JP2010235805A - Closed-cell urethane sheet and production method thereof - Google Patents

Closed-cell urethane sheet and production method thereof Download PDF

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JP2010235805A
JP2010235805A JP2009086071A JP2009086071A JP2010235805A JP 2010235805 A JP2010235805 A JP 2010235805A JP 2009086071 A JP2009086071 A JP 2009086071A JP 2009086071 A JP2009086071 A JP 2009086071A JP 2010235805 A JP2010235805 A JP 2010235805A
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urethane
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isocyanate
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JP5636164B2 (en
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Koichi Kusakawa
公一 草川
Noriyuki Sera
範幸 世良
Minoru Yoshioka
稔 吉岡
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NHK Spring Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a closed-cell urethane sheet which has the density lower than before and both of high extensibility and high strength while keeping waterproofness as a sealing material and to provide a production method of the closed-cell urethane sheet. <P>SOLUTION: The closed-cell urethane sheet is obtained by mixing a thermally expandable microcapsule in a liquid urethane raw material and is used as the sealing material. The liquid urethane raw material comprises an isocyanate-terminated urethane prepolymer being a reaction product obtained by reacting dimer acid-based polyol, low molecular weight glycol and isocyanate. The closed-cell urethane sheet has ≥90° contact angle. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、独泡ウレタンシート及びその製造方法に関する。具体的には、例えば自動車のテールランプのシール部のような自動車分野あるいは建築分野や家電分野等で防水シーリング材として利用される独泡ウレタンシート及びその製造方法に関する。   The present invention relates to a closed-cell urethane sheet and a method for producing the same. Specifically, the present invention relates to a closed-cell urethane sheet used as a waterproof sealing material, for example, in the automobile field, such as a car tail lamp seal part, or in the field of construction or home appliances, and a manufacturing method thereof.

周知の如く、軟質ウレタンフォームは連続気泡であることが一般的である。また、独立気泡のウレタンフォームを得ようとしても、収縮し易く、収縮しないようにするにはウレタンの剛性を上げていき、収縮力に耐える方法しかない。しかし、この方法では硬質のウレタンフォームは得られるが、軟質のウレタンフォームは原理的に得られない。   As is well known, flexible urethane foam is generally open-celled. Moreover, even if an attempt is made to obtain closed-cell urethane foam, there is only a method to withstand the shrinkage force by increasing the rigidity of urethane in order to prevent shrinkage. However, in this method, a hard urethane foam can be obtained, but a soft urethane foam cannot be obtained in principle.

従来、ウレタンフォームに関する技術としては、例えば特許文献1〜3が知られている。   Conventionally, for example, Patent Documents 1 to 3 are known as techniques related to urethane foam.

特許文献1には、特定のポリオール化合物と多官能イソシアネート化合物、整泡剤を添加して非反応性気体の存在下で攪拌し、メレンゲ状態の気泡分散液を得た後硬化させる技術が開示されている。特許文献1は、衝撃吸収性とクッション性に優れ、底着き感の無い軟質ポリウレタンフォームを提供することを目的とする。しかし、この技術では、機械的攪拌により気泡を混入させる方法であるため、密度は実施例1に記載のように0.85g/cmと高く、低密度にすることができない。 Patent Document 1 discloses a technique in which a specific polyol compound, a polyfunctional isocyanate compound, and a foam stabilizer are added and stirred in the presence of a non-reactive gas to obtain a meringue cell dispersion and then cured. ing. Patent document 1 aims at providing the flexible polyurethane foam which is excellent in shock absorption and cushioning properties, and does not have a feeling of bottoming. However, in this technique, since bubbles are mixed by mechanical stirring, the density is as high as 0.85 g / cm 3 as described in Example 1, and cannot be reduced.

特許文献2には、特定のポリプロピレングリコールに特定の溶解性を有するガスを溶解させて得られるポリウレタンフォームの製造方法について開示されている。しかし、特許文献2の場合、ポリウレタンフォームの平均密度が0.6〜1.0g/cmと低密度にならない。 Patent Document 2 discloses a method for producing a polyurethane foam obtained by dissolving a gas having a specific solubility in a specific polypropylene glycol. However, in the case of Patent Document 2, the average density of the polyurethane foam is not as low as 0.6 to 1.0 g / cm 3 .

特許文献3には、液状ポリウレタンプレポリマーと水とを含むポリウレタン組成物において、熱膨張性マイクロカプセルを配合したことを特徴とするポリウレタンフォーム組成物について開示されている。特許文献3は、低硬度で耐摩耗性に優れたウレタンフォームを得ることを目的とし、用途として、紙葉搬送ロールが挙げられている。なお、特許文献3において、熱膨張マイクロカプセルの配合量は0.25〜1.0重量部と少ない。   Patent Document 3 discloses a polyurethane foam composition in which a thermally expandable microcapsule is blended in a polyurethane composition containing a liquid polyurethane prepolymer and water. Patent Document 3 aims at obtaining a urethane foam having low hardness and excellent wear resistance, and a paper sheet transport roll is cited as an application. In Patent Document 3, the amount of thermally expanded microcapsules is as small as 0.25 to 1.0 parts by weight.

特開2005−264048号公報JP 2005-264048 A 特開2006−206793号公報JP 2006-206793 A 特開平6−199978号公報Japanese Patent Laid-Open No. 6-199978

本発明はこうした事情を考慮してなされたもので、従来と比べて低密度であるとともに、シーリング材として防水性を維持しつつ、高い伸びと強度を合わせ持つ独泡ウレタンシート及びその製造方法を提供することを目的とする。   The present invention has been made in consideration of such circumstances, and a closed-cell urethane sheet having a low density as compared with the conventional one and maintaining high waterproofness as a sealing material, and having both high elongation and strength, and a method for producing the same. The purpose is to provide.

本発明に係る独泡ウレタンシートは、液状ウレタン原料に熱膨張マイクロカプセルを配合してなる、シーリング材として利用される独泡ウレタンシートであり、前記液状ウレタン原料がダイマー酸系ポリオール及び低分子量グリコールとイソシアナートの反応生成物であるイソシアナート末端ウレタンプレポリマーよりなり、独泡ウレタンの接触角が90度以上であることを特徴とする。   The closed-cell urethane sheet according to the present invention is a closed-cell urethane sheet used as a sealing material, in which thermally expanded microcapsules are blended with a liquid urethane material, and the liquid urethane material is a dimer acid-based polyol and a low molecular weight glycol. And an isocyanate-terminated urethane prepolymer which is a reaction product of isocyanate and the contact angle of closed-cell urethane is 90 degrees or more.

本発明に係る独泡ウレタンシートの製造方法は、ダイマー酸系ポリオール及び低分子量グリコールとイソシアナートの反応生成物であるイソシアナート末端ウレタンプレポリマーよりなる液状ウレタン原料と、熱膨張マイクロカプセルを配合する工程と、この熱膨張マイクロカプセルを配合したウレタン原料を、離型性基材の少なくとも片側にシート状に塗布する工程と、シート状の液状ウレタン原料を加熱により発泡させて硬化し、ウレタンシートを形成する工程を具備することを特徴とする。   The process for producing a self-foaming urethane sheet according to the present invention comprises a liquid urethane raw material comprising a dimer acid-based polyol and an isocyanate-terminated urethane prepolymer which is a reaction product of a low molecular weight glycol and an isocyanate, and a thermal expansion microcapsule. A step of applying a urethane raw material containing the thermal expansion microcapsule in a sheet form on at least one side of the releasable substrate, and foaming and curing the sheet-like liquid urethane raw material to form a urethane sheet. It is characterized by comprising the step of forming.

本発明によれば、シーリング材として実用的に満足する高い伸び,強度の独泡ウレタンシートが得られる。また、得られる独泡ウレタンシートによれば、高い止水性とともに、透湿性が大幅に低減できる。   According to the present invention, a closed-cell urethane sheet having high elongation and strength that is practically satisfactory as a sealing material can be obtained. Moreover, according to the obtained self-foaming urethane sheet, moisture permeability can be significantly reduced along with high water-stopping properties.

図1は、本発明に係る独泡ウレタンシートの一例について、製造方法を工程順に示す断面図を示す。FIG. 1: shows sectional drawing which shows a manufacturing method in order of a process about an example of the closed cell urethane sheet which concerns on this invention. 図2は、本発明に係る片面にスキン層を有する独泡ウレタンシートの断面図を示す。FIG. 2 shows a cross-sectional view of a closed cell urethane sheet having a skin layer on one side according to the present invention.

次に、本発明について更に詳しく説明する。
周知の如く、一般に軟質ウレタンフォームは連続気泡であるが、疎水性原料を用いることにより止水性を発現するウレタン発泡体を作ることができる。このことは、例えば特公昭59−37036号公報、特公昭58−17784号公報に開示されている。しかし、連続気泡のため水蒸気が透過して、条件によってはシール構造物付近で結露が発生する可能性がある。従って、結露によって支障が生じる用途では独立気泡タイプの止水性シーリング材が望まれている。
Next, the present invention will be described in more detail.
As is well known, a flexible urethane foam is generally open-celled, but a urethane foam that exhibits water-stopping properties can be made by using a hydrophobic raw material. This is disclosed in, for example, Japanese Patent Publication No. 59-37036 and Japanese Patent Publication No. 58-17784. However, water vapor permeates due to open cells, and condensation may occur near the seal structure depending on conditions. Therefore, a closed cell type water-proof sealing material is desired for applications in which dew condensation causes trouble.

本発明者等は、独立気泡タイプのウレタンシーリング材実現のために、ウレタン原料に膨張マイクロカプセルを配合した発泡ウレタンフォームを以前から研究しており、その結果、単に膨張マイクロカプセルと液状ウレタン原料を配合しただけのものでは、十分な伸びと強度を得ることは困難で、シーリング材として用いた場合に裂けたり接着時に切れたりして実用上問題があることを既に究明している。   In order to realize a closed-cell type urethane sealant, the present inventors have been researching foamed urethane foams in which expanded microcapsules are blended with urethane raw materials, and as a result, simply expanded microcapsules and liquid urethane raw materials. It is difficult to obtain sufficient elongation and strength with only the blending, and it has already been found that there is a practical problem that it is torn or cut at the time of adhesion when used as a sealing material.

このようなことから、本発明者は、上述したように、液状ウレタン原料に熱膨張マイクロカプセルを配合してなり、液状ウレタン原料がダイマー酸系ポリオール及び低分子量グリコールとイソシアナートの反応生成物であるイソシアナート末端ウレタンプレポリマーよりなり、独泡ウレタンの接触角が90度以上である独泡ウレタンシートを究明するに至ったものである。本発明では、熱膨張マイクロカプセルを配合すると同時に接触角を90度以上とした疎水性ウレタンにすることで、独立気泡が付加されるために止水性や耐透湿性が大幅に向上する。   For this reason, as described above, the present inventor blended thermal expansion microcapsules with a liquid urethane raw material, and the liquid urethane raw material is a reaction product of dimer acid polyol, low molecular weight glycol and isocyanate. The present invention has led to the investigation of a closed-cell urethane sheet comprising a certain isocyanate-terminated urethane prepolymer and having a closed-cell urethane contact angle of 90 degrees or more. In the present invention, when the thermally expanded microcapsules are blended and at the same time a hydrophobic urethane having a contact angle of 90 degrees or more is added, closed cells are added, so that the water-stopping property and moisture permeability resistance are greatly improved.

本発明において、液状ウレタン原料はダイマー酸系ポリオール、前記のイソシアナート末端プレポリマー、発泡剤、触媒、架橋剤などからなり、これらを混合することでウレタン発泡体が製造できる。
使用できる前記ポリオールとしては、例えばダイマー酸ポリエステルポリオールが挙げられる。ダイマー酸とは、トール油脂肪酸などの不飽和脂肪酸の二量体で、略二価の脂肪酸である。ダイマー酸ポリエステルポリオールとは、このダイマー酸と短鎖ジオールとのポリエステルである。その他のダイマー酸系ポリオールとしては、ダイマー酸を水素添加して得られるダイマージオールとアジピン酸やセバチン酸などの二塩基性酸とのポリエステル、あるいはダイマー酸及びダイマージオールにプロピレンオキサイドやエチレンオキサイドを付加重合したアルキレンポリオールなどが例示できる。これらのダイマー酸系ポリオールを用いることで、疎水性が向上し止水性及び透湿性の向上がはかられる。
In this invention, a liquid urethane raw material consists of a dimer acid type polyol, said isocyanate terminal prepolymer, a foaming agent, a catalyst, a crosslinking agent, etc., A urethane foam can be manufactured by mixing these.
Examples of the polyol that can be used include dimer acid polyester polyol. Dimer acid is a dimer of unsaturated fatty acid such as tall oil fatty acid, which is a substantially divalent fatty acid. The dimer acid polyester polyol is a polyester of this dimer acid and a short chain diol. Other dimer acid polyols include dimer diols obtained by hydrogenation of dimer acid and polyesters of dibasic acids such as adipic acid and sebacic acid, or propylene oxide and ethylene oxide added to dimer acid and dimer diol. Examples include polymerized alkylene polyols. By using these dimer acid-based polyols, hydrophobicity is improved, and water-stopping and moisture permeability are improved.

本発明において、低分子量グリコールとイソシアナートとの反応生成物であるイソシアネート末端プレポリマーとは、低分子量のグリコール類としてポリアルキレングリコール、ポリエステルジオール、ポリテトラメチレングリコール、ポリカプロラクトングリコール等とMDI系ポリイソシアネート、トリレンジイソシアネート、トリジンジイソシアネート、ナフタリンジイソシアネートなどの芳香族系ポリイソシアネート、ヘキサメチレンジイソシアネート、イソホロンジイソシアネート、キシリレンジイソシアネート、水添XDIなどのジイソシアナートとの反応性生物である。前記低分子グリコールの分子量は、300〜1000であることが伸びと強度を向上することが顕著であり好ましい。これらのイソシアネート末端プレポリマーのNCO%は、10〜25%であることが伸び・強度の向上および原料の粘度が低いことから好ましい。   In the present invention, an isocyanate-terminated prepolymer which is a reaction product of a low molecular weight glycol and an isocyanate is a low molecular weight glycol such as polyalkylene glycol, polyester diol, polytetramethylene glycol, polycaprolactone glycol or the like and an MDI-based polypolymer. It is a reactive organism with diisocyanates such as aromatic polyisocyanates such as isocyanate, tolylene diisocyanate, tolidine diisocyanate and naphthalene diisocyanate, hexamethylene diisocyanate, isophorone diisocyanate, xylylene diisocyanate and hydrogenated XDI. The molecular weight of the low-molecular glycol is preferably from 300 to 1,000 because it is remarkable that the elongation and strength are improved. The NCO% of these isocyanate-terminated prepolymers is preferably 10 to 25% because elongation / strength is improved and the viscosity of the raw material is low.

本発明において、イソシアネート末端プレポリマーとポリオールとの混合比は、NCO/OH(インデックス)が0.8〜1.4の範囲となるようにするのが望ましい。ここで、インデックスが0.8未満では、得られるポリウレタンフォームの止水性や永久歪みなどの物性が低下し、1.4を越えると架橋反応が進み過ぎて成形性が低下する。   In the present invention, it is desirable that the mixing ratio of the isocyanate-terminated prepolymer and the polyol is such that NCO / OH (index) is in the range of 0.8 to 1.4. Here, when the index is less than 0.8, properties such as water-stopping property or permanent distortion of the obtained polyurethane foam are lowered, and when it exceeds 1.4, the crosslinking reaction is excessively advanced and the moldability is lowered.

本発明においては、従来の製造方法と同様に、触媒、架橋剤、整泡剤、鎖伸長剤、減粘剤などの添加物を適宜に配合することができる。
本発明において、触媒としては公知のアミン系触媒や有機金属系触媒を用いることができる。具体的には、例えばビス(ジメチルアミノエチル)エーテル、ペンタメチルジエチレントリアミン、N,N−ジメチルシクロヘキシルアミン、N,N−ジメチルエタノールアミン、N,N,N’,N’−テトラメチルヘキサメチレンジアミン、N,N,N’,N’−テトラメチルプロピレンジアミン、N,N,N’,N’−テトラメチルエチレンジアミン、トリエチレンジアミン、N−メチル−N’−(ジメチルアミノ)エチルピペラジン、N−メチルモノフォリン、N−エチルモノフォリン、トリエチルアミン、ラウリン酸錫、オクタン酸錫が挙げられる。この触媒の添加量は、ポリオール成分100重量部に対して一般に0.01〜5重量部程度が好ましい。
In the present invention, additives such as a catalyst, a crosslinking agent, a foam stabilizer, a chain extender, and a viscosity reducing agent can be appropriately blended as in the conventional production method.
In the present invention, a known amine catalyst or organometallic catalyst can be used as the catalyst. Specifically, for example, bis (dimethylaminoethyl) ether, pentamethyldiethylenetriamine, N, N-dimethylcyclohexylamine, N, N-dimethylethanolamine, N, N, N ′, N′-tetramethylhexamethylenediamine, N, N, N ′, N′-tetramethylpropylenediamine, N, N, N ′, N′-tetramethylethylenediamine, triethylenediamine, N-methyl-N ′-(dimethylamino) ethylpiperazine, N-methylmono Forin, N-ethylmonoforin, triethylamine, tin laurate, and tin octoate are mentioned. The amount of the catalyst added is generally preferably about 0.01 to 5 parts by weight with respect to 100 parts by weight of the polyol component.

本発明において、架橋剤としては、比較的低分子量のものが用いられる。例えばジオールやトリオール、多価アミン、又はこれらにエチレンオキシド、プロピレンオキシドを付加したもの、トリエタノールアミン、ジエタノールアミンなどを用いることができる。架橋剤の添加量は、ポリオール成分100重量部に対して一般に0〜20重量部程度が好ましい。整泡剤としては、一般に用いられているシリコーン系整泡剤を適宜用いることができる。なお、ポリウレタンフォームに要求される性能に応じて、難燃剤、充填材、帯電防止剤、着色剤、安定剤などを必要に応じて本発明の目的を逸脱しない範囲で添加することができる。   In the present invention, a crosslinking agent having a relatively low molecular weight is used. For example, diol, triol, polyvalent amine, those obtained by adding ethylene oxide or propylene oxide, triethanolamine, diethanolamine, or the like can be used. The addition amount of the crosslinking agent is generally preferably about 0 to 20 parts by weight with respect to 100 parts by weight of the polyol component. As the foam stabilizer, a commonly used silicone foam stabilizer can be used as appropriate. In addition, according to the performance requested | required of a polyurethane foam, a flame retardant, a filler, an antistatic agent, a coloring agent, a stabilizer, etc. can be added in the range which does not deviate from the objective of this invention as needed.

本発明において、独泡ウレタンの接触角を90度以上のウレタン、つまり疎水性ウレタンにする方法としては、例えば疎水性オイルの添加として、アスファルト、粘着付与樹脂、石油樹脂、ポリブテン、ワックスなどの疎水性防水付与材を添加する方法や、疎水性ポリオールとしてオレフィン系ポリオール、ポリブタジエン系ポリオールやダイマー酸系ポリオール、ひまし油系ポリオールのような分子骨格が主に炭素と水素から成る疎水性ポリオールを用いる方法、整泡剤として分子中にOH基、アミノ基などのイソシアナートと反応する官能基を有するシリコーン化合物や官能基を持たないシリコーンオイル、あるいはフッ素系整泡剤などを用いる方法、イソシアナートとしてジフェニルメタンジイソシアナートのような芳香環を多く有するイソシアナートを大量に用いる方法などが挙げられる。   In the present invention, as a method of making the urethane foam contact angle 90 ° or more, that is, a hydrophobic urethane, for example, as hydrophobic oil addition, hydrophobicity such as asphalt, tackifying resin, petroleum resin, polybutene, wax, etc. A method for adding a water-resistant waterproofing material, a method using a hydrophobic polyol mainly composed of carbon and hydrogen, such as an olefinic polyol, a polybutadiene-based polyol, a dimer acid-based polyol, or a castor oil-based polyol as a hydrophobic polyol, As a foam stabilizer, a method using a silicone compound having a functional group that reacts with an isocyanate such as OH group or amino group in the molecule, a silicone oil having no functional group, or a fluorine foam stabilizer, or diphenylmethane diisocyanate as an isocyanate. Has many aromatic rings such as isocyanate Such as a method of using an isocyanate in large quantities, and the like.

本発明において、熱膨張性マイクロカプセルは、加熱することで膨張する液体や気体で、例えばプロパン、ブタン、ノルマルブタン、イソブタン、イソペンタン、ノルマルペンタン、ヘキサン、メチレンクロライド、フロン類などを合成樹脂カプセルに内包させたものである。合成樹脂の種類は、アクリルニトリル、アクリル酸エステル、メタクリル酸エステル、スチレン、酢酸ビニル、塩化ビニリデンなどの共重合体である。それ以外に、発泡ビーズとして知られているスチレン樹脂に炭酸ガスを含浸したスチレンビーズやポリプロピレンビーズ、ポリエチレンビーズなども膨張性マイクロカプセルとして好適である。
補助発泡剤としては、通常のウレタンフォームを製造する時に用いる発泡剤で、水や低沸点炭化水素、フッ素系化合物、塩素系化合物など揮発性の有機化合物などを併用すると低密度発泡体を安定して製造するのに好ましい。
In the present invention, the thermally expandable microcapsule is a liquid or gas that expands when heated.For example, propane, butane, normal butane, isobutane, isopentane, normal pentane, hexane, methylene chloride, chlorofluorocarbons, etc. are used as synthetic resin capsules. It is included. The kind of synthetic resin is a copolymer such as acrylonitrile, acrylic acid ester, methacrylic acid ester, styrene, vinyl acetate, and vinylidene chloride. In addition, styrene beads, polypropylene beads, polyethylene beads and the like in which carbon dioxide gas is impregnated with styrene resin known as foam beads are also suitable as the expandable microcapsules.
The auxiliary foaming agent is a foaming agent used in the production of ordinary urethane foam. When used in combination with volatile organic compounds such as water, low-boiling hydrocarbons, fluorine-based compounds, and chlorine-based compounds, the low-density foam is stabilized. Is preferable.

本発明において、熱膨張性マイクロカプセルを配合した液状ウレタン原料を離型性基材の少なくとも片面にシート状に塗布する方法としては、離型性基材として、紙やポリエステルフィルムの表面にシリコーン樹脂をコーティングしたものや、ポリプロピレンやポリメチルペンテンのようにそれ自体が離型性を持った樹脂のフィルムの上にコーティング法により塗布するものである。
液状ウレタン原料を塗布する方法としては、例えばロールコーターやナイフコーター、ダイスコーター、スプレーコーターが好適な手段として挙げられる。
In the present invention, as a method of applying a liquid urethane raw material containing thermally expandable microcapsules in a sheet form on at least one side of a releasable substrate, a silicone resin is applied to the surface of paper or polyester film as a releasable substrate. Or a resin film such as polypropylene or polymethylpentene, which itself has releasability, is applied by a coating method.
As a method of applying the liquid urethane raw material, for example, a roll coater, a knife coater, a die coater, or a spray coater can be cited as a suitable means.

本発明において、独泡ウレタンシートは例えば図1(A)〜(C)に示すように製造する。   In the present invention, the closed-cell urethane sheet is produced, for example, as shown in FIGS.

まず、ポリオール、イソシアネート、触媒、熱膨張性マイクロカプセル及び他の添加剤を混合し、液状ウレタン原料を準備する。次に、図1(A)に示すように、離型性基材としての第1のフィルム1a上に液状ウレタン原料2を均一に塗布する。つづいて、液状ウレタン原料2の上に第2のフィルム1bを載せる(図1(B)参照)。更に、第1・第2のフィルム1a,1bで挟まれた状態の液状ウレタン原料を、オーブンに入れ、60℃〜130℃で均一に加熱する。これにより、発泡と樹脂化が進行し、独泡ウレタンシート3が形成される。なお、熱膨張性マイクロカプセルの加熱が均一でないと、発泡倍率が不均一となり厚みなど寸法が一定しないため、形状の整ったシート状ウレタンフォームが得られない。ひきつづき、第1・第2のフィルム1a,1bに挟まれた状態の独泡ウレタンシート3を取り出した後、第1・第2のフィルム1a,1bを剥離し、上下面にスキン層4が形成された製品を得る(図1(C)参照)。
なお、図1では、第1・第2のフィルム1a,1bを剥離した場合について述べたが、これに限らず、図2に示すように、第2のフィルム1bのみを剥し第1のフィルム1aを残してもよい。この場合、片面にスキン層4を有する独泡ウレタンシート3と第1のフィルム1aの一体品となる。また、本発明は、図示しないが、両面に第1・第2のフィルムを有する独泡ウレタンシートにも及ぶ。
First, a polyol, isocyanate, a catalyst, a thermally expandable microcapsule, and other additives are mixed to prepare a liquid urethane raw material. Next, as shown to FIG. 1 (A), the liquid urethane raw material 2 is apply | coated uniformly on the 1st film 1a as a mold release base material. Subsequently, the second film 1b is placed on the liquid urethane raw material 2 (see FIG. 1B). Further, the liquid urethane raw material sandwiched between the first and second films 1a and 1b is placed in an oven and heated uniformly at 60 ° C to 130 ° C. Thereby, foaming and resinification progress and the closed-cell urethane sheet 3 is formed. If the heat-expandable microcapsules are not uniformly heated, the expansion ratio is not uniform and the thickness and other dimensions are not constant, and thus a well-formed sheet-like urethane foam cannot be obtained. Next, after taking out the closed cell urethane sheet 3 sandwiched between the first and second films 1a and 1b, the first and second films 1a and 1b are peeled off to form the skin layers 4 on the upper and lower surfaces. A finished product is obtained (see FIG. 1C).
In addition, in FIG. 1, although the case where the 1st, 2nd films 1a and 1b were peeled was described, it is not restricted to this, As shown in FIG. 2, only the 2nd film 1b is peeled and the 1st film 1a May be left. In this case, the closed cell urethane sheet 3 having the skin layer 4 on one side is integrated with the first film 1a. Moreover, although this invention is not shown in figure, this invention also extends to the closed-cell urethane sheet which has the 1st and 2nd film on both surfaces.

本発明において、シート状の液状ウレタン原料を加熱により発泡する手段としては、熱膨張性マイクロカプセルを含有したウレタン原液を離型性基材の上に塗布した後、加熱装置に導入して60℃〜130℃に加熱することが挙げられる。これにより、ウレタンの硬化と同時にマイクロカプセルの膨張が進行する。補助発泡剤を用いる場合は、加熱と同時に補助発泡剤による発泡が進行し、マイクロカプセルの膨張がやや遅れて進行する。   In the present invention, as a means for foaming the sheet-like liquid urethane raw material by heating, a urethane stock solution containing thermally expandable microcapsules is applied onto a releasable substrate, and then introduced into a heating device at 60 ° C. Heating to ~ 130 ° C can be mentioned. Thereby, expansion | swelling of a microcapsule progresses simultaneously with hardening of urethane. When the auxiliary foaming agent is used, foaming by the auxiliary foaming agent proceeds simultaneously with heating, and the expansion of the microcapsules proceeds with a slight delay.

以下、本発明の具体的な実施例について説明する。なお、本実施形態は下記に述べることに限定されない。また、文中、「部」は質量基準であるものとする。
(実施例1)
まず、ダイマー酸ポリエステルポリオール(DIC社製、分子量1300で水酸基価120のダイマー酸とジエチレングリコールからなるポリエステルポリオール)100部、水0.9部、シリコーン整泡剤(信越化学社製の商品名:NP−405)1部、スタノクトSO(錫系触媒)0.3部、イソシアナート末端プレポリマー(日本ポリウレタン社製DC5600、分子量600のポリプロピレングリコールとMDIからなるプレポリマー)112部よりなる液状ウレタン原料に、膨張マイクロカプセル(日本フィライト社製の商品名:エクスパンセルDU40、膨張マイクロカプセル)10部を配合して液温35℃にて撹拌した。次に、このマイクロカプセルを配合した液状ウレタン原料を、ポリエステル系離型フィルム上に1.8mmの隙間を設けたナイフコーターを用いコーティングした。次に、加熱オーブン中で70℃,3.5分加熱後、130℃で6.5分加熱した後、シート状ウレタン製品を離型フィルムから剥離した。得られた製品の接触角は95度で、密度0.0955g/cm、独泡率13%、厚み約10mmの極めて平滑な表面を持った製品であった。また、引張強さは196kPa,伸びは120%,透湿性は1.3gで止水性は160mmであった。
Hereinafter, specific examples of the present invention will be described. Note that the present embodiment is not limited to the following description. In the text, “part” is based on mass.
Example 1
First, dimer acid polyester polyol (manufactured by DIC, 100 parts of a polyester polyol composed of dimer acid having a molecular weight of 1300 and a hydroxyl value of 120 and diethylene glycol), 0.9 part of water, a silicone foam stabilizer (trade name: NP manufactured by Shin-Etsu Chemical Co., Ltd.) -405) Liquid urethane raw material consisting of 1 part, 0.3 part of stanoct SO (tin-based catalyst), 112 parts of isocyanate-terminated prepolymer (DC5600 made by Nippon Polyurethane, prepolymer consisting of polypropylene glycol and MDI having a molecular weight of 600) , 10 parts of expanded microcapsules (trade name: Expancel DU40, expanded microcapsules manufactured by Nippon Philite Co., Ltd.) were mixed and stirred at a liquid temperature of 35 ° C. Next, the liquid urethane raw material blended with the microcapsules was coated using a knife coater provided with a 1.8 mm gap on a polyester release film. Next, after heating at 70 ° C. for 3.5 minutes in a heating oven and then heating at 130 ° C. for 6.5 minutes, the sheet-like urethane product was peeled from the release film. The obtained product had a contact angle of 95 degrees, a density of 0.0955 g / cm 3 , a closed cell ratio of 13% and a thickness of about 10 mm and a very smooth surface. In addition, the tensile strength was 196 kPa, the elongation was 120%, the moisture permeability was 1.3 g, and the water stopping property was 160 mm.

(実施例2)
実施例1におけるダイマー酸ポリエステルポリオールを、水酸基価80に変更し、イソシアナート末端プレポリマーを81.7部に変更した以外は、実施例1と同じしてシート状ウレタンを作製した。得られた製品の接触角は95度で、密度0.0925g/cm,独泡率15%で、厚み約10mmの極めて平滑な表面を持った製品であった。また、引張強さは181kPa、伸び140%、透湿性1.3gで、止水性は160mmであった。
(Example 2)
A sheet-like urethane was prepared in the same manner as in Example 1 except that the dimer acid polyester polyol in Example 1 was changed to a hydroxyl value of 80 and the isocyanate-terminated prepolymer was changed to 81.7 parts. The obtained product had a contact angle of 95 degrees, a density of 0.0925 g / cm 3 , a closed cell ratio of 15%, and a very smooth surface having a thickness of about 10 mm. Further, the tensile strength was 181 kPa, the elongation was 140%, the moisture permeability was 1.3 g, and the waterstop was 160 mm.

(比較例1)
まず、エクセノール4600(旭硝子社製の商品名、分子量5000で水酸基価34.5のポリプロピレングリコール)100部、FTR1600(三井化学社製の商品名で石油樹脂)15部、水2.0部、NP−405(信越化学社製の商品名でシリコーン整泡剤)1部、スタノクトSO(錫系触媒)0.3部、T65(日本ポリウレタン社製の商品名でトルエンジイソシアナート)25.9部よりなる液体原料を液温35℃にて攪拌した。次に、この液状ウレタン原料をポリエステル系離型フィルム上に1.8mmの隙間を設けたナイフコーターを用いてコーティングした。つづいて、加熱オーブン中で70℃,3.5分加熱し、更に130℃で6.5分加熱した後、独泡ウレタンシート(シート状ウレタン製品)を離型フィルムから剥離した。得られた製品の接触角は95度で、密度0.094g/cm、独泡率0%、厚み約10mmの極めて平滑な表面を持った製品であった。なお、引張強さは113kPa、伸びは120%、透湿性は4.5gで、止水性は70mmであった。
(Comparative Example 1)
First, 100 parts of Exenol 4600 (trade name manufactured by Asahi Glass Co., Ltd., polypropylene glycol having a molecular weight of 5000 and a hydroxyl value of 34.5), 15 parts of FTR 1600 (petroleum resin under the trade name of Mitsui Chemicals), 2.0 parts of water, NP -405 (silicone foam stabilizer under the trade name of Shin-Etsu Chemical Co., Ltd.), 0.3 part of stanoct SO (tin-based catalyst), T65 (toluene diisocyanate under the trade name of Nippon Polyurethane) 25.9 parts The liquid raw material was stirred at a liquid temperature of 35 ° C. Next, this liquid urethane raw material was coated on a polyester release film using a knife coater having a gap of 1.8 mm. Subsequently, after heating in a heating oven at 70 ° C. for 3.5 minutes and further at 130 ° C. for 6.5 minutes, the closed cell urethane sheet (sheet-like urethane product) was peeled from the release film. The obtained product had a contact angle of 95 degrees, a density of 0.094 g / cm 3 , a closed cell rate of 0%, and a thickness of about 10 mm and a very smooth surface. The tensile strength was 113 kPa, the elongation was 120%, the moisture permeability was 4.5 g, and the water stoppage was 70 mm.

(比較例2)
まず、テスラック2456(日立化成ポリオール社製の商品名、分子量1000で、水酸基価130、ダイマー酸とジエチレングリコールからなるポリエステルポリオール)100部、水1.6部、NP−405(信越化学社製の商品名でシリコーン整泡剤)1部、DABCO−33LV(日本乳化剤社製の商品名でアミン触媒)0.2部、スタノクトSO(錫系触媒)0.26部、イソシアナート末端プレポリマー(前述のダイマー酸ポリオールとT65よりなる、NCO%=30)60.2部よりなる液状ウレタン原料を液温35℃にて攪拌した。次に、この液状ウレタン原料をポリエステル系離型フィルム上に1.8mmの隙間を設けたナイフコーターを用いてコーティングした。つづいて、加熱オーブン中で70℃,3.5分加熱し、更に130℃で6.5分加熱した後、シート状ウレタン製品を離型フィルムから剥離した。得られた製品の接触角は98度で、密度0.091g/cm、独泡率0%の厚み約10mmの極めて平滑な表面を持った製品であった。なお、引張強さは147kPa、伸びは110%で、透湿性は3.4gで、止水性は70mmであった。
(Comparative Example 2)
First, Teslac 2456 (trade name, manufactured by Hitachi Chemical Polyol Co., Ltd., molecular weight 1000, hydroxyl value 130, polyester polyol composed of dimer acid and diethylene glycol) 100 parts, water 1.6 parts, NP-405 (product manufactured by Shin-Etsu Chemical Co., Ltd.) 1 part of silicone foam stabilizer), 0.2 part of DABCO-33LV (Amine catalyst under the trade name made by Nippon Emulsifier Co., Ltd.), 0.26 part of stannoc SO (tin catalyst), isocyanate-terminated prepolymer (as described above) A liquid urethane raw material consisting of 60.2 parts of NCO% = 30) consisting of dimer acid polyol and T65 was stirred at a liquid temperature of 35 ° C. Next, this liquid urethane raw material was coated on a polyester release film using a knife coater having a gap of 1.8 mm. Subsequently, after heating in a heating oven at 70 ° C. for 3.5 minutes and further at 130 ° C. for 6.5 minutes, the sheet-like urethane product was peeled from the release film. The obtained product had a contact angle of 98 degrees, a density of 0.091 g / cm 3 , a closed cell ratio of 0%, and a thickness of about 10 mm and a very smooth surface. The tensile strength was 147 kPa, the elongation was 110%, the moisture permeability was 3.4 g, and the waterstop was 70 mm.

次に、物性測定方法について述べる。
1)接触角の測定は、得られたウレタンフォームをアルミフォイルではさみ、約200℃で加熱しつつ圧力約50kg/cmにてプレスし薄いフィルム状にして、協和接触角測定機で測定した。
2)独泡率はASTMD2856−70により、サンプルサイズ(25mm×25mm×10mm)の試験片を、東京サイエンス社製のベックマン空気比較式比重計にて独泡率を測定した。
Next, a method for measuring physical properties will be described.
1) The contact angle was measured by sandwiching the obtained urethane foam with aluminum foil, pressing it at a pressure of about 50 kg / cm 2 while heating at about 200 ° C. to form a thin film, and measuring with a Kyowa contact angle measuring machine. .
2) The closed cell rate was measured by ASTM D2856-70 using a test size of a sample size (25 mm × 25 mm × 10 mm) with a Beckman air comparison hydrometer made by Tokyo Science.

3)透湿性は、サンプルサイズ(外径φ75mm,内径φ35.5mm,厚み10mm)の試験片を標準瓶に50%圧縮してセットし、瓶の中にシリカゲルを約45g正確に秤量し、85℃,湿度85%の高温恒湿槽に24時間放置した後の重量増加量とする。
4)止水性はサンプルサイズ(外径φ60mm,内径60mm,厚み10mm)の試験片をアクリル板に50%圧縮にて圧締し注水し漏れを観察する。24時間ごとに10mmずつ水圧を上げていき漏れた水圧を止水性とする。
3) For the moisture permeability, a test piece of sample size (outer diameter φ75 mm, inner diameter φ35.5 mm, thickness 10 mm) was set in a standard bottle with 50% compression, and about 45 g of silica gel was accurately weighed in the bottle. The weight increase after standing in a high temperature and humidity chamber at 85 ° C. and humidity of 85% for 24 hours.
4) Water-stopping is performed by squeezing a test piece of sample size (outer diameter φ 60 mm, inner diameter 60 mm, thickness 10 mm) onto an acrylic plate with 50% compression and injecting water to observe leakage. The water pressure is increased by 10 mm every 24 hours and the leaked water pressure is regarded as water-stopping.

下記表1は、上記実施例1,2及び比較例1,2は、マイクロカプセル,水の配合量及び得られた製品の物性値を示す。

Figure 2010235805
In Table 1 below, Examples 1 and 2 and Comparative Examples 1 and 2 show the microcapsules, the blending amount of water, and the physical properties of the obtained products.
Figure 2010235805

なお、本発明は、上記実施形態そのままに限定されるものではなく、実施段階ではその要旨を逸脱しない範囲で構成要素を変形して具体化できる。また、上記実施形態に開示されている複数の構成要素の適宜な組み合せにより種々の発明を形成できる。例えば、実施形態に示される全構成要素から幾つかの構成要素を削除してもよい。更に、異なる実施形態に亘る構成要素を適宜組み合せてもよい。   Note that the present invention is not limited to the above-described embodiment as it is, and can be embodied by modifying the constituent elements without departing from the scope of the invention in the implementation stage. Further, various inventions can be formed by appropriately combining a plurality of constituent elements disclosed in the embodiment. For example, some components may be deleted from all the components shown in the embodiment. Furthermore, you may combine suitably the component covering different embodiment.

1a…第1のフィルム(離型性基材)、1b…第2のフィルム(離型性基材)、2…液状ウレタン原料、3…独泡ウレタンシート、4…スキン層。   DESCRIPTION OF SYMBOLS 1a ... 1st film (mold release base material), 1b ... 2nd film (mold release base material), 2 ... Liquid urethane raw material, 3 ... Self-foaming urethane sheet, 4 ... Skin layer.

Claims (2)

液状ウレタン原料に熱膨張マイクロカプセルを配合してなる、シーリング材として利用される独泡ウレタンシートであり、
前記液状ウレタン原料がダイマー酸系ポリオール及び低分子量グリコールとイソシアナートの反応生成物であるイソシアナート末端ウレタンプレポリマーよりなり、独泡ウレタンの接触角が90度以上であることを特徴とする独泡ウレタンシート。
It is a closed-cell urethane sheet used as a sealing material, which is made by blending thermally expanded microcapsules with a liquid urethane material.
The liquid foam raw material is composed of an isocyanate-terminated urethane prepolymer which is a reaction product of a dimer acid polyol and a low molecular weight glycol and an isocyanate, and the contact angle of the closed cell urethane is 90 degrees or more. Urethane sheet.
ダイマー酸系ポリオール及び低分子量グリコールとイソシアナートの反応生成物であるイソシアナート末端ウレタンプレポリマーよりなる液状ウレタン原料と、熱膨張マイクロカプセルを配合する工程と、この熱膨張マイクロカプセルを配合したウレタン原料を、離型性基材の少なくとも片側にシート状に塗布する工程と、シート状の液状ウレタン原料を加熱により発泡させて硬化し、ウレタンシートを形成する工程を具備することを特徴とする独泡ウレタンシートの製造方法。 Liquid urethane raw material composed of isocyanate-terminated urethane prepolymer which is a reaction product of dimer acid polyol and low molecular weight glycol and isocyanate, a step of blending thermal expansion microcapsules, and a urethane raw material blending these thermal expansion microcapsules And a step of applying a sheet on at least one side of the releasable substrate and a step of foaming and curing the sheet-like liquid urethane raw material by heating to form a urethane sheet. A method for producing a urethane sheet.
JP2009086071A 2008-07-31 2009-03-31 Self-foaming urethane sheet and method for producing the same Active JP5636164B2 (en)

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US12/511,356 US20100028650A1 (en) 2008-07-31 2009-07-29 Closed-cell urethane sheet, manufacturing method thereof and waterproof sealing materials

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JP2011157452A (en) * 2010-01-29 2011-08-18 Nhk Spring Co Ltd Closed-cell urethane sheet and method for producing the same
JP2011213924A (en) * 2010-03-31 2011-10-27 Nhk Spring Co Ltd Foamed polyurethane sheet
JP2013018897A (en) * 2011-07-13 2013-01-31 Nhk Spring Co Ltd Sheet-like polyurethane foam and method for producing the same
WO2019069802A1 (en) * 2017-10-05 2019-04-11 三井化学株式会社 Polyurethane resin, molded article, and method for producing polyurethane resin

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JP2001352156A (en) * 2000-06-07 2001-12-21 Asahi Rubber:Kk Formed polyurethane for electronic component and method for manufacturing electronic component coated therewith
JP2002037829A (en) * 2000-07-27 2002-02-06 Toyo Quality One Corp Self-adhesive foam
JP2002327039A (en) * 2001-05-02 2002-11-15 Yokohama Rubber Co Ltd:The Heat-curable urethane composition
JP2003205963A (en) * 2001-11-06 2003-07-22 Toyo Seikan Kaisha Ltd Sealant for cap
JP2004107414A (en) * 2002-09-17 2004-04-08 Mitsui Chemicals Inc Urethane sealant corresponding to recycling
JP2004359760A (en) * 2003-06-03 2004-12-24 Toyo Seikan Kaisha Ltd Sealing material for lid and lid using the same
JP2006282819A (en) * 2005-03-31 2006-10-19 Nhk Spring Co Ltd Water stop material comprising polyurethane foam
JP2008133395A (en) * 2006-11-29 2008-06-12 Yokohama Rubber Co Ltd:The Urethane adhesive composition
JP2009173806A (en) * 2008-01-25 2009-08-06 Bridgestone Corp Water-cut-off polyurethane foam
JP2009256522A (en) * 2008-04-19 2009-11-05 Nitto Denko Corp Heat-peelable type adhesive sheet
JP2010037353A (en) * 2008-07-31 2010-02-18 Nhk Spring Co Ltd Method of manufacturing closed-cell urethane sheet, and waterproof sealing material
JP2010202754A (en) * 2009-03-03 2010-09-16 Achilles Corp Water cut-off polyurethane foam

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011157452A (en) * 2010-01-29 2011-08-18 Nhk Spring Co Ltd Closed-cell urethane sheet and method for producing the same
JP2011213924A (en) * 2010-03-31 2011-10-27 Nhk Spring Co Ltd Foamed polyurethane sheet
JP2013018897A (en) * 2011-07-13 2013-01-31 Nhk Spring Co Ltd Sheet-like polyurethane foam and method for producing the same
WO2019069802A1 (en) * 2017-10-05 2019-04-11 三井化学株式会社 Polyurethane resin, molded article, and method for producing polyurethane resin

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