JP2004331881A - Porous molded product - Google Patents

Porous molded product Download PDF

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Publication number
JP2004331881A
JP2004331881A JP2003131892A JP2003131892A JP2004331881A JP 2004331881 A JP2004331881 A JP 2004331881A JP 2003131892 A JP2003131892 A JP 2003131892A JP 2003131892 A JP2003131892 A JP 2003131892A JP 2004331881 A JP2004331881 A JP 2004331881A
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JP
Japan
Prior art keywords
pore
porous molded
forming agent
porous
thermoplastic resin
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JP2003131892A
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Japanese (ja)
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JP4188748B2 (en
Inventor
Hisayoshi Ito
久義 伊藤
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Daicel Corp
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Daicel Chemical Industries Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for manufacturing a porous molded product with a porous structure of an unsymmetrical pattern that has a precise pore structure at the outermost surface and a rough void structure in the inside. <P>SOLUTION: The method for manufacturing the porous molded product comprises a step of melt-blending a resin composition containing a thermoplastic resin and a pore forming agent and then molding it, a step of dipping the thermoplastic resin molding into a solvent S<SB>1</SB>capable of dissolving the thermoplastic resin and swelling the molding, and a step of removing the molding from the solvent S<SB>1</SB>and then dipping the molding into a solvent S<SB>2</SB>that can not dissolve the resin but can dissolve the pore forming agent. According to the method, the porous molded product with the porous structure of the unsymmetrical pattern that has the precise pore structure at the surface and the rough void structure in the inside is obtained. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明は、固液分離膜として利用できる多孔成形体、及びその製造に適した多孔成形体の製造方法に関する。
【0002】
【従来の技術】
従来、連続通孔を有する多孔体の製造法として、湿式相転換法が採用されており、樹脂、両溶媒、貧溶媒又は製膜条件を選択することにより、最表面に緻密な孔構造を有し、内部は粗大なボイド構造を有する非対称型の多孔構造が得られることが知られている。
【0003】
しかしこの方法は、樹脂が良溶媒に溶解したドープ溶液の状態から樹脂を析出させて多孔体を形成するために、多孔体における樹脂部分の樹脂の密度が粗になってしまい、その結果得られる多孔体の機械強度が非常に弱く、脆い多孔体しか得られないという問題がある。
【0004】
一方、分離膜としての応用例は極めて少ないが、樹脂に気孔形成剤を混合し、混錬、成形後に気孔形成剤のみを溶媒等で除去することにより多孔体を得る、溶融成形/溶媒抽出法が知られている。
【0005】
特開2001−2825号公報には、気孔形成剤として加工温度で溶融状態になる多価アルコールを用い、多孔度の高い連続通孔性の多孔体を得る方法が提示されている。この方法は、一旦樹脂を溶融状態にしてから構造を形成させるために、樹脂の分子の絡み合いが十分に確保でき、また樹脂の密度も高く出来るため最終的な多孔体の機械強度は前述の湿式相転換法で得られるものと比較すると格段に高くなる。
【0006】
しかし一方では、湿式相転換法で得られる分離膜のように最表面に緻密な孔構造を有し、内部は粗大なボイド構造を有する非対称型の多孔構造を得ることは不可能であった。
【0007】
【特許文献1】特開2001−2825号公報
【0008】
【発明が解決しようとする課題】
本発明は、気孔形成剤を用いて、湿式相転換法を適用した場合と同様な多孔構造を有する成形体を得るものであり、前記した多孔構造の多孔成形体及びその製造方法を提供することを課題とするものである。
【0009】
【課題を解決するための手段】
本発明は、熱可塑性樹脂及び気孔形成剤を含有し、気孔形成剤の含有量が、気孔形成剤の当初使用量の5質量%以下である多孔成形体であり、表面から全体の厚みに対して1/10以上内側の孔の平均孔径Dと、表面の平均孔径Dが、次式(I):D>2×D (I)で示される関係を満たしている多孔成形体を提供する。
【0010】
この多孔成形体中には、下記定義により規定される残存状態の気孔形成剤が必ず存在しているものであり、この残存している気孔形成剤は、製造時に添加され、その後で除去処理されたものの一部が除去されずに残存したものである。「表面」とは、多孔成形体が平面状等の場合には外表面を意味し、管状等の場合には外表面及び内表面を意味する。
【0011】
更に本発明は、熱可塑性樹脂と気孔形成剤を含む樹脂組成物を溶融混錬し、成型加工する工程、
熱可塑性樹脂を溶解させる溶媒Sに浸漬し、熱可塑性樹脂成形体を膨潤させる工程、
熱可塑性樹脂成形体を取り出した後、熱可塑性樹脂は溶解させないが、気孔形成剤は溶解させる溶媒Sに浸漬する工程、
を具備する多孔成形体の製造方法を提供する。
【0012】
この製造方法を適用して得られた多孔成形体中には、気孔形成剤が残存していないものと、気孔形成剤が残存しているものとの両方が含まれる。気孔形成剤が残存しているか、残存していないかは、次の方法により確認することができる。即ち、得られた多孔成形体を、熱可塑性樹脂成分及び気孔形成剤の双方が溶解可能な溶媒に溶解し、H−NMRにより、気孔形成剤量を定量する。
【0013】
【発明の実施の形態】
まず、本発明の多孔成形体の製造に適した多孔成形体の製造方法を、工程ごとに説明する。なお、以下で説明する工程以外にも、当業者において通常なされる工程を付加することができる。
【0014】
第1工程において、熱可塑性樹脂と気孔形成剤を含む樹脂組成物を溶融混錬し、成型加工する。なお、次工程に移行する前に冷却工程を設けることができる。
【0015】
成形体の形状及び大きさは、最終的に得られる多孔成形体の用途等に応じて適宜決定する。
【0016】
溶融混錬方法としては、単軸又は二軸スクリュー押出機、ニーダー、カレンダーロール等の装置を用いて行うことができる。また溶融混錬に先立ち、熱可塑性樹脂を予め凍結粉砕機等で粉体状に予備加工したり、ヘンシェルミキサー、タンブルミキサー、ボールミル等で予備混錬してもよい。
【0017】
成形方法としては、射出成形、押出成形、ブロー成形、カレンダー成形等が挙げられるが、生産性や加工の容易さから、射出成形、押出成形が好ましい。また、押出成形や射出成形の過程において、又は熱融着等の付加工程の処理過程において、他の基材との積層品として成形することもできる。
【0018】
成形温度は、熱可塑性樹脂の種類、熱可塑性樹脂と気孔形成剤の混合比率、成形方法に応じて設定する。
【0019】
熱可塑性樹脂と気孔形成剤の組み合わせは、次工程以降の処理で用いる溶媒S、Sの種類に関連して決定する。
【0020】
熱可塑性樹脂は特に制限されるものではなく、ポリスチレン(PS)、耐衝撃ポリスチレン(HIPS)等のスチレン系樹脂;ポリプロピレン(PP)、ポリエチレン(PE)等のオレフィン系樹脂;ポリエチレンテレフタレート(PET)、ポリブチレンテレフタラート(PBT)等のポリエステル系樹脂;ポリカーボネート樹脂(PC)、ポリメチルメタクリレート(PMMA)、セルロースアセテート(CA)、セルロースアセテートプロピオネート(CAP)、セルロースアセテートブチレート(CAB)等のセルロース誘導体系樹脂;ポリ塩化ビニル(PVC)、ポリフッ化ビニリデン(PVDF)等のハロゲン系樹脂;エチレンビニルアルコール共重合樹脂(EVOH)、エチレン酢酸ビニル共重合樹脂(EVA)、スチレンブタジエン共重合樹脂(SB、SBS)、スチレンアクリルニトリル共重合樹脂(AS)等の共重合体樹脂が挙げられる。これらの樹脂は、単独で用いても良いし、2以上の混合物であっても良い。
【0021】
気孔形成剤は溶媒に可溶なものであれば制限されないが、特に水溶性のものが好ましく、オリゴ糖、常温固体である多価アルコール等が挙げられる。
【0022】
オリゴ糖類(又は小糖類)としては、二糖類(マルトース、イソマルトース、パラチノース、セロビオース、ラクトース、スクロース、トレハロース、ゲンチオビノース、コージービオース、ラミナリビオース、メリビオース、ニゲロース、ソホロース等)、三糖類(マルトトリオース、メレチトース、ラフィノース等)、四糖類(スタキオース、セロテトラオース等)、五糖類や六糖類等が好ましい。オリゴ糖は還元型であっても非還元型であっても良いが、熱を加えることを考慮すると、還元型のほうがより好ましい。多価アルコールとしては、常温固体でかつ溶融時に急激な粘度低下を引き起こさないものが望ましく、その観点からペンタエリスリトールが好ましい。これらの気孔形成剤は、単独でも、2以上の混合物であっても良い。なお、気孔形成剤の粘度調整等の目的で、他の水溶性多価アルコールや水溶性単糖類を添加しても良い。
【0023】
気孔形成剤の添加量は、多孔成形体の機械的強度、多孔成形体を分離膜として適用した場合の分離能力、処理時間等に応じて調整することができる。気孔形成剤の添加量は、熱可塑性樹脂と気孔形成剤の合計量中、気孔形成剤の含有量が、好ましくは40〜90質量%、より好ましくは50〜80質量%、更に好ましくは60〜75質量%となる量である。
【0024】
また、熱可塑性樹脂及び気孔形成剤の他にも、多孔成形体の機械的強度、加工性を改善する目的、粘度特性を改良する目的で、他の添加剤を添加しても良い。更に必要に応じて、熱安定剤、滑剤、紫外線吸収剤、増粘剤、難燃剤、酸化防止剤、帯電防止剤、ファイバー等の強化剤を含有していても良い。このような添加剤は、熱可塑性樹脂100質量部に対して、30質量部以下であることが好ましい。
【0025】
次に第2工程において、熱可塑性樹脂を溶解させる溶媒Sに浸漬し、熱可塑性樹脂成形体を膨潤させる。この工程の処理により、成形体の表面を膨潤させることで、次工程の処理において気孔形成剤が除去されやすくなる。
【0026】
溶媒Sは有機溶媒が好ましい。溶媒Sへの浸漬時間は、好ましくは1〜300秒、より好ましくは10〜180秒である。溶媒に浸漬する時間が1秒以上であると十分な膨潤状態を作り出すことができ、300秒以下であると熱可塑性樹脂が溶媒中に溶解拡散してしまう。
【0027】
次に第3工程において、熱可塑性樹脂成形体を取り出した後、熱可塑性樹脂は溶解させないが、気孔形成剤は溶解させる溶媒Sに浸漬する。
【0028】
第2工程の処理により、成形体の外表面は膨潤した状態になっており、第3工程の処理により、外表面では熱可塑性樹脂が相転換を起こして微細な孔構造を形成し、同時に気孔形成剤の溶媒Sへの溶出に伴い、成形体内部では粗大な孔構造の形成が行われる。
【0029】
溶媒Sは水が好ましく、50〜90℃の温水がより好ましい。溶媒Sへの浸漬時間は、成形体に含有されている気孔形成剤の95質量%以上が除去されるに十分な時間であることが好ましい。
【0030】
本発明の製造方法を適用することにより、気孔形成剤を含有しない成形体と、気孔形成剤を含有する多孔成形体が得られる。多孔成形体が気孔形成剤を含有するとき、気孔形成剤の残存量が、気孔形成剤の当初使用量(第1工程における使用量)の5質量%以下の量である。
【0031】
本発明の製造方法を適用して得られた多孔成形体は、湿式相転換法により得られる多孔体と同様に内部に粗大な孔構造、表面に緻密な孔構造を持つ複合型の孔構造を有する。
【0032】
本発明の多孔成形体は、表面から全体の厚みに対して1/10以上内側の孔の平均孔径Dと、表面の平均孔径Dが、次式(I):D>2×D (I)で示される関係を満たしている。多孔成形体を固液分離用の分離膜として適用した場合、前記式(I)を満たすことで、分離性能(例えば、分画分子量)と膜全体の液体透過性能(例えば、透水速度)をバランス良く具備させることができる。
【0033】
多孔成形体を浄水用の分離膜として利用する場合を考慮すると、上記式中のDは、クリプトスポリジウム(原虫)の分離に十分とされる2μm以下であることが好ましい。
【0034】
本発明の多孔成形体は、空孔率が好ましくは40〜90%、より好ましくは50〜80%、更に好ましくは60〜75%である。
【0035】
本発明の多孔成形体は、空孔率がP%である多孔成形体の引張速度50mm/分のときの引張破断点強度S(JIS K7113準拠のプラスチック成形品の引張試験)が、S>40×(100−P)/100(MPa)(40MPaは、引張速度50mm/分のときの一般的な熱可塑性樹脂の単体での成形品の引張破断点強度を示す。)を満たすことが好ましい。
【0036】
湿式相転換法で得られる多孔体は、熱可塑性樹脂溶液から作製されるため、多孔体内の熱可塑性樹脂の凝集力が弱く、多孔体の機械強度を低下させる。一方、本発明の製造方法を適用して得られた多孔成形体は、溶融混錬工程を含んでいるため、熱可塑性樹脂の分子間の絡み合いが十分に確保されているので、多孔成形体の機械強度の低下がない。
【0037】
本発明の多孔成形体は、平膜、中空糸膜等の様々な形態の膜にすることができる。
【0038】
本発明の多孔成形体は、固液分離用膜として、浄水の膜浄化、工業排水、下水等の浄化処理等の用途に適用できる。
【0039】
【実施例】
以下、実施例により本発明をさらに詳しく説明するが、本発明はこれらにより限定されるものではない。以下で用いた各成分の詳細は次のとおりである。
【0040】
樹脂−1:エチレンビニルアルコール共重合樹脂(クラレ社製のEP−L101B、エチレン含量19.8質量%)
樹脂−2:ポリスチレン樹脂(東洋スチレン社製のHRM63C)
樹脂−3:セルロースアセテートブチレート樹脂(イーストマン製 CAB171−15S)
気孔形成剤−1:オリゴ糖(PO−10,東和化成製)
気孔形成剤−2:ペンタエリスリトール(和光純薬製)
溶媒−1:ジメチルスルホオキシドDMSO(和光純薬製)
溶媒−2:テトラヒドロフラン(和光純薬製)。
【0041】
実施例1〜4、比較例1
(第1工程)
表1に示す組成(質量%表示)の各成分からなる樹脂組成物を、ブラベンダー(東洋精機製ラボプラストミル)により設定温度200℃で5分間溶融混錬した。その後、一旦室温まで冷却した後、プレス機にて200℃、20MPa、3分間の条件で、厚さ1mmの板状に成形した。
【0042】
(第2工程)
プレスした成形品を速やかに30℃、20MPa、3分間の条件で冷却した後、表1の時間、溶媒(S)に浸漬した。
【0043】
(第3工程)
その後、速やかに60℃の温水(溶媒S)中に浸漬し、仕込んだ気孔形成剤質量の95%相当の質量減少が確認できるまでそのまま放置し、多孔成形体を得た。
【0044】
実施例1で得られた多孔成形体の外表面及び内部の孔構造(表面から100μmの部分)の走査型電子顕微鏡写真を図1(外表面;4000倍)及び図2(内部構造;500倍)に示し、比較例1で得られた多孔体の外表面の電子顕微鏡写真(2000倍)を図3に示す。表1中の各測定値の測定方法は次のとおりである。
【0045】
(1)多孔成形体の孔径、内部の孔径Dの測定
走査型電子顕微鏡(SEM:日本電子製)を用い、多孔成形体の断面の孔構造を確認した。多孔成形体の孔に連続性がある場合は、独立した孔が存在しない(図1参照)。そこで、100−10,000倍で撮影された多孔体断面の写真から、一つの孔を形成する向かい合わせの樹脂相間の距離が最低になるときの値を孔径とし(例えば、孔が楕円形であるとすると、短径の長さが孔径となる)、厚さ1mmの多孔成形体の外表面より100μm以上内側の断面から100箇所を無作為に抽出して孔径測定を行い、平均孔径として表示した。
【0046】
(2)多孔体の孔径、外表面の孔径Dの測定
孔径Dの測定と同様にして測定した。なお、多孔体表面の孔構造が独立した孔からなる場合には、それぞれの孔の面積を円換算し、このときの計算された直径を孔径とした。100箇所の孔を無作為に抽出して孔径測定を行い、平均孔径として表示した。
【0047】
(3)多孔成形体の機械強度
多孔成形体をJIS K7113準拠の2号ダンベルのサイズに打ち抜き、引張速度50mm/分の引張速度でテンシロンRTA520(東洋精機製)を用いて引張試験を実施し、引張破断点強度を得た。
【0048】
(4)多孔成形体の空孔率の測定
多孔成形体を25℃の純水中に浸漬し、多孔成形体内部からの気泡の発生が認められなくなるまで減圧状態に保った。その後、多孔成形体の重量を測定し、湿潤重量Mを得た。次に多孔成形体を絶乾状態まで乾燥した後に重量を測定し、乾燥重量Mを得た。これらの測定値と水の比重ρ、多孔体の原料となった熱可塑性樹脂の比重ρより、以下の式を用いて空孔率Pを算出した。
【0049】
P=100×{[(M−M)/ρ]/[(M−M)/ρ+M/ρ]}
比較例2〜4
表1に示す組成(重量%表示)の各成分からなる樹脂組成物を用い、第2工程の処理をしない他は実施例1〜4、比較例1と同様にして、多孔成形体を得た。
【0050】
比較例5、6
表1に示す組成、温度で熱可塑性樹脂を溶媒(ジメチルスルホキシド)に溶解し、原料ドープを得た。原料ドープを室温に保ったガラス板上に厚さ1mmとなるようにキャストし、1分間放置した後、ガラス板ごと25℃の純水中に浸漬して多孔体を得た。
【0051】
【表1】

Figure 2004331881
【0052】
実施例1〜4では、外表面の孔径(D)、内部の孔径(D)、機械強度において申し分ない性能を有する多孔成形体が得られた。
【0053】
比較例1は、溶媒への浸漬時間が長すぎたため、熱可塑性樹脂が溶媒中に溶解、拡散してしまい、結果として多孔成形体の外観、形状を損なってしまった。また、多孔成形体表面に繊維状の熱可塑性樹脂が付着した状態となり、その後の利用は不可能と判断した。
【0054】
比較例2〜4の多孔成形体は、機械強度は良好なものの、全体が均一孔を有するスポンジ構造となり、最表面に緻密な孔構造を形成させることができなかった。
【0055】
比較例5、6の多孔体は、湿式相転換法で作成された多孔体であるため、機械強度が非常に小さかった。
【0056】
【発明の効果】
本発明の製造方法によれば、表面に緻密な孔構造を有し、内部は粗大なボイド構造を有する非対称型の多孔構造を有する多孔成形体を得ることができる。
【図面の簡単な説明】
【図1】実施例1で得られた多孔体の最表面の電子顕微鏡写真(4000倍)。
【図2】実施例1で得られた多孔体の内部構造の電子顕微鏡写真(500倍)。
【図3】比較例1で得られた多孔体の最表面の電子顕微鏡写真(2000倍)。[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a porous molded body that can be used as a solid-liquid separation membrane, and a method for producing a porous molded body suitable for producing the same.
[0002]
[Prior art]
Conventionally, a wet phase inversion method has been employed as a method for producing a porous body having continuous pores, and a dense pore structure is formed on the outermost surface by selecting a resin, both solvents, a poor solvent, or film forming conditions. However, it is known that an asymmetric type porous structure having a coarse void structure inside can be obtained.
[0003]
However, in this method, since the resin is precipitated from the state of the dope solution in which the resin is dissolved in the good solvent to form the porous body, the density of the resin in the resin portion in the porous body becomes coarse, and the resulting result is obtained. There is a problem that the mechanical strength of the porous body is very weak, and only a brittle porous body can be obtained.
[0004]
On the other hand, although there are very few applications as a separation membrane, a porous material is obtained by mixing a resin with a pore-forming agent, kneading and molding, and removing only the pore-forming agent with a solvent or the like to obtain a porous body. It has been known.
[0005]
Japanese Patent Application Laid-Open No. 2001-2825 discloses a method of using a polyhydric alcohol which becomes a molten state at a processing temperature as a pore-forming agent to obtain a highly porous continuous porous material. In this method, since the structure is formed after the resin is once in a molten state, the entanglement of the resin molecules can be sufficiently secured, and the density of the resin can be increased. It is much higher than that obtained by the phase inversion method.
[0006]
On the other hand, however, it was not possible to obtain an asymmetric porous structure having a dense pore structure on the outermost surface and a coarse void structure inside as in a separation membrane obtained by a wet phase inversion method.
[0007]
[Patent Document 1] Japanese Patent Application Laid-Open No. 2001-2825
[Problems to be solved by the invention]
The present invention provides a molded article having the same porous structure as that obtained by applying the wet phase inversion method using a pore-forming agent, and provides a porous molded article having the above-described porous structure and a method for producing the same. Is the subject.
[0009]
[Means for Solving the Problems]
The present invention is a porous molded article containing a thermoplastic resin and a pore-forming agent, wherein the content of the pore-forming agent is 5% by mass or less of the initially used amount of the pore-forming agent. The porous molded body having an average pore diameter D 1 of 1/10 or more inside and an average pore diameter D 2 of the surface satisfying a relationship represented by the following formula (I): D 1 > 2 × D 2 (I) I will provide a.
[0010]
In this porous molded body, a pore-forming agent in a residual state defined by the following definition is always present, and the remaining pore-forming agent is added at the time of production and then removed. Part of the material that remains without being removed. "Surface" means an outer surface when the porous molded body is planar or the like, and means an outer surface and an inner surface when the porous molded body is tubular or the like.
[0011]
Further, the present invention is a step of melt-kneading a resin composition containing a thermoplastic resin and a pore-forming agent, and molding and processing.
Process was immersed in a solvent S 1 for dissolving the thermoplastic resin to swell the thermoplastic resin molded article,
After removal of the thermoplastic resin molded article, the process thermoplastic resin is not dissolved, the pore forming agent is immersed in a solvent S 2 to be dissolved,
The present invention provides a method for producing a porous molded body comprising:
[0012]
The porous compact obtained by applying this production method includes both a porous molded body in which no pore forming agent remains and a porous molded body in which the pore forming agent remains. Whether or not the pore forming agent remains or not can be confirmed by the following method. That is, the obtained porous molded body is dissolved in a solvent in which both the thermoplastic resin component and the pore forming agent are soluble, and the amount of the pore forming agent is quantified by 1 H-NMR.
[0013]
BEST MODE FOR CARRYING OUT THE INVENTION
First, a method for producing a porous molded article suitable for producing the porous molded article of the present invention will be described step by step. In addition to the steps described below, steps commonly performed by those skilled in the art can be added.
[0014]
In the first step, a resin composition containing a thermoplastic resin and a pore-forming agent is melt-kneaded and molded. Note that a cooling step can be provided before moving to the next step.
[0015]
The shape and size of the molded article are appropriately determined according to the use of the finally obtained porous molded article and the like.
[0016]
The melt-kneading method can be performed using a single-screw or twin-screw extruder, a kneader, a calender roll, or another device. Prior to melt kneading, the thermoplastic resin may be preliminarily processed into a powdery state by a freeze grinder or the like, or may be preliminarily kneaded by a Henschel mixer, a tumble mixer, a ball mill, or the like.
[0017]
Examples of the molding method include injection molding, extrusion molding, blow molding, calender molding, and the like. Injection molding and extrusion molding are preferred from the viewpoint of productivity and ease of processing. Also, in the process of extrusion molding or injection molding, or in the process of an additional step such as heat fusion, it can be molded as a laminate with another substrate.
[0018]
The molding temperature is set according to the type of the thermoplastic resin, the mixing ratio of the thermoplastic resin and the pore-forming agent, and the molding method.
[0019]
The combination of the thermoplastic resin and the pore-forming agent is determined in relation to the types of the solvents S 1 and S 2 used in the subsequent processes.
[0020]
The thermoplastic resin is not particularly limited, and styrene resins such as polystyrene (PS) and high-impact polystyrene (HIPS); olefin resins such as polypropylene (PP) and polyethylene (PE); polyethylene terephthalate (PET); Polyester resins such as polybutylene terephthalate (PBT); polycarbonate resins (PC), polymethyl methacrylate (PMMA), cellulose acetate (CA), cellulose acetate propionate (CAP), cellulose acetate butyrate (CAB), etc. Cellulose derivative resins; halogen resins such as polyvinyl chloride (PVC) and polyvinylidene fluoride (PVDF); ethylene vinyl alcohol copolymer resin (EVOH), ethylene vinyl acetate copolymer resin (EVA), styrene resin Diene copolymer resin (SB, SBS), include copolymer resins, styrene-acrylonitrile copolymer resin (AS). These resins may be used alone or as a mixture of two or more.
[0021]
The pore-forming agent is not limited as long as it is soluble in a solvent, but is preferably a water-soluble one, and examples thereof include oligosaccharides and polyhydric alcohols that are solid at room temperature.
[0022]
Oligosaccharides (or small sugars) include disaccharides (maltose, isomaltose, palatinose, cellobiose, lactose, sucrose, trehalose, gentibinose, cozybiose, laminaribiose, melibiose, nigerose, sophorose, etc.), and trisaccharides (Maltotriose, meletitose, raffinose, etc.), tetrasaccharides (stachyose, cellotetraose, etc.), pentasaccharides, hexasaccharides, etc. are preferred. The oligosaccharide may be in a reduced form or a non-reduced form, but the reduced form is more preferable in consideration of applying heat. As the polyhydric alcohol, those which are solid at room temperature and do not cause a sharp decrease in viscosity upon melting are desirable, and pentaerythritol is preferred from that viewpoint. These pore-forming agents may be used alone or in a mixture of two or more. In addition, other water-soluble polyhydric alcohols or water-soluble monosaccharides may be added for the purpose of adjusting the viscosity of the pore-forming agent.
[0023]
The amount of the pore-forming agent to be added can be adjusted according to the mechanical strength of the porous molded body, the separation ability when the porous molded body is applied as a separation membrane, the processing time, and the like. Regarding the amount of the pore-forming agent added, the content of the pore-forming agent is preferably 40 to 90% by mass, more preferably 50 to 80% by mass, and still more preferably 60 to 90% by mass of the total amount of the thermoplastic resin and the pore forming agent. The amount is 75% by mass.
[0024]
Further, in addition to the thermoplastic resin and the pore-forming agent, other additives may be added for the purpose of improving the mechanical strength and processability of the porous molded body, and for improving the viscosity characteristics. Further, if necessary, a heat stabilizer, a lubricant, an ultraviolet absorber, a thickener, a flame retardant, an antioxidant, an antistatic agent, and a reinforcing agent such as fiber may be contained. Such additives are preferably used in an amount of 30 parts by mass or less based on 100 parts by mass of the thermoplastic resin.
[0025]
Next, in the second step, was immersed in a solvent S 1 for dissolving the thermoplastic resin to swell the thermoplastic resin molded article. By swelling the surface of the molded body by the treatment in this step, the pore-forming agent is easily removed in the treatment in the next step.
[0026]
The solvent S 1 is an organic solvent. The immersion time in the solvent S1 is preferably 1 to 300 seconds, more preferably 10 to 180 seconds. If the immersion time in the solvent is 1 second or more, a sufficient swelling state can be created, and if it is 300 seconds or less, the thermoplastic resin dissolves and diffuses in the solvent.
[0027]
Then in the third step, after removal of the thermoplastic resin molded article, the thermoplastic resin is not dissolved, the pore forming agent is immersed in the solvent S 2 to dissolve.
[0028]
By the treatment in the second step, the outer surface of the molded body is in a swollen state, and by the treatment in the third step, the thermoplastic resin undergoes phase transformation on the outer surface to form a fine pore structure, and at the same time, pores are formed. with the dissolution of the former to the solvent S 2, the formation of coarse pore structure is performed inside the formed body.
[0029]
Solvent S 2 is preferably water, more preferably hot water at 50 to 90 ° C.. Time of immersion in the solvent S 2 is preferably more than 95 wt% of pore-forming agent contained in the molded body is a sufficient time to be removed.
[0030]
By applying the production method of the present invention, a molded article containing no pore-forming agent and a porous molded article containing the pore-forming agent can be obtained. When the porous molded article contains a pore-forming agent, the residual amount of the pore-forming agent is 5% by mass or less of the initially used amount of the pore-forming agent (the amount used in the first step).
[0031]
The porous compact obtained by applying the production method of the present invention has a composite pore structure having a coarse pore structure inside and a dense pore structure on the surface similarly to the porous body obtained by the wet phase inversion method. Have.
[0032]
Porous molded article of the present invention, the inner and the average pore diameter D 1 of the hole 1/10 or more to the total thickness from the surface, the average pore diameter D 2 of the surface, the following equation (I): D 1> 2 × D 2 The relationship shown in (I) is satisfied. When the porous molded body is applied as a separation membrane for solid-liquid separation, by satisfying the above formula (I), the separation performance (for example, the molecular weight cut off) and the liquid permeation performance (for example, water permeation rate) of the whole membrane are balanced. Can be well equipped.
[0033]
Considering the case of using the porous shaped body as a separation membrane for water purification, D 2 in the above formula is preferably not more than 2μm, which is sufficient for the separation of cryptosporidium (protozoa).
[0034]
The porosity of the porous molded article of the present invention is preferably 40 to 90%, more preferably 50 to 80%, and still more preferably 60 to 75%.
[0035]
The porous molded product of the present invention has a tensile strength at break S (tensile test of a plastic molded product in accordance with JIS K7113) at a tensile speed of 50 mm / min of a porous molded product having a porosity of P%, where S> 40. X (100-P) / 100 (MPa) (40 MPa indicates a tensile strength at break of a molded article of a single thermoplastic resin alone at a tensile speed of 50 mm / min).
[0036]
Since the porous body obtained by the wet phase inversion method is made from a thermoplastic resin solution, the cohesive force of the thermoplastic resin in the porous body is weak, and the mechanical strength of the porous body is reduced. On the other hand, since the porous molded body obtained by applying the production method of the present invention includes a melt-kneading step, the entanglement between the molecules of the thermoplastic resin is sufficiently ensured. There is no decrease in mechanical strength.
[0037]
The porous molded article of the present invention can be formed into various types of membranes such as a flat membrane and a hollow fiber membrane.
[0038]
INDUSTRIAL APPLICABILITY The porous molded body of the present invention can be used as a membrane for solid-liquid separation, such as membrane purification of purified water, purification of industrial wastewater, sewage, and the like.
[0039]
【Example】
Hereinafter, the present invention will be described in more detail by way of examples, but the present invention is not limited thereto. The details of each component used below are as follows.
[0040]
Resin-1: Ethylene vinyl alcohol copolymer resin (EP-L101B manufactured by Kuraray Co., Ltd., ethylene content 19.8% by mass)
Resin-2: Polystyrene resin (HRM63C manufactured by Toyo Styrene Co.)
Resin-3: Cellulose acetate butyrate resin (CAB171-15S manufactured by Eastman)
Pore forming agent-1: oligosaccharide (PO-10, manufactured by Towa Kasei)
Pore forming agent-2: pentaerythritol (manufactured by Wako Pure Chemical Industries)
Solvent-1: dimethyl sulfoxide DMSO (manufactured by Wako Pure Chemical Industries)
Solvent-2: tetrahydrofuran (manufactured by Wako Pure Chemical Industries).
[0041]
Examples 1-4, Comparative Example 1
(First step)
The resin composition composed of each component having the composition shown in Table 1 (indicated by mass%) was melt-kneaded at a set temperature of 200 ° C. for 5 minutes by Brabender (Labo Plastmill manufactured by Toyo Seiki). Then, after cooling to room temperature once, it was formed into a plate having a thickness of 1 mm under the conditions of 200 ° C., 20 MPa, and 3 minutes using a press machine.
[0042]
(2nd process)
The pressed molded product was immediately cooled at 30 ° C. and 20 MPa for 3 minutes, and then immersed in the solvent (S 1 ) for the time shown in Table 1.
[0043]
(3rd step)
Then, it was immediately immersed in hot water (solvent S 2 ) at 60 ° C. and left as it was until a mass reduction of 95% of the charged pore forming agent was confirmed, to obtain a porous molded body.
[0044]
Scanning electron micrographs of the outer surface and the inner pore structure (portion 100 μm from the surface) of the porous molded body obtained in Example 1 are shown in FIGS. 1 (outer surface; 4000 times) and 2 (inner structure; 500 times). FIG. 3 shows an electron micrograph (× 2000) of the outer surface of the porous body obtained in Comparative Example 1. The measuring method of each measured value in Table 1 is as follows.
[0045]
(1) The pore size of the porous molded body, the interior of the pore diameter D 1 of the measuring scanning electron microscope: using (SEM manufactured by JEOL) to confirm the cross-section of the pore structure of the porous molded body. When the pores of the porous molded body have continuity, there are no independent pores (see FIG. 1). Thus, from a photograph of a cross section of a porous body taken at a magnification of 100 to 10,000, the value at which the distance between the resin phases facing each other that forms one hole is defined as the hole diameter (for example, when the hole has an elliptical shape). If there is, the length of the minor axis is the pore diameter), 100 points are randomly extracted from the cross section of 100 μm or more inside the outer surface of the porous molded body having a thickness of 1 mm, the pore diameter is measured, and displayed as the average pore diameter. did.
[0046]
(2) porous body having a pore size, in the same manner as in the measurement of the measuring hole diameter D 1 of the hole diameter D 2 of the outer surface was measured. When the pore structure on the surface of the porous body was composed of independent pores, the area of each pore was converted to a circle, and the diameter calculated at this time was defined as the pore diameter. 100 holes were randomly sampled and the hole diameter was measured and displayed as the average hole diameter.
[0047]
(3) Mechanical strength of the porous molded body The porous molded body was punched into a size of No. 2 dumbbell according to JIS K7113, and a tensile test was performed using a Tensilon RTA520 (manufactured by Toyo Seiki) at a tensile speed of 50 mm / min. The tensile strength at break was obtained.
[0048]
(4) Measurement of Porosity of Porous Molded Body The porous molded body was immersed in pure water at 25 ° C. and kept under reduced pressure until generation of air bubbles from inside the porous molded body was no longer observed. Thereafter, the weight of the porous molded body was measured to obtain a wet weight M 1. Then weighed after drying the porous shaped body to absolute dry state to obtain a dry weight M 2. From these measured values, the specific gravity ρ 1 of water, and the specific gravity ρ 2 of the thermoplastic resin used as the raw material of the porous body, the porosity P was calculated using the following equation.
[0049]
P = 100 × {[(M 1 −M 2 ) / ρ 1 ] / [(M 1 −M 2 ) / ρ 1 + M 2 / ρ 2 ]}
Comparative Examples 2 to 4
A porous molded body was obtained in the same manner as in Examples 1 to 4 and Comparative Example 1 except that a resin composition having the components shown in Table 1 (indicated by weight%) was used, and the treatment in the second step was not performed. .
[0050]
Comparative Examples 5 and 6
The thermoplastic resin was dissolved in a solvent (dimethyl sulfoxide) at the composition and temperature shown in Table 1 to obtain a raw material dope. The raw material dope was cast to a thickness of 1 mm on a glass plate kept at room temperature, left for 1 minute, and then immersed together with the glass plate in pure water at 25 ° C to obtain a porous body.
[0051]
[Table 1]
Figure 2004331881
[0052]
In Examples 1-4, the diameter of the outer surface (D 2), the interior of the pore diameter (D 1), a porous molded article having a satisfactory performance in mechanical strength is obtained.
[0053]
In Comparative Example 1, since the immersion time in the solvent was too long, the thermoplastic resin was dissolved and diffused in the solvent, and as a result, the appearance and shape of the porous molded article were impaired. In addition, a fibrous thermoplastic resin was attached to the surface of the porous molded body, and it was determined that subsequent use was impossible.
[0054]
Although the porous molded bodies of Comparative Examples 2 to 4 had good mechanical strength, the whole had a sponge structure having uniform pores, and a dense pore structure could not be formed on the outermost surface.
[0055]
Since the porous bodies of Comparative Examples 5 and 6 were formed by the wet phase inversion method, the mechanical strength was very low.
[0056]
【The invention's effect】
According to the production method of the present invention, it is possible to obtain a porous molded body having an asymmetric porous structure having a dense pore structure on the surface and a coarse void structure inside.
[Brief description of the drawings]
FIG. 1 is an electron micrograph (× 4000) of the outermost surface of a porous body obtained in Example 1.
FIG. 2 is an electron micrograph (× 500) of the internal structure of the porous body obtained in Example 1.
FIG. 3 is an electron micrograph (× 2000) of the outermost surface of the porous body obtained in Comparative Example 1.

Claims (10)

熱可塑性樹脂及び気孔形成剤を含有し、気孔形成剤の含有量が、気孔形成剤の使用量の5質量%以下である多孔成形体であり、表面から全体の厚みに対して1/10以上内側の孔の平均孔径Dと、表面の平均孔径Dが、次式(I):D>2×D (I)で示される関係を満たしている多孔成形体。A porous molded article containing a thermoplastic resin and a pore-forming agent, wherein the content of the pore-forming agent is 5% by mass or less of the used amount of the pore-forming agent, and is 1/10 or more of the total thickness from the surface. and the average pore diameter D 1 of the inner hole, the average pore diameter D 2 of the surface, the following equation (I): D 1> 2 × D porous molded bodies meet the relationship represented by 2 (I). が2μm以下である請求項1記載の多孔成形体。Porous molded body according to claim 1, wherein D 2 is 2μm or less. 空孔率が40〜90%である請求項1又は2記載の多孔成形体。The porous molded article according to claim 1 or 2, wherein the porosity is 40 to 90%. 空孔率がP%である多孔成形体の引張速度50mm/分のときの引張破断点強度S(JIS K7113準拠のプラスチック成形品の引張試験)が、S>40×(100−P)/100(MPa)を満たす請求項1〜3のいずれか1記載の多孔成形体。The tensile strength at break (S: tensile test of a plastic molded article in accordance with JIS K7113) at a tensile speed of 50 mm / min of a porous molded article having a porosity of P% is S> 40 × (100−P) / 100. The porous molded product according to any one of claims 1 to 3, which satisfies (MPa). 固液分離用の平膜として使用する請求項1〜4のいずれか1記載の多孔成形体。The porous molded article according to any one of claims 1 to 4, which is used as a flat membrane for solid-liquid separation. 熱可塑性樹脂と気孔形成剤を含む樹脂組成物を溶融混錬し、成型加工する工程、
熱可塑性樹脂を溶解させる溶媒Sに浸漬し、熱可塑性樹脂成形体を膨潤させる工程、
熱可塑性樹脂成形体を取り出した後、熱可塑性樹脂は溶解させないが、気孔形成剤は溶解させる溶媒Sに浸漬する工程、
を具備する多孔成形体の製造方法。
Melt-kneading a resin composition containing a thermoplastic resin and a pore-forming agent, a step of molding,
Process was immersed in a solvent S 1 for dissolving the thermoplastic resin to swell the thermoplastic resin molded article,
After removal of the thermoplastic resin molded article, the process thermoplastic resin is not dissolved, the pore forming agent is immersed in a solvent S 2 to be dissolved,
A method for producing a porous molded body comprising:
が有機溶媒、Sが水である請求項6記載の多孔成形体の製造方法。S 1 is an organic solvent, the production method of the porous molded body according to claim 6, wherein S 2 is water. 気孔形成剤が、常温固体の多価アルコール及び糖類から選ばれる1又は2以上のものである請求項6又は7記載の多孔成形体の製造方法。The method for producing a porous molded article according to claim 6 or 7, wherein the pore-forming agent is one or more selected from polyhydric alcohols and saccharides which are solid at room temperature. 気孔形成剤の添加量が、熱可塑性樹脂と気孔形成剤の合計量中、40〜90質量%となる量である請求項6〜8のいずれか1記載の多孔成形体の製造方法。The method for producing a porous molded article according to any one of claims 6 to 8, wherein the amount of the pore forming agent is 40 to 90% by mass based on the total amount of the thermoplastic resin and the pore forming agent. 溶媒Sに浸漬する工程において、多孔成形体に含有されている気孔形成剤の95質量%以上を除去する請求項6〜9のいずれか1記載の多孔成形体の製造方法。In the step of immersion in a solvent S 2, a manufacturing method of the porous molded body according to any one of claims 6-9 to remove more than 95% by weight of the pore former contained in the porous shaped body.
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KR101319912B1 (en) * 2005-08-04 2013-10-18 도레이 배터리 세퍼레이터 필름 주식회사 Polyethylene microporous membrane, process for production thereof, and battery separator
WO2009041353A1 (en) * 2007-09-25 2009-04-02 Fujifilm Corporation Process for producing porous film and porous film
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