JP7331453B2 - Method for manufacturing porous body - Google Patents

Method for manufacturing porous body Download PDF

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JP7331453B2
JP7331453B2 JP2019093762A JP2019093762A JP7331453B2 JP 7331453 B2 JP7331453 B2 JP 7331453B2 JP 2019093762 A JP2019093762 A JP 2019093762A JP 2019093762 A JP2019093762 A JP 2019093762A JP 7331453 B2 JP7331453 B2 JP 7331453B2
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urethane resin
polyol
porous body
producing
molecular weight
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JP2020186352A (en
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章恵 藤下
亮 前田
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DIC Corp
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Priority to CN202010278671.XA priority patent/CN112029136A/en
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    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/28Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof by elimination of a liquid phase from a macromolecular composition or article, e.g. drying of coagulum
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    • C09D175/00Coating compositions based on polyureas or polyurethanes; Coating compositions based on derivatives of such polymers
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    • C09D7/00Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
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    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/30Low-molecular-weight compounds
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    • C08G18/4236Polycondensates having carboxylic or carbonic ester groups in the main chain containing only aliphatic groups
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    • C08J2201/00Foams characterised by the foaming process
    • C08J2201/04Foams characterised by the foaming process characterised by the elimination of a liquid or solid component, e.g. precipitation, leaching out, evaporation
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    • C08J2475/04Polyurethanes
    • C08J2475/06Polyurethanes from polyesters

Description

本発明は、湿式製膜法による多孔体の製造方法に関する。 TECHNICAL FIELD The present invention relates to a method for producing a porous body by a wet film-forming method.

液晶ガラス、ハードディスクガラス、シリコンウエハ、半導体などの高度な表面平坦性が要求される分野においては、ウレタン樹脂組成物を使用した研磨パッドが広く利用されている。中でも、最終の仕上げ研磨においては、DMF(ジメチルホルムアミド)等の溶剤で希釈したウレタン樹脂を水中で凝固させる湿式成膜法によって加工された軟質な多孔体が使用されている(例えば、特許文献1を参照。)。 Polishing pads using urethane resin compositions are widely used in fields requiring a high degree of surface flatness, such as liquid crystal glass, hard disk glass, silicon wafers, and semiconductors. Among them, in the final polishing, a soft porous body processed by a wet film forming method in which urethane resin diluted with a solvent such as DMF (dimethylformamide) is solidified in water is used (for example, Patent Document 1 ).

この多孔体による研磨パッドに対して要求される特性としては、例えば、加工体表面の平坦性を保持するための高い体積弾性率を持つこと(=低圧縮率)、表面のスクラッチを抑制する材料としての柔軟性、及び、スラリー(研磨液)の保持と安定的な研磨を担う多孔セルの微細さと均一性(湿式成膜性)等が挙げられる。 The properties required for this porous polishing pad include, for example, a high bulk modulus (=low compressibility) to maintain the flatness of the surface of the workpiece, and a material that suppresses scratches on the surface. and the fineness and uniformity (wet film-forming property) of porous cells responsible for holding slurry (polishing liquid) and stable polishing.

これらの要求特性を満たす要因の1つとしては、研磨パッドにおける多孔セルの均一性や細さが挙げられる。しかしながら、そのような研磨パッドを得ることは簡単なことではなかった。 One factor that satisfies these required properties is the uniformity and fineness of the porous cells in the polishing pad. However, obtaining such a polishing pad was not an easy task.

特開2004-256738号公報JP-A-2004-256738

本発明が解決しようとする課題は、湿式成膜法により、細かく均一なセルを有する多孔体を製造する方法を提供することにある。 The problem to be solved by the present invention is to provide a method for producing a porous body having fine and uniform cells by a wet film-forming method.

本発明は、ウレタン樹脂(A)、溶剤(B)、及び、成膜助剤(C)を含有するウレタン樹脂組成物を湿式成膜して多孔体を製造する方法であって、前記成膜助剤(C)が、ポリオキシプロピレン構造を有し、1分子あたりの平均水酸基数が2を超えて4以下のポリオール(c1)であることを特徴とする多孔体の製造方法を提供するものである。 The present invention provides a method for producing a porous body by wet film-forming of a urethane resin composition containing a urethane resin (A), a solvent (B), and a film-forming aid (C), wherein the film-forming A method for producing a porous body, wherein the auxiliary agent (C) is a polyol (c1) having a polyoxypropylene structure and having an average number of hydroxyl groups of more than 2 and not more than 4 per molecule. is.

本発明によれば、特定の成膜助剤を用いることで、湿式成膜法により、細かく均一な多孔体を製造することができる。よって、本発明は、研磨パッド、人工皮革・合成皮革の製造に特に好適に使用することができる。 According to the present invention, a fine and uniform porous body can be produced by a wet film-forming method by using a specific film-forming aid. Therefore, the present invention can be used particularly preferably for manufacturing polishing pads, artificial leathers and synthetic leathers.

なお、本発明において前記「多孔体」とは、ウレタン樹脂組成物を湿式成膜法により凝固させれば自ずと得られる程度の多数の孔を有するものであり、例えば、面の厚さ方向に長い紡錘形または涙滴形の多孔構造を形成しているものをいう。 In the present invention, the "porous body" refers to a body having a large number of pores which can be naturally obtained by solidifying a urethane resin composition by a wet film-forming method. It refers to those that form a spindle-shaped or teardrop-shaped porous structure.

本発明は、ウレタン樹脂(A)、溶剤(B)、及び、特定の成膜助剤(C)を含有するウレタン樹脂組成物を湿式成膜して多孔体を製造する方法である。 The present invention is a method for producing a porous body by wet film-forming of a urethane resin composition containing a urethane resin (A), a solvent (B), and a specific film-forming aid (C).

本発明においては、成膜助剤(C)として、ポリオキシプロピレン構造を有し、1分子あたりの平均水酸基数が2を超えて4以下のポリオール(c1)を用いることが必須である。前記ポリオール(c1)は、疎水性が高いため、ウレタン樹脂の凝固速度がマイルドとなるため、多孔セルが細かく均一となる。前記ポリオール(c1)の平均水酸基数としては、より一層優れた多孔セル形成ができる点から、2.5~3.5の範囲であることが好ましい。 In the present invention, it is essential to use a polyol (c1) having a polyoxypropylene structure and having an average number of hydroxyl groups of more than 2 and 4 or less per molecule as the film forming aid (C). Since the polyol (c1) has high hydrophobicity, the coagulation speed of the urethane resin becomes mild, and the porous cells become fine and uniform. The average number of hydroxyl groups of the polyol (c1) is preferably in the range of 2.5 to 3.5 from the viewpoint of enabling more excellent porous cell formation.

前記ポリオール(c1)としては、例えば、グリセリンとプロピレンオキサイドとの付加物;グリセリンを開始剤として、プロピレンオキサイドを付加した後に、その末端にエチンオキサイドを更に付加したもの、グリセリンを開始剤として、プロピレンオキサイド及びエチレンオキサイドの混合物を付加したもの等のグリセリンとプロピレンオキサイドとエチレンオキサイドとの反応物;トリメチロールプロパンとプロピレンオキサイドとの付加物;トリメチロールプロパンを開始剤として、プロピレンオキサイドを付加した後に、その末端にエチンオキサイドを更に付加したもの、トリメチロールプロパンを開始剤として、プロピレンオキサイド及びエチレンオキサイドの混合物を付加したもの等のトリメチロールプロパンとプロピレンオキサイドとエチレンオキサイドとの反応物などを用いることができる。これらの中でも、より一層優れた多孔セル形成ができる点から、グリセリンとプロピレンオキサイドとの付加物、及び/又は、トリメチロールプロパンとプロピレンオキサイドとの付加物を用いることが好ましい。 Examples of the polyol (c1) include, for example, an adduct of glycerin and propylene oxide; a product obtained by adding propylene oxide to glycerin as an initiator and then adding ethyne oxide to the end thereof; using glycerin as an initiator and propylene Reactions of glycerin, propylene oxide and ethylene oxide, such as adducts of mixtures of oxide and ethylene oxide; adducts of trimethylolpropane and propylene oxide; trimethylolpropane as initiator, after addition of propylene oxide, A reaction product of trimethylolpropane, propylene oxide and ethylene oxide, such as a product obtained by adding an ethyne oxide to the end thereof, or a product obtained by adding a mixture of propylene oxide and ethylene oxide using trimethylolpropane as an initiator, may be used. can. Among these, it is preferable to use an adduct of glycerin and propylene oxide and/or an adduct of trimethylolpropane and propylene oxide from the point of being able to form more excellent porous cells.

前記ポリオール(c1)の数平均分子量としては、より一層優れた多孔セル形成ができる点から、450~10,000の範囲であることが好ましく、1,000~7,000の範囲がより好ましい。なお、前記ポリオール(c1)の数平均分子量は、ゲル・パーミエーション・クロマトグラフィー(GPC)法により、下記の条件で測定した値を示す。 The number average molecular weight of the polyol (c1) is preferably in the range of 450 to 10,000, more preferably in the range of 1,000 to 7,000, from the viewpoint of forming more excellent porous cells. The number average molecular weight of the polyol (c1) is a value measured under the following conditions by a gel permeation chromatography (GPC) method.

前記ポリオール(c1)の含有量としては、より一層優れた多孔セル形成ができる点から、前記ウレタン樹脂(A)100質量部に対して、0.1~30質量部の範囲であることが好ましく、0.5~20質量部の範囲がより好ましい。 The content of the polyol (c1) is preferably in the range of 0.1 to 30 parts by mass with respect to 100 parts by mass of the urethane resin (A), in order to form more excellent porous cells. , more preferably in the range of 0.5 to 20 parts by mass.

本発明で用いるウレタン樹脂(A)としては、例えば、ポリオール(a1)とポリイソシアネート(a2)との反応物を用いることができる。 As the urethane resin (A) used in the present invention, for example, a reaction product of a polyol (a1) and a polyisocyanate (a2) can be used.

前記ポリオール(a1)としては、例えば、ポリエステルポリオール、ポリエーテルポリオール、ポリカーボネートポリオール等を用いることができる。これらのポリオールは単独で用いても2種以上を併用してもよい。 As the polyol (a1), for example, polyester polyol, polyether polyol, polycarbonate polyol, etc. can be used. These polyols may be used alone or in combination of two or more.

前記ポリオール(a1)の数平均分子量としては、多孔体の機械的特性、及び、柔軟性の点から、500~10,000の範囲であることが好ましく、700~8,000の範囲がより好ましい。なお、前記ポリオール(a1)の数平均分子量は、ゲル・パーミエーション・クロマトグラフィー(GPC)法により測定した値を示す。 The number average molecular weight of the polyol (a1) is preferably in the range of 500 to 10,000, more preferably in the range of 700 to 8,000, from the viewpoint of the mechanical properties and flexibility of the porous body. . The number average molecular weight of the polyol (a1) is the value measured by gel permeation chromatography (GPC).

前記ポリオール(a1)には、必要に応じて、数平均分子量が500未満の鎖伸長剤(a1-1)を併用してもよい。前記鎖伸長剤(a1-1)としては、例えば、水酸基を有する鎖伸長剤、アミノ基を有する鎖伸長剤等を用いることができる。これらの鎖伸長剤(a1-1)は単独で用いても2種以上を併用してもよい。 The polyol (a1) may be used in combination with a chain extender (a1-1) having a number average molecular weight of less than 500, if necessary. As the chain extender (a1-1), for example, a chain extender having a hydroxyl group, a chain extender having an amino group, or the like can be used. These chain extenders (a1-1) may be used alone or in combination of two or more.

前記水酸基を有する鎖伸長剤としては、例えば、エチレングリコール、ジエチレンリコール、トリエチレングリコール、プロピレングリコール、1,3-プロパンジオール、1,3-ブタンジオール、1,4-ブタンジオール、ヘキサメチレングリコール、サッカロース、メチレングリコール、グリセリン、ソルビトール等の脂肪族ポリオール化合物;ビスフェノールA、4,4’-ジヒドロキシジフェニル、4,4’-ジヒドロキシジフェニルエーテル、4,4’-ジヒドロキシジフェニルスルホン、水素添加ビスフェノールA、ハイドロキノン等の芳香族ポリオール化合物;水などを用いることができる。これらの鎖伸長剤は単独で用いても2種以上を併用してもよい。 Examples of the chain extender having a hydroxyl group include ethylene glycol, diethylene glycol, triethylene glycol, propylene glycol, 1,3-propanediol, 1,3-butanediol, 1,4-butanediol, hexamethylene glycol, Aliphatic polyol compounds such as sucrose, methylene glycol, glycerin, sorbitol; bisphenol A, 4,4'-dihydroxydiphenyl, 4,4'-dihydroxydiphenyl ether, 4,4'-dihydroxydiphenyl sulfone, hydrogenated bisphenol A, hydroquinone, etc. of aromatic polyol compounds; water and the like can be used. These chain extenders may be used alone or in combination of two or more.

前記アミノ基を有する鎖伸長剤としては、例えば、エチレンジアミン、1,2-プロパンジアミン、1,6-ヘキサメチレンジアミン、ピペラジン、2-メチルピペラジン、2,5-ジメチルピペラジン、イソホロンジアミン、4,4’-ジシクロヘキシルメタンジアミン、3,3’-ジメチル-4,4’-ジシクロヘキシルメタンジアミン、1,2-シクロヘキサンジアミン、1,4-シクロヘキサンジアミン、アミノエチルエタノールアミン、ヒドラジン、ジエチレントリアミン、トリエチレンテトラミン等を用いることができる。これらの鎖伸長剤は単独で用いても2種以上を併用してもよい。 Examples of the chain extender having an amino group include ethylenediamine, 1,2-propanediamine, 1,6-hexamethylenediamine, piperazine, 2-methylpiperazine, 2,5-dimethylpiperazine, isophoronediamine, 4,4 '-dicyclohexylmethanediamine, 3,3'-dimethyl-4,4'-dicyclohexylmethanediamine, 1,2-cyclohexanediamine, 1,4-cyclohexanediamine, aminoethylethanolamine, hydrazine, diethylenetriamine, triethylenetetramine, etc. can be used. These chain extenders may be used alone or in combination of two or more.

前記ポリイソシアネート(a2)としては、例えば、4,4’-ジフェニルメタンジイソシアネート、2,4’-ジフェニルメタンジイソシアネート、カルボジイミド変性ジフェニルメタンジイソシアネート、クルードジフェニルメタンジイソシアネート、フェニレンジイソシアネート、トリエンジイソシアネート、ナフタレンジイソシアネート、キシリレンジイソシアネート、テトラメチルキシリレンジイソシアネート等の芳香族ポリイソシアネート;ヘキサメチレンジイソシアネート、リジンジイソシアネート等の脂肪族ポリイソシアネート;シクロヘキサンジイソシアネート、水添キシリレンジイソシアネート、イソホロンジイソシアネート、ジシクロヘキシルメタンジイソシアネート等の脂環式ポリイソシアネートなどを用いることができる。これらのポリイソシアネートは単独で用いても2種以上を併用してもよい。 Examples of the polyisocyanate (a2) include 4,4′-diphenylmethane diisocyanate, 2,4′-diphenylmethane diisocyanate, carbodiimide-modified diphenylmethane diisocyanate, crude diphenylmethane diisocyanate, phenylene diisocyanate, triene diisocyanate, naphthalene diisocyanate, xylylene diisocyanate, tetra Aromatic polyisocyanates such as methylxylylene diisocyanate; Aliphatic polyisocyanates such as hexamethylene diisocyanate and lysine diisocyanate; Alicyclic polyisocyanates such as cyclohexane diisocyanate, hydrogenated xylylene diisocyanate, isophorone diisocyanate and dicyclohexylmethane diisocyanate; can be done. These polyisocyanates may be used alone or in combination of two or more.

前記ウレタン樹脂(A)の製造方法としては、例えば、前記ポリオール(a1)と前記ポリイソシアネート(a2)と必要に応じて前記鎖伸長剤(a1-1)とを仕込み、反応させることによって製造する方法が挙げられる。これらの反応は、50~100℃の温度で概ね3~10時間行うことが好ましい。また、前記反応は、後述する溶剤(B)中で行ってもよい。 As a method for producing the urethane resin (A), for example, the polyol (a1), the polyisocyanate (a2) and, if necessary, the chain extender (a1-1) are charged and reacted. method. These reactions are preferably carried out at a temperature of 50 to 100° C. for approximately 3 to 10 hours. Moreover, you may perform the said reaction in the solvent (B) mentioned later.

前記ポリオール(a1)が有する水酸基並びに前記鎖伸長剤(a1-1)が有する水酸基及びアミノ基の合計と、前記ポリイソシアネート(a2)が有するイソシアネート基とのモル比[(イソシアネート基)/(水酸基及びアミノ基)]としては、0.8~1.2の範囲であることが好ましく、0.9~1.1の範囲であることがより好ましい。 The molar ratio of the sum of the hydroxyl groups of the polyol (a1) and the hydroxyl groups and amino groups of the chain extender (a1-1) to the isocyanate groups of the polyisocyanate (a2) [(isocyanate group)/(hydroxyl group and amino group)] is preferably in the range of 0.8 to 1.2, more preferably in the range of 0.9 to 1.1.

以上の方法により得られるウレタン樹脂(A)の重量平均分子量としては、多孔体の機械的強度及び柔軟性の点から、5,000~1,000,000の範囲であることが好ましく、10,000~500,000の範囲がより好ましい。なお、前記ウレタン樹脂(A)の重量平均分子量は、前記ポリオール(a1)の数平均分子量と同様に測定して得られた値を示す。 The weight average molecular weight of the urethane resin (A) obtained by the above method is preferably in the range of 5,000 to 1,000,000 from the viewpoint of the mechanical strength and flexibility of the porous body. A range of 000 to 500,000 is more preferred. The weight average molecular weight of the urethane resin (A) is the value obtained by measuring in the same manner as the number average molecular weight of the polyol (a1).

前記ウレタン樹脂(A)の含有量としては、例えば、ウレタン樹脂組成物中10~90質量部の範囲が挙げられる。 The content of the urethane resin (A) is, for example, in the range of 10 to 90 parts by mass in the urethane resin composition.

前記溶剤(B)としては、例えば、酢酸エチル、酢酸メチル、酢酸ブチル、アセトン、メチルエチルケトン、メチルイソブチルケトン、ヘプタン、ヘキサン、シクロヘキサン、メチルシクロヘキサン、トルエン、o-キシレン、m-キシレン、p-キシレン、メタノール、エタノール、イソプロピルアルコール、イソブタノール、sec-ブタノール、ターシャリーブタノール、N,N,2-トリメチルプロピオンアミド、N,N-ジメチルアクリルアミド、N,N-ジメチルプロピオンアミド、N,N-ジエチルアセトアミド、N,N-ジエチルアクリルアミド、1,3-ジメチル-2-イミダゾリジノン、N-エチルピロリドン、2-ピロリドン等を用いることができる。これらの有機溶媒は単独で用いても2種以上を併用してもよい。 Examples of the solvent (B) include ethyl acetate, methyl acetate, butyl acetate, acetone, methyl ethyl ketone, methyl isobutyl ketone, heptane, hexane, cyclohexane, methylcyclohexane, toluene, o-xylene, m-xylene, p-xylene, methanol, ethanol, isopropyl alcohol, isobutanol, sec-butanol, tertiary butanol, N,N,2-trimethylpropionamide, N,N-dimethylacrylamide, N,N-dimethylpropionamide, N,N-diethylacetamide, N,N-diethylacrylamide, 1,3-dimethyl-2-imidazolidinone, N-ethylpyrrolidone, 2-pyrrolidone and the like can be used. These organic solvents may be used alone or in combination of two or more.

前記溶剤(B)の含有量としては、例えば、ウレタン樹脂組成物中10~90質量%の範囲が挙げられる。 The content of the solvent (B) is, for example, in the range of 10 to 90% by mass in the urethane resin composition.

前記ウレタン樹脂組成物は、前記ウレタン樹脂(A)、前記溶剤(B)、及び、前記成膜助剤(C)を必須成分として含有するが、必要に応じて、その他の添加剤を含有してもよい。 The urethane resin composition contains the urethane resin (A), the solvent (B), and the film-forming aid (C) as essential components, and optionally contains other additives. may

前記その他の添加剤としては、例えば、前記(c1)以外の成膜助剤、顔料、難燃剤、可塑剤、軟化剤、安定剤、ワックス、消泡剤、分散剤、浸透剤、界面活性剤、フィラー、防黴剤、抗菌剤、紫外線吸収剤、酸化防止剤、耐候安定剤、蛍光増白剤、老化防止剤、増粘剤等を用いることができる。これらの添加剤は単独で用いても2種以上を併用してもよい。 Examples of the other additives include film formation aids other than (c1), pigments, flame retardants, plasticizers, softeners, stabilizers, waxes, antifoaming agents, dispersants, penetrants, and surfactants. , a filler, an antifungal agent, an antibacterial agent, an ultraviolet absorber, an antioxidant, a weather stabilizer, a fluorescent whitening agent, an antiaging agent, a thickener, and the like. These additives may be used alone or in combination of two or more.

次に、前記ウレタン樹脂組成物を湿式成膜法により多孔体を製造する方法について説明する。 Next, a method for producing a porous body from the urethane resin composition by a wet film-forming method will be described.

前記湿式成膜法とは、前記ウレタン樹脂組成物を、基材表面に塗布または含浸し、次いで、該塗布面または含浸面に水や水蒸気等を接触させることによって前記ウレタン樹脂(A)を凝固させ多孔体を製造する方法である。 In the wet film-forming method, the urethane resin composition is applied or impregnated onto the surface of a base material, and then the urethane resin (A) is solidified by bringing the coated surface or the impregnated surface into contact with water, steam, or the like. This is a method for producing a strained porous body.

前記ウレタン樹脂組成物を塗布する基材としては、例えば、不織布、織布、編み物からなる基材;樹脂フィルム等を用いることができる。前記基材を構成するものとしては、例えば、ポリエステル繊維、ナイロン繊維、アクリル繊維、ポリウレタン繊維、アセテート繊維、レーヨン繊維、ポリ乳酸繊維等の化学繊維;綿、麻、絹、羊毛、これらの混紡繊維などを用いることができる。 As the base material to which the urethane resin composition is applied, for example, a base material made of a nonwoven fabric, a woven fabric, or a knitted fabric; a resin film or the like can be used. Chemical fibers such as polyester fiber, nylon fiber, acrylic fiber, polyurethane fiber, acetate fiber, rayon fiber, and polylactic acid fiber; cotton, hemp, silk, wool, and blended fibers thereof. etc. can be used.

前記基材の表面には、必要に応じて制電加工、離型処理加工、撥水加工、吸水加工、抗菌防臭加工、制菌加工、紫外線遮断加工等の処理が施されていてもよい。 If necessary, the surface of the base material may be subjected to antistatic treatment, release treatment, water repellent treatment, water absorption treatment, antibacterial deodorant treatment, antibacterial treatment, ultraviolet shielding treatment, and the like.

前記基材表面に前記ウレタン樹脂組成物を塗布または含浸する方法としては、例えば、グラビアコーター法、ナイフコーター法、パイプコーター法、コンマコーター法が挙げられる。その際、ウレタン樹脂組成物の粘度を調整し塗工作業性を向上するため、必要に応じて、有機溶剤(B)の使用量を調節して良い。 Examples of the method of applying or impregnating the urethane resin composition onto the substrate surface include gravure coater method, knife coater method, pipe coater method, and comma coater method. At that time, the amount of the organic solvent (B) used may be adjusted as necessary in order to adjust the viscosity of the urethane resin composition and improve the coating workability.

前記方法により塗布または含浸された前記ウレタン樹脂組成物からなる塗膜の膜厚としては、0.5~5mmの範囲であることが好ましく、0.5~3mmの範囲がより好ましい。 The thickness of the coating film made of the urethane resin composition applied or impregnated by the above method is preferably in the range of 0.5 to 5 mm, more preferably in the range of 0.5 to 3 mm.

前記ウレタン樹脂組成物が塗布または含浸され形成した塗布面に水または水蒸気を接触させる方法としては、例えば、前記ウレタン樹脂組成物からなる塗布層や含浸層の設けられた基材を水浴中に浸漬する方法;前記塗布面上にスプレー等を用いて水を噴霧する方法などが挙げられる。前記浸漬は、例えば、5~60℃の水浴中に、2~20分間行うことが挙げられる。 As a method of bringing water or steam into contact with the coated surface formed by coating or impregnating the urethane resin composition, for example, a substrate provided with a coating layer or an impregnated layer made of the urethane resin composition is immersed in a water bath. a method of spraying water onto the coating surface using a spray or the like. The immersion is performed, for example, in a water bath at 5 to 60° C. for 2 to 20 minutes.

前記方法によって得られた多孔体は、常温の水や温水を用いてその表面を洗浄して溶剤(B)を抽出除去し、次いで乾燥することが好ましい。前記洗浄は、例えば、5~60℃の水で20~120分間行うことが挙げられ、洗浄に用いる水は1回以上入れ替えるか、あるいは、流水で連続して入れ替えるのが好ましい。前記乾燥は、例えば、80~120℃に調整した乾燥機等を使用して、10~60分間行うことが好ましい。 The surface of the porous body obtained by the above method is preferably washed with water at room temperature or warm water to extract and remove the solvent (B), and then dried. The washing may be carried out, for example, with water of 5 to 60° C. for 20 to 120 minutes, and the water used for washing is preferably replaced once or more, or continuously replaced with running water. The drying is preferably carried out for 10 to 60 minutes using, for example, a dryer adjusted to 80 to 120°C.

以上、本発明によれば、特定の成膜助剤を用いることで、湿式成膜法により、細かく均一な多孔体を製造することができる。よって、本発明は、研磨パッド、人工皮革・合成皮革の製造に特に好適に使用することができる。 As described above, according to the present invention, a fine and uniform porous body can be produced by a wet film-forming method by using a specific film-forming aid. Therefore, the present invention can be used particularly preferably for manufacturing polishing pads, artificial leathers and synthetic leathers.

以下、実施例を用いて、本発明をより詳細に説明する。 The present invention will be described in more detail below using examples.

[合成例1]ウレタン樹脂(A-1)の合成
攪拌機、還流器、温度計を有する反応装置に、ポリエステルポリオール(エチレングリコール及びアジピン酸の反応物、数平均分子量;2,000)を100質量部、1,4-ブタンジオールを20質量部、N,N-ジメチルホルムアミドを564質量部、及び、4,4’-ジフェニルメタンジイソシアネートを68質量部投入し、撹拌下60℃で6時間反応させ、引き続き、イソプロピルアルコールを1質量部投入して、更に60℃で1時間撹拌することによって、ウレタン樹脂組成物を得た。
得られたウレタン樹脂組成物は、固形分;25質量%、粘度;600dPa・s、ウレタン樹脂の重量平均分子量は188,100であった。
[Synthesis Example 1] Synthesis of urethane resin (A-1) 100 mass of polyester polyol (reaction product of ethylene glycol and adipic acid, number average molecular weight: 2,000) was placed in a reactor equipped with a stirrer, a reflux device, and a thermometer. parts, 20 parts by mass of 1,4-butanediol, 564 parts by mass of N,N-dimethylformamide, and 68 parts by mass of 4,4′-diphenylmethane diisocyanate, and reacted at 60° C. for 6 hours with stirring, Subsequently, 1 part by mass of isopropyl alcohol was added, and the mixture was further stirred at 60° C. for 1 hour to obtain a urethane resin composition.
The resulting urethane resin composition had a solid content of 25% by mass, a viscosity of 600 dPa·s, and a weight average molecular weight of 188,100.

[数平均分子量・重量平均分子量の測定方法]
合成例で用いた原料ポリオールの数平均分子量、ポリオール(c1)の数平均分子量、ウレタン樹脂(A)の重量平均分子量 は、ゲル・パーミエーション・クロマトグラフィー(GPC)法により、下記の条件で測定した値を示す。
[Method for measuring number average molecular weight/weight average molecular weight]
The number average molecular weight of the raw material polyol, the number average molecular weight of the polyol (c1), and the weight average molecular weight of the urethane resin (A) used in Synthesis Examples were measured by gel permeation chromatography (GPC) under the following conditions. value.

測定装置:高速GPC装置(東ソー株式会社製「HLC-8220GPC」)
カラム:東ソー株式会社製の下記のカラムを直列に接続して使用した。
「TSKgel G5000」(7.8mmI.D.×30cm)×1本
「TSKgel G4000」(7.8mmI.D.×30cm)×1本
「TSKgel G3000」(7.8mmI.D.×30cm)×1本
「TSKgel G2000」(7.8mmI.D.×30cm)×1本
検出器:RI(示差屈折計)
カラム温度:40℃
溶離液:テトラヒドロフラン(THF)
流速:1.0mL/分
注入量:100μL(試料濃度0.4質量%のテトラヒドロフラン溶液)
標準試料:下記の標準ポリスチレンを用いて検量線を作成した。
Measuring device: High-speed GPC device ("HLC-8220GPC" manufactured by Tosoh Corporation)
Column: The following columns manufactured by Tosoh Corporation were connected in series and used.
"TSKgel G5000" (7.8mm I.D. x 30cm) x 1 "TSKgel G4000" (7.8mm I.D. x 30cm) x 1 "TSKgel G3000" (7.8mm I.D. x 30cm) x 1 Book "TSKgel G2000" (7.8 mm I.D. x 30 cm) x 1 Detector: RI (differential refractometer)
Column temperature: 40°C
Eluent: Tetrahydrofuran (THF)
Flow rate: 1.0 mL/min Injection volume: 100 μL (tetrahydrofuran solution with a sample concentration of 0.4% by mass)
Standard sample: A calibration curve was created using the following standard polystyrene.

(標準ポリスチレン)
東ソー株式会社製「TSKgel 標準ポリスチレン A-500」
東ソー株式会社製「TSKgel 標準ポリスチレン A-1000」
東ソー株式会社製「TSKgel 標準ポリスチレン A-2500」
東ソー株式会社製「TSKgel 標準ポリスチレン A-5000」
東ソー株式会社製「TSKgel 標準ポリスチレン F-1」
東ソー株式会社製「TSKgel 標準ポリスチレン F-2」
東ソー株式会社製「TSKgel 標準ポリスチレン F-4」
東ソー株式会社製「TSKgel 標準ポリスチレン F-10」
東ソー株式会社製「TSKgel 標準ポリスチレン F-20」
東ソー株式会社製「TSKgel 標準ポリスチレン F-40」
東ソー株式会社製「TSKgel 標準ポリスチレン F-80」
東ソー株式会社製「TSKgel 標準ポリスチレン F-128」
東ソー株式会社製「TSKgel 標準ポリスチレン F-288」
東ソー株式会社製「TSKgel 標準ポリスチレン F-550」
(standard polystyrene)
"TSKgel standard polystyrene A-500" manufactured by Tosoh Corporation
"TSKgel standard polystyrene A-1000" manufactured by Tosoh Corporation
"TSKgel standard polystyrene A-2500" manufactured by Tosoh Corporation
"TSKgel standard polystyrene A-5000" manufactured by Tosoh Corporation
"TSKgel standard polystyrene F-1" manufactured by Tosoh Corporation
"TSKgel standard polystyrene F-2" manufactured by Tosoh Corporation
"TSKgel standard polystyrene F-4" manufactured by Tosoh Corporation
"TSKgel standard polystyrene F-10" manufactured by Tosoh Corporation
"TSKgel standard polystyrene F-20" manufactured by Tosoh Corporation
"TSKgel standard polystyrene F-40" manufactured by Tosoh Corporation
"TSKgel standard polystyrene F-80" manufactured by Tosoh Corporation
"TSKgel standard polystyrene F-128" manufactured by Tosoh Corporation
"TSKgel standard polystyrene F-288" manufactured by Tosoh Corporation
"TSKgel standard polystyrene F-550" manufactured by Tosoh Corporation

[実施例1]
合成例1で得られたウレタン樹脂組成物100質量部に対し、N,N-ジメチルホルムアミド(以下、「DMF」と略記する。)を40質量部、ポリプロピレントリオール(AGC株式会社製「エクセノール3030」、官能基数;3、数平均分子量3,000、以下「c1-1」」と略記する。)を2質量部加えて配合液を作成し、厚さ(Wet)1mmとなるようにポリエチレンテレフタレート(PET)フィルムに塗布した。次いで、凝固浴(25℃の水)へ塗布基材を10分間浸漬させ、ウレタン樹脂を凝固させた。その後、この基材を50℃の水に60分間浸漬させて溶剤を洗浄した。洗浄後、基材を100℃で30分間熱風乾燥させ、多孔体を得た。
[Example 1]
Per 100 parts by mass of the urethane resin composition obtained in Synthesis Example 1, 40 parts by mass of N,N-dimethylformamide (hereinafter abbreviated as "DMF") and polypropylene triol ("Exenol 3030" manufactured by AGC Co., Ltd. , number of functional groups: 3, number average molecular weight of 3,000, hereinafter abbreviated as “c1-1”.) to prepare a blended solution, and polyethylene terephthalate ( PET) film. Then, the coated substrate was immersed in a coagulation bath (25° C. water) for 10 minutes to coagulate the urethane resin. After that, the substrate was immersed in water at 50° C. for 60 minutes to wash off the solvent. After washing, the substrate was dried with hot air at 100° C. for 30 minutes to obtain a porous body.

[実施例2]
実施例1において、c1-1に代えて、ポリプロピレントリオール(旭硝子ウレタン株式会社製「エクセノール2030」、官能基数;3、数平均分子量2,000、以下「c1-2」」と略記する。)を用いた以外は、実施例1と同様にして多孔体を得た。
[Example 2]
In Example 1, instead of c1-1, polypropylene triol ("Exenol 2030" manufactured by Asahi Glass Urethane Co., Ltd., number of functional groups: 3, number average molecular weight: 2,000, hereinafter abbreviated as "c1-2") was used. A porous body was obtained in the same manner as in Example 1, except that it was used.

[実施例3]
実施例1において、c1-1に代えて、ポリプロピレントリオール(旭硝子ウレタン株式会社製「エクセノール5030」、官能基数;3、数平均分子量5,000、以下「c1-3」」と略記する。)を用いた以外は、実施例1と同様にして多孔体を得た。
[Example 3]
In Example 1, instead of c1-1, polypropylene triol ("Exenol 5030" manufactured by Asahi Glass Urethane Co., Ltd., number of functional groups: 3, number average molecular weight: 5,000, hereinafter abbreviated as "c1-3") was used. A porous body was obtained in the same manner as in Example 1, except that it was used.

[比較例1]
実施例1において、c1-1に代えて、ポリプロピレングリコール(旭硝子ウレタン株式会社製「エクセノール3020」、官能基数;2、数平均分子量3,200、以下「cR1-1」」と略記する。)を用いた以外は、実施例1と同様にして多孔体を得た。
[Comparative Example 1]
In Example 1, instead of c1-1, polypropylene glycol (“Exenol 3020” manufactured by Asahi Glass Urethane Co., Ltd., number of functional groups: 2, number average molecular weight of 3,200, hereinafter abbreviated as “cR1-1”) was used. A porous body was obtained in the same manner as in Example 1, except that it was used.

[比較例2]
実施例1において、c1-1に代えて、ドデシルベンゼンスルホン酸(以下「DBS」と略記する。)を用いた以外は、実施例1と同様にして多孔体を得た。
[Comparative Example 2]
A porous body was obtained in the same manner as in Example 1, except that dodecylbenzenesulfonic acid (hereinafter abbreviated as "DBS") was used instead of c1-1.

[湿式成膜性の評価方法]
実施例で得られた多孔体の断面状態を、日本電子株式会社製走査型電子顕微鏡「JSM-IT500」(倍率:100倍)で観察し、セル形状(細さ、均一性)を確認し、最大横幅が70μm以下のセルが全体の60%を占めていれば「○」、それ以外は「×」と評価した。
[Method for evaluating wet film formability]
The cross-sectional state of the porous body obtained in the example was observed with a scanning electron microscope "JSM-IT500" manufactured by JEOL Ltd. (magnification: 100 times), and the cell shape (fineness, uniformity) was confirmed. If cells with a maximum lateral width of 70 μm or less accounted for 60% of the total, they were evaluated as “◯”, and otherwise as “X”.

[圧縮率の評価方法]
実施例で得られた多孔体について、JISL-1021-6に準拠して圧縮率評価を行った。具体的には、初荷重2kPaを30秒間かけた後の「標準圧力下における厚さ:t0」を測定し、次に、最終荷重98kPaの荷重を30秒間かけた後の「一定圧力下における厚さ:t1」を測定し、これを下記の式に適用して圧縮率を算出した。
圧縮率(%)=100×(t0-t1)/t0
これによって求められた圧縮率が20%以下であれば「○」、それ以外は「×」と評価した。
[Evaluation method of compression rate]
The porous bodies obtained in Examples were evaluated for compressibility in accordance with JISL-1021-6. Specifically, the “thickness under standard pressure: t0” after applying an initial load of 2 kPa for 30 seconds was measured, and then the “thickness under constant pressure” after applying a final load of 98 kPa for 30 seconds. t1” was measured and applied to the following formula to calculate the compression rate.
Compression rate (%) = 100 x (t0-t1)/t0
If the obtained compression rate was 20% or less, it was evaluated as "good", and otherwise as "poor".

Figure 0007331453000001
Figure 0007331453000001

本発明の製造方法により得られた多孔体は、セルが細かく均一であり、低圧縮率性にも優れることが分かった。 It was found that the porous body obtained by the production method of the present invention has fine and uniform cells and is excellent in low compressibility.

一方、比較例1は成膜助剤として、ポリオール(c1)の代わりに、平均水酸基数が2であるポリオールを用いた態様であるが、多孔セル形成が不良であり、低圧縮率性も不良であった。 On the other hand, Comparative Example 1 is an embodiment in which a polyol having an average number of hydroxyl groups of 2 was used instead of the polyol (c1) as a film-forming aid, but the formation of porous cells was poor and the low compressibility was also poor. Met.

比較例2は成膜助剤として、ポリオール(c1)の代わりに、ドデシルベンゼンスルホン酸を用いた態様であるが、多孔セル形成が不良であり、低圧縮率性も不良であった。 Comparative Example 2 is an embodiment in which dodecylbenzenesulfonic acid was used instead of the polyol (c1) as the film-forming aid.

Claims (6)

ウレタン樹脂(A)、溶剤(B)、及び、成膜助剤(C)を含有するウレタン樹脂組成物を湿式成膜して多孔体を製造する方法であって、
前記成膜助剤(C)が、ポリオキシプロピレン構造を有し、1分子あたりの平均水酸基数が2を超えて4以下のポリオール(c1)であり、
前記ポリオール(c1)が、グリセリンとプロピレンオキサイドとの付加物を含むものであることを特徴とする多孔体の製造方法。
A method for producing a porous body by wet film-forming of a urethane resin composition containing a urethane resin (A), a solvent (B), and a film-forming aid (C), comprising:
The film-forming aid (C) is a polyol (c1) having a polyoxypropylene structure and an average number of hydroxyl groups per molecule exceeding 2 and 4 or less,
A method for producing a porous body , wherein the polyol (c1) contains an adduct of glycerin and propylene oxide .
前記ウレタン樹脂(A)が、ポリエステルポリオールを含むポリオール(a1)を必須原料とするものである請求項1記載の多孔体の製造方法。2. The method for producing a porous body according to claim 1, wherein the urethane resin (A) contains a polyol (a1) containing a polyester polyol as an essential raw material. 前記ウレタン樹脂(A)が、さらに、数平均分子量500未満の鎖伸長剤(a1-1)を必須原料とするものであり、前記鎖伸長剤(a1-1)が、脂肪族ポリオール化合物を含むものである請求項1記載の多孔体の製造方法。The urethane resin (A) further contains a chain extender (a1-1) having a number average molecular weight of less than 500 as an essential raw material, and the chain extender (a1-1) contains an aliphatic polyol compound. 2. The method for producing a porous body according to claim 1, wherein 前記ウレタン樹脂(A)の重量平均分子量が、10,000~500,000の範囲である請求項1記載の多孔体の製造方法。2. The method for producing a porous body according to claim 1, wherein the urethane resin (A) has a weight average molecular weight in the range of 10,000 to 500,000. 前記ポリオール(c1)の数平均分子量が、450~10,000の範囲である請求項1記載の多孔体の製造方法。 2. The method for producing a porous body according to claim 1, wherein the polyol (c1) has a number average molecular weight in the range of 450 to 10,000. 前記ポリオール(c1)の含有量が、前記ウレタン樹脂(A)100質量部に対して、0.1~30質量部の範囲である請求項1~5の何れか1項記載の多孔体の製造方法。 The production of the porous body according to any one of claims 1 to 5, wherein the content of the polyol (c1) is in the range of 0.1 to 30 parts by mass with respect to 100 parts by mass of the urethane resin (A). Method.
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