyolefin and the water-soluble polymer, but it is a block polymer of the polyolefin and the hydrophilic polymer. Is preferred. For example, a block polymer of polyolefin and polyether can be used.

【0007】上記(A)、(B)及び(C)成分の混合
割合は、(A)成分が35〜85重量部、(B)成分が
10〜60重量部、(C)成分が5〜30重量部であ
る。(A)成分が35重量部より少ないと汎用性樹脂の
ポリオレフィン樹脂を用いる特色を出し難く、85重量
部より多いと微細孔の数が少な過ぎる。また、(B)成
分が10重量部より少ないと微細孔の数が少な過ぎ、6
0重量部より多いと微細孔の数が多過ぎる。また、
(C)成分が5重量部より少ないと(A)成分と(B)
成分の相溶性を良く出来ず、30重量部より多くてもそ
の相溶性の改善の効果はそれぼど増加はしない。
The mixing ratio of the above components (A), (B) and (C) is 35 to 85 parts by weight for component (A), 10 to 60 parts by weight for component (B), and 5 to 60 parts by weight for component (C). 30 parts by weight. When the amount of the component (A) is less than 35 parts by weight, it is difficult to obtain a characteristic using a polyolefin resin as a general-purpose resin, and when the amount is more than 85 parts by weight, the number of micropores is too small. If the component (B) is less than 10 parts by weight, the number of micropores is too small, and
If it is more than 0 parts by weight, the number of micropores is too large. Also,
If the component (C) is less than 5 parts by weight, the components (A) and (B)
The compatibility of the components cannot be improved, and even if it exceeds 30 parts by weight, the effect of improving the compatibility does not increase much.

【0008】本発明のポリオレフィン系多孔質成形体を
製造するには、 上記のポリオレフィン樹脂(A)、
水溶性ポリマー(B)及び相溶化剤(C)を混合する
が、これには例えば通常用いられているブレンダー類を
用いればよい。次に、 この混合物を溶融混合機で溶
融してさらに混合し、中空糸紡糸用ノズル、フィルム或
いはシート成形用ダイスを取り付けた押出機から通常の
方法により吐出して成形すればよい。さらに 得られ
た成形体を水に浸漬し、成形体中の水溶性ポリマーを抽
出除去する。この際熱水を使用することにより、水溶性
ポリマーの溶出速度を促進することができる。そして、
その抽出処理された成形体を取り出して、風乾、送
風乾燥、真空乾燥等通常利用されている乾燥方法により
乾燥し、ポリオレフィン系多孔質成形体を完成させる。
このようにしてポリオレフィン系多孔質成形体を製造す
ると、水溶性ポリマー(B)を使用しているので、それ
自身に成形性があり、上述のように溶剤や液状油を用い
る場合より成形が容易であり、フィルムや中空糸の成形
体の形状の選択幅を広げることができ、例えば厚さが数
mmのプレートや中空糸より外径及び内径の大きい管状
体を製造することもできる。また、(C)成分を使用す
ることにより(A)成分と(B)成分の相溶性が良くな
り、これら成分の溶融混合物において各成分の良好な分
散状態が得られ、その状態で成形されるので、後の工程
を経て得られる多孔質成形体は微細孔の大きさ、数、分
布を均一にし易い。また、(B)成分を抽出除去する際
には水を使用でき、しかもその温度を変えて抽出速度を
調整することができ、(B)成分の添加量を増やしても
成形時の成形体の強度を液状油のように減少させないで
済むことや、上記した延伸法のような製造条件の微妙な
バランスをとる必要がない等のこととともに、複雑な工
程条件管理が必要ではなく、それだけ種々の形状の多孔
質成形体を製造することも容易であり、特に孔径がμm
〜数10μmのように大きい微細孔の多孔質成形体を製
造することができるようになった効果は大きい。また、
有機溶剤や液状油を使用しないで済むので後処理の問題
もなく、生産性もよい。
In order to produce the polyolefin porous molded article of the present invention, the above-mentioned polyolefin resin (A)
The water-soluble polymer (B) and the compatibilizer (C) are mixed, and for example, a commonly used blender may be used. Next, the mixture may be melted and further mixed by a melt mixer, and may be discharged and molded by a usual method from an extruder equipped with a hollow fiber spinning nozzle, a film or sheet forming die. Further, the obtained molded body is immersed in water to extract and remove the water-soluble polymer in the molded body. At this time, the dissolution rate of the water-soluble polymer can be accelerated by using hot water. And
The molded body subjected to the extraction treatment is taken out and dried by a commonly used drying method such as air drying, blast drying, and vacuum drying to complete a polyolefin-based porous molded body.
When the polyolefin-based porous molded article is manufactured in this manner, since the water-soluble polymer (B) is used, the polyolefin-based porous molded article itself has moldability, and is easier to mold than when a solvent or liquid oil is used as described above. Thus, it is possible to widen the selection range of the shape of the molded product of the film or the hollow fiber, for example, it is possible to produce a plate having a thickness of several mm or a tubular body having an outer diameter and an inner diameter larger than that of the hollow fiber. Further, by using the component (C), the compatibility between the component (A) and the component (B) is improved, and a good dispersion state of each component is obtained in a molten mixture of these components, and the mixture is molded in that state. Therefore, the size, the number, and the distribution of the fine pores are easily uniform in the porous molded body obtained through the subsequent steps. Further, water can be used to extract and remove the component (B), and the temperature can be changed to adjust the extraction speed. Along with the fact that the strength does not need to be reduced like liquid oil and that there is no need to balance the manufacturing conditions as in the above-mentioned drawing method, complicated process condition management is not necessary, and various It is also easy to produce a porous molded body having a shape,
The effect of being able to manufacture a porous molded body having fine pores as large as 10 μm is great. Also,
Since there is no need to use an organic solvent or liquid oil, there is no problem of post-treatment and the productivity is good.

【0009】[0009]

【発明の実施の形態】詳細は以下の実施例で説明する
が、水溶性ポリマー(B)を用いたのでそれ自身の成形
性、強度が溶剤や液状油よりははるかに優れ、また、水
で抽出除去できるので微細孔形成工程の条件設定が容易
になり、相溶化剤(C)によりポリオレフィン樹脂
(A)と(B)成分の相溶性を改善((C)のポリオレ
フィンはポリオレフィン樹脂(A)と親和性があり、ポ
リエーテルは親水性であり水溶性ポリマー(B)と親和
性があり、(C)成分は(A)成分と(B)成分の両方
に親和性があることにより両者の混ざりを良くする)し
て均一な組成物からなる成形体が得られ、これらにより
汎用性樹脂の(A)成分を用いた多孔質の中空糸、フィ
ルムのみならず管状体、プレート等のポリオレフィン系
多孔質成形体をその形状、微細孔の孔径等の選択幅を広
くして得られる。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS As will be described in detail in the following examples, since the water-soluble polymer (B) is used, its own moldability and strength are far superior to those of solvents and liquid oils. Since extraction and removal can be performed, it is easy to set the conditions of the micropore forming step, and the compatibility of the polyolefin resin (A) and the component (B) is improved by the compatibilizer (C). And the polyether is hydrophilic and has an affinity for the water-soluble polymer (B), and the component (C) has an affinity for both the component (A) and the component (B). To improve the mixing) to obtain a molded product composed of a uniform composition, which is used not only for porous hollow fibers and films using the component (A) of a general-purpose resin, but also for polyolefin-based materials such as tubular bodies and plates. The shape of the porous compact Obtained by widening the selection range of the pore diameter of the micropores.

【0010】[0010]

【実施例】以下に実施例によって本発明をさらに詳細に
説明するが、本発明はこれらに限定されるものではな
い。また、各実施例における部はいずれも重量部であ
る。 実施例1 ポリプロピレン樹脂(MI 0.5)47部、熱可塑性
ポリビニルアルコール(MI 2)42部、ポリプロピ
レン/ポリエーテルブロック型ポリマー(MI20)1
1部、メチレンビスステアリン酸アマイド(滑剤)3部
をブレンダーで混合し、その混合物を押出機において2
10℃で溶融混練し、ペレットを製造した。このペレッ
トを用いて中空糸成形用ノズルを設置した押出機により
成形し、中空糸状成形体(糸径1mmφ、膜厚150μ
m)を得た。この成形体を70℃の熱水に12時間浸漬
し、ついで送風式乾燥機で60℃、6時間乾燥し、多孔
質中空糸を得た。この多孔質中空糸について写真法によ
り調べたところ、空隙率は41%、平均微細孔径は20
μmであった。
EXAMPLES The present invention will be described in more detail with reference to the following Examples, but it should not be construed that the present invention is limited thereto. All parts in each example are parts by weight. Example 1 47 parts of polypropylene resin (MI 0.5), 42 parts of thermoplastic polyvinyl alcohol (MI 2), polypropylene / polyether block type polymer (MI20) 1
1 part of methylene bisstearic acid amide (lubricant) was mixed in a blender, and the mixture was mixed in an extruder for 2 hours.
The mixture was melt-kneaded at 10 ° C. to produce pellets. The pellets are formed by an extruder equipped with a hollow fiber forming nozzle, and are formed into a hollow fiber shaped body (a fiber diameter of 1 mmφ, a film thickness of 150 μm)
m). This molded body was immersed in hot water of 70 ° C. for 12 hours, and then dried at 60 ° C. for 6 hours with a blow dryer to obtain a porous hollow fiber. When this porous hollow fiber was examined by a photographic method, the porosity was 41% and the average fine pore diameter was 20%.
μm.

【0011】実施例2 実施例1において、ポリプロピレン樹脂(MI 0.
5)67部、熱可塑性ポリビニルアルコール(MI
0.4〜0.7)27部、ポリプロピレン/ポリエーテ
ルブロック型ポリマー(MI 20)6部、メチレンビ
スステアリン酸アマイド3部としたこと以外は同様にし
て中空糸状成形体(糸径1mmφ、膜厚130μm)を
得た。この成形体について実施例1と同様に抽出除去処
理を行なった後乾燥させ、多孔質中空糸を得、これにつ
いても実施例1と同様に測定したところ、空隙率は26
%、平均微細孔径は6μmであった。
Example 2 In Example 1, a polypropylene resin (MI 0.
5) 67 parts, thermoplastic polyvinyl alcohol (MI
0.4-0.7) 27 parts, a polypropylene / polyether block type polymer (MI 20) 6 parts, and methylene bisstearic acid amide 3 parts, except that the hollow fiber-shaped molded article (filament diameter 1 mmφ, membrane 130 μm). The molded body was subjected to the extraction and removal treatment in the same manner as in Example 1 and then dried to obtain a porous hollow fiber. When the porous hollow fiber was measured in the same manner as in Example 1, the porosity was 26.
%, The average micropore diameter was 6 μm.

【0012】実施例3 実施例1において、ポリプロピレン樹脂(MI 2)3
2部、熱可塑性ポリビニルアルコール(MI 10)6
0部、ポリプロピレン/ポリエーテルブロック型ポリマ
ー(MI 20)8部、メチレンビスステアリン酸アマ
イド3部としたこと以外は同様にしてペレットを製造
し、このペレットを用いて熱プレスにより230℃でシ
ート状成形体(厚さ1mm)を作製した。この成形体に
ついて実施例1と同様に抽出除去処理を行なった後乾燥
させ、多孔質シート状成形体を得、これについても実施
例1と同様に測定したところ、空隙率は64%、平均微
細孔径は40μmであった。
Example 3 In Example 1, a polypropylene resin (MI 2) 3
2 parts, thermoplastic polyvinyl alcohol (MI 10) 6
Pellets were produced in the same manner except that 0 parts, 8 parts of a polypropylene / polyether block type polymer (MI 20) and 3 parts of methylene bisstearic acid amide were used. A molded body (1 mm thick) was produced. The molded body was subjected to the extraction removal treatment in the same manner as in Example 1, and then dried to obtain a porous sheet-shaped molded body. The porous body was measured in the same manner as in Example 1. The porosity was 64% and the average fineness was small. The pore size was 40 μm.

【0013】実施例4 実施例3において、ポリプロピレン樹脂(MI 2)3
2部、熱可塑性ポリビニルアルコール(MI 10)5
0部、ポリプロピレン/ポリエーテルブロック型ポリマ
ー(MI 20)10部、メチレンビスステアリン酸ア
マイド3部としたこと以外は同様にしてシート状成形体
(厚さ1mm)を得た。この成形体について実施例1と
同様に抽出除去処理を行なった後乾燥させ、多孔質シー
ト状成形体を得、これについても実施例1と同様に測定
したところ、空隙率は59%、平均微細孔径は30μm
であった。
Example 4 In Example 3, a polypropylene resin (MI 2) 3
2 parts, thermoplastic polyvinyl alcohol (MI 10) 5
A sheet-like molded product (1 mm thick) was obtained in the same manner except that 0 part, 10 parts of a polypropylene / polyether block type polymer (MI 20), and 3 parts of methylene bisstearic acid amide were used. The molded body was subjected to the extraction and removal treatment in the same manner as in Example 1 and then dried to obtain a porous sheet-shaped molded body. The porous body was measured in the same manner as in Example 1. The pore size is 30 μm
Met.

【0014】比較例1 実施例1において、熱可塑性ポリビニルアルコールを使
用せず、メチレンビスステアリン酸アマイドを2部にし
たこと以外は同様にして中空糸状成形体を得た。この成
形体について実施例1と同様に抽出除去処理を行なった
後乾燥させた結果、水による溶出分はほぼ0であった。
Comparative Example 1 A hollow fiber-shaped molded product was obtained in the same manner as in Example 1, except that thermoplastic polyvinyl alcohol was not used and methylene bisstearic acid amide was used in two parts. The molded product was subjected to the extraction and removal treatment in the same manner as in Example 1, and then dried. As a result, the elution by water was almost zero.

【0015】比較例2 実施例1において、ポリプロピレン/ポリエースルブロ
ック型ポリマーの代わりに、ポリプロピレン/ポリスチ
レンブロック型ポリマー(ポリスチレンは疎水性ポリマ
ー)を使用したこと以外は同様にして中空糸状成形体の
成形を行なったところ、紡糸ノズルから吐出されるスト
ランドは連続して巻き取ることができず、短いものしか
得られななかった(糸径5mmφ、膜厚1mm)。この
成形体について実施例1と同様に抽出除去処理を行なっ
た後乾燥させた結果、空隙率は47%であったが、全体
に微細孔の分布が不均一であり、微細孔のない部分と微
細孔のある部分が判然と目視された。
Comparative Example 2 A hollow fiber shaped article was produced in the same manner as in Example 1 except that a polypropylene / polystyrene block type polymer (polystyrene was a hydrophobic polymer) was used instead of the polypropylene / polyester block type polymer. When the molding was performed, the strand discharged from the spinning nozzle could not be continuously wound up, and only a short strand was obtained (yarn diameter 5 mmφ, film thickness 1 mm). The molded body was subjected to extraction removal treatment in the same manner as in Example 1 and then dried. As a result, the porosity was 47%. Microporous areas were clearly visible.

【0016】比較例3 実施例1において、ポリプロピレンを69部に、熱可塑
性ポリビニルアルコールの代わりに大豆油を20部とし
た以外は同様にして中空糸状成形体の成形を行ったとこ
ろ、紡糸ノズルから吐出されるストランドは連続して巻
き取ることは全く不可能であり、且つ大豆油がノズル出
口で液状で流出した。固体部をメチルエチルケトン溶剤
中に浸漬し、大豆油を抽出除去後乾燥させた結果、空隙
率は10%であった。
Comparative Example 3 A hollow fiber molded article was molded in the same manner as in Example 1 except that polypropylene was used in 69 parts and soybean oil was used in place of thermoplastic polyvinyl alcohol in 20 parts. The discharged strand was completely impossible to wind up continuously, and soybean oil flowed out at the nozzle outlet in a liquid state. The solid portion was immersed in a methyl ethyl ketone solvent, and the soybean oil was extracted and removed, followed by drying. As a result, the porosity was 10%.

【0017】[0017]

【発明の効果】本発明によれば、ポリオレフィン樹脂に
水溶性ポリマーとこれらの相溶化剤を併用した溶融混合
物から得られた成形体より水で水溶性ポリマーを抽出除
去し、多孔質成形体を製造したので、孔径の大きい微細
孔を有することができ、フィルム、プレートや中空糸、
管状体等において厚さや太さ等の成形体形状を幅広く選
択することができる多孔質成形体を得ることができ、し
かも条件設定が簡単に行なえ、生産性がよいだけではな
く、微細孔の大きさ、数や分布が均一なポリオレフィン
系多孔質成形体の製造方法を提供することができる。
According to the present invention, a water-soluble polymer is extracted and removed with water from a molded product obtained from a molten mixture of a polyolefin resin and a water-soluble polymer in combination with a compatibilizing agent thereof. As it is manufactured, it can have fine pores with large pore size, films, plates and hollow fibers,
It is possible to obtain a porous molded body in which the shape of the molded body such as a thickness and a thickness can be widely selected in a tubular body and the like, and the conditions can be easily set, and not only the productivity is good, but also the size of the fine pores is improved. A method for producing a polyolefin-based porous molded article having a uniform number and distribution can be provided.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 ポリオレフィン樹脂(A)35〜85重
量部、水溶性ポリマー(B)10〜60重量部及び該
(A)成分と(B)成分を相溶させる相溶化剤(C)5
〜30重量部を溶融混合する溶融混合物生成工程と、該
溶融混合物を成形体に成形する成形工程と、該成形体中
の上記(B)成分を水で抽出除去する水溶性ポリマー抽
出除去工程を有する多孔質成形体の製造方法。
1. A polyolefin resin (A) in an amount of 35 to 85 parts by weight, a water-soluble polymer (B) in an amount of 10 to 60 parts by weight, and a compatibilizer (C) 5 for making the components (A) and (B) compatible with each other.
A melt mixture forming step of melt mixing up to 30 parts by weight, a forming step of forming the melt mixture into a formed body, and a water-soluble polymer extracting and removing step of extracting and removing the component (B) in the formed body with water. A method for producing a porous molded article having the same.
【請求項2】 水溶性ポリマー(B)がポリビニルアル
コール成分を含むポリマーである請求項1記載の多孔質
成形体の製造方法。
2. The method according to claim 1, wherein the water-soluble polymer (B) is a polymer containing a polyvinyl alcohol component.
【請求項3】 相溶化剤(C)がポリオレフィンとポリ
エーテルからなるブロックポリマーである請求項1又は
2に記載の多孔質成形体の製造方法。
3. The method according to claim 1, wherein the compatibilizer (C) is a block polymer comprising a polyolefin and a polyether.
JP01330597A 1997-01-09 1997-01-09 Method for producing polyolefin porous molded body Expired - Lifetime JP3658618B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP01330597A JP3658618B2 (en) 1997-01-09 1997-01-09 Method for producing polyolefin porous molded body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP01330597A JP3658618B2 (en) 1997-01-09 1997-01-09 Method for producing polyolefin porous molded body

Publications (2)

Publication Number Publication Date
JPH10195231A true JPH10195231A (en) 1998-07-28
JP3658618B2 JP3658618B2 (en) 2005-06-08

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ID=11829480

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Country Status (1)

Country Link
JP (1) JP3658618B2 (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57111333A (en) * 1980-12-29 1982-07-10 Dainippon Printing Co Ltd Porous material and preparation of same
JPH05179110A (en) * 1991-12-28 1993-07-20 Agency Of Ind Science & Technol Biodegradable thermoplastic resin molding
JPH09165464A (en) * 1995-12-13 1997-06-24 Nippon Synthetic Chem Ind Co Ltd:The Preparation of porous molded product
JP2000515903A (en) * 1996-07-12 2000-11-28 ハンツマン・ペトロケミカル・コーポレーシヨン Polyetheramine modification of polypropylene

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57111333A (en) * 1980-12-29 1982-07-10 Dainippon Printing Co Ltd Porous material and preparation of same
JPH05179110A (en) * 1991-12-28 1993-07-20 Agency Of Ind Science & Technol Biodegradable thermoplastic resin molding
JPH09165464A (en) * 1995-12-13 1997-06-24 Nippon Synthetic Chem Ind Co Ltd:The Preparation of porous molded product
JP2000515903A (en) * 1996-07-12 2000-11-28 ハンツマン・ペトロケミカル・コーポレーシヨン Polyetheramine modification of polypropylene

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