JP2014065810A - Manufacturing method of bubble-enclosed adhesive tape or sheet - Google Patents

Manufacturing method of bubble-enclosed adhesive tape or sheet Download PDF

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JP2014065810A
JP2014065810A JP2012211620A JP2012211620A JP2014065810A JP 2014065810 A JP2014065810 A JP 2014065810A JP 2012211620 A JP2012211620 A JP 2012211620A JP 2012211620 A JP2012211620 A JP 2012211620A JP 2014065810 A JP2014065810 A JP 2014065810A
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pressure
sensitive adhesive
bubble
manufacturing
mpa
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Hiromi Matsushita
洋己 松下
Hiroko Mori
裕子 森
Shinya Takeda
慎也 竹田
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Nichiban Co Ltd
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Nichiban Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a manufacturing method of a bubble-enclosed adhesive tape or sheet capable of realizing large bubble diameters regardless of types of substrates and enabling the verification of a homogeneously foamed state even when magnified by 100 times.SOLUTION: The provided manufacturing method of a bubble-enclosed adhesive tape or sheet is a method for manufacturing a bubble-enclosed adhesive tape or sheet wherein a bubble-enclosed tackifier layer is formed on at least one side of a substrate and comprises a melting step of heating and melting a tackifier raw ingredient including a thermoplastic resin till the melt viscosity thereof reaches 5000-200000 mPa s, a mixing step of adding 25-80 parts.vol. of a component gaseous at normal temperature and normal pressure to 100 parts.vol. of the tackifier raw ingredient melted and mixing within an environment wherein the liquid pressure is maintained at 3-10 MPa, and a pressure release step of forming, upon the completion of the mixing step, bubbles within the tackifier layer by releasing the pressure impressed onto the tackifier raw ingredient.

Description

本発明は、気泡入り粘着テープ及びシートの製造方法に関する。   The present invention relates to a foamed adhesive tape and a method for producing a sheet.

従来より、粘着テープ及びシートの製造に際し、粘着剤層に微細な独立気泡を含有させることによって、粘着特性(特に初期粘着力や粗面への接着性)を向上させ、更には、粘着剤の使用量を低減することによりコストダウンを実現する手法が提案されている。   Conventionally, in the production of pressure-sensitive adhesive tapes and sheets, the pressure-sensitive adhesive layer contains fine closed cells to improve the pressure-sensitive adhesive properties (particularly the initial pressure-sensitive adhesive force and the adhesiveness to the rough surface). There has been proposed a method for realizing cost reduction by reducing the amount of use.

ここで、特許文献1及び2には、熱分解型発泡剤を粘着剤層中に含有させ、これを加熱発泡させる方法が提案されている。また、特許文献3には、気化性物質(例えば水)を基材に含有させ、これをガス化させて粘着剤層中に独立気泡を形成する方法が提案されている。更には、特許文献4及び5には、ホットメルト熱プラスチック接着剤内にガスを混入し、当該混合物を加圧した後、圧力を開放し、粘着剤内に気泡を形成させる手法、粘着剤層を少なくともその一面に形成してなる粘着シートを、圧力5〜200kg/cmのガス雰囲気内に置いて、当該粘着剤層に該雰囲気ガスを加圧下に溶解させた後、圧力を解放する手法、がそれぞれ提案されている。 Here, Patent Documents 1 and 2 propose a method in which a heat decomposable foaming agent is contained in an adhesive layer and this is heated and foamed. Patent Document 3 proposes a method in which a vaporizable substance (for example, water) is contained in a base material and gasified to form closed cells in the pressure-sensitive adhesive layer. Further, Patent Documents 4 and 5 describe a method in which a gas is mixed in a hot-melt thermoplastic adhesive, the mixture is pressurized, then the pressure is released, and bubbles are formed in the adhesive. A method in which a pressure-sensitive adhesive sheet formed on at least one surface thereof is placed in a gas atmosphere at a pressure of 5 to 200 kg / cm 2 , the atmospheric gas is dissolved in the pressure-sensitive adhesive layer under pressure, and then the pressure is released. Have been proposed.

特開昭62−263278号公報JP-A-62-263278 特公昭64−6678号公報Japanese Patent Publication No. 64-6678 特公平2−27705号公報Japanese Patent Publication No. 2-27705 特開昭53−17645号公報JP-A-53-17645 特開平08−199125号公報Japanese Patent Laid-Open No. 08-199125

ここで、特許文献1及び2の手法によると、得られる気泡の直径(以下、気泡径という)が小さく、十分な発泡倍率が得られないという課題がある。また、特許文献3の手法によると、得られる気泡径は大きいものの、基材の種類が不織布等の気化性物質を含有可能なものに限定されてしまう等という課題がある。例えば、プラスチックフィルムに関しては、水を含むことができないため、そもそも水蒸気発泡は不可能である。また、織布に関しては、縦横に織り込まれた糸の部分に水を吸収できるため水蒸気発泡は可能であるが、逆に、糸の部分のみしか気泡が生成しないという欠点がある。その他にも、気泡が一方の粘着剤の表層部に偏在する傾向が強いため、均一に粘着剤全体を発泡させることが難しく、特に、粘着剤厚が厚くなるほどその傾向は顕著になる。更には、特許文献4及び5の手法によれば、圧力室内での加圧と圧の開放が必要で、バッチ式であり、連続式ではないという欠点がある。特に、特許文献4は圧力が小さく、粘着剤では満足に発泡させることが出来ないという欠点がある。また、特許文献5の方法によると、粘着剤の表層部に気泡が集中し、粘着剤の内部ではほとんど気泡が生じないという不具合を生じやすい欠点がある。そこで、本発明は、基材の種類を問わず大きい気泡径及び高い発泡倍率を実現でき、100倍に拡大しても粘着剤内部にて均一に発泡している状態が確認可能な、気泡入り粘着テープ又はシートの製造方法(特に、連続生産可能な製造方法)を提供することを目的とする。   Here, according to the methods of Patent Documents 1 and 2, there is a problem that the diameter of the obtained bubbles (hereinafter referred to as the bubble diameter) is small, and a sufficient expansion ratio cannot be obtained. Further, according to the technique of Patent Document 3, there is a problem that, although the bubble diameter obtained is large, the type of the substrate is limited to those capable of containing a vaporizable substance such as a nonwoven fabric. For example, regarding a plastic film, since water cannot be contained, steam foaming is impossible in the first place. In addition, with regard to the woven fabric, water can be absorbed into the portion of the yarn woven in the vertical and horizontal directions, so that water vapor foaming is possible, but conversely, there is a drawback that bubbles are generated only in the portion of the yarn. In addition, since bubbles tend to be unevenly distributed in the surface layer portion of one pressure-sensitive adhesive, it is difficult to uniformly foam the entire pressure-sensitive adhesive, and the tendency becomes more remarkable as the pressure-sensitive adhesive thickness increases. Furthermore, according to the methods of Patent Documents 4 and 5, there is a drawback that it is necessary to pressurize and release the pressure in the pressure chamber, which is a batch type and not a continuous type. In particular, Patent Document 4 has a drawback that the pressure is small and the pressure-sensitive adhesive cannot be foamed satisfactorily. Further, according to the method of Patent Document 5, bubbles are concentrated on the surface layer portion of the pressure-sensitive adhesive, and there is a drawback that a problem that bubbles are hardly generated inside the pressure-sensitive adhesive is likely to occur. Therefore, the present invention can realize a large bubble diameter and a high expansion ratio regardless of the type of base material, and can be confirmed to be uniformly foamed inside the pressure-sensitive adhesive even when enlarged to 100 times. It aims at providing the manufacturing method (especially manufacturing method which can be continuously produced) of an adhesive tape or a sheet | seat.

本発明は、
基材の少なくとも一方に気泡入り粘着剤層が形成された気泡入り粘着シート又はテープの製造方法において、
熱可塑性樹脂を含む粘着剤原料を加熱し、溶融粘度が5000〜200000mPa・sとなるまで溶融させる溶融工程と、
液圧が3〜10MPaに維持された環境下、溶融した粘着剤原料100容量部に対し、常温及び常圧で気体である成分25〜80容量部を添加して混練する混合工程と、
混合工程後、粘着剤原料に印加された圧力を開放し、粘着剤層中に気泡を形成させる圧力開放工程と
を含むことを特徴とする、気泡入り粘着剤の製造方法である。
The present invention
In the method for producing a foamed pressure-sensitive adhesive sheet or tape in which a foamed pressure-sensitive adhesive layer is formed on at least one of the substrates,
A melting step in which a pressure-sensitive adhesive material containing a thermoplastic resin is heated and melted until the melt viscosity becomes 5000 to 200000 mPa · s;
In an environment where the liquid pressure is maintained at 3 to 10 MPa, a mixing step of adding and kneading 25 to 80 parts by volume of a gaseous component at normal temperature and normal pressure with respect to 100 parts by volume of the pressure-sensitive adhesive raw material,
After the mixing step, the pressure applied to the pressure-sensitive adhesive raw material is released, and a pressure release step of forming bubbles in the pressure-sensitive adhesive layer is included.

ここで、粘着剤原料が、スチレン系エラストマー及び粘着付与樹脂を含むものであってもよい(即ち、気泡入り粘着シート又はテープが、スチレン系ホットメルト型粘着シート又はテープであってもよい)。また、基材はプラスチックフィルム、織布及び不織布からなるものであってもよい。更に、溶融粘度が10000〜100000mPa・sであってもよい。   Here, the pressure-sensitive adhesive material may include a styrene-based elastomer and a tackifier resin (that is, the bubble-containing pressure-sensitive adhesive sheet or tape may be a styrene-based hot-melt pressure-sensitive adhesive sheet or tape). The substrate may be made of a plastic film, a woven fabric, and a non-woven fabric. Further, the melt viscosity may be 10,000 to 100,000 mPa · s.

本発明によれば、基材の種類を問わず大きい気泡径及び高い発泡倍率を実現でき、さらにその気泡が粘着剤中で均一に分散している、連続生産可能な気泡入り粘着テープ又はシートの製造方法を提供することができるという効果を奏する。   According to the present invention, a large bubble diameter and a high expansion ratio can be realized regardless of the type of the substrate, and the bubbles are uniformly dispersed in the pressure-sensitive adhesive. There exists an effect that a manufacturing method can be provided.

図1は、本形態に係る押出機である。FIG. 1 shows an extruder according to this embodiment. 図2は、実施例7に係る気泡入りホットメルト型粘着テープの表面を100倍に拡大した写真である。FIG. 2 is a photograph in which the surface of the hot-melt adhesive tape with bubble according to Example 7 is magnified 100 times. 図3は、水発泡の場合(布基材)の気泡入りホットメルト型粘着テープの表面を100倍に拡大した写真である。FIG. 3 is a photograph in which the surface of a hot-melt pressure-sensitive adhesive tape containing bubbles in the case of water foaming (cloth base material) is magnified 100 times. 図4は、熱分解型化学発泡剤で発泡させた場合(布基材)の気泡入りホットメルト型粘着テープの表面を100倍に拡大した写真である。FIG. 4 is a photograph in which the surface of a hot-melt pressure-sensitive adhesive tape containing bubbles in the case of foaming with a pyrolytic chemical foaming agent (cloth base material) is magnified 100 times. 図5は、実施例9に係る気泡入りホットメルト型粘着テープの表面を100倍に拡大した写真である。FIG. 5 is a photograph in which the surface of the hot-melt adhesive tape with bubble according to Example 9 is magnified 100 times. 図6は、実施例10に係る気泡入りホットメルト型粘着テープの表面を100倍に拡大した写真である。FIG. 6 is a photograph in which the surface of the hot-melt adhesive tape with bubble according to Example 10 is magnified 100 times. 図7は、比較例1に係る気泡入りホットメルト型粘着テープの表面を100倍に拡大した写真である。FIG. 7 is a photograph in which the surface of the hot melt adhesive tape with bubbles according to Comparative Example 1 is magnified 100 times. 図8は、比較例2に係る気泡入りホットメルト型粘着テープの表面を100倍に拡大した写真である。FIG. 8 is a photograph in which the surface of the hot melt adhesive tape with bubbles according to Comparative Example 2 is magnified 100 times.

以下、本発明に係る気泡入り粘着テープ又はシートの製造方法の一形態(ホットメルト型粘着剤の製造方法の一形態)を説明する。尚、本発明は当該形態に限定されるものではなく、溶剤型粘着剤やエマルジョン型粘着剤にも適用可能である。   Hereinafter, an embodiment of a method for producing a foamed pressure-sensitive adhesive tape or sheet according to the present invention (an embodiment of a method for producing a hot-melt adhesive) will be described. In addition, this invention is not limited to the said form, It can apply also to a solvent type adhesive and an emulsion type adhesive.

本形態に係る気泡入りホットメルト型粘着テープ又はシートの製造方法は、
熱可塑性樹脂を含む粘着剤原料を加熱し、溶融粘度が5000〜200000mPa・sとなるまで溶融させる溶融工程と、
液圧が3〜10MPaに維持された環境下、溶融した粘着剤原料100容量部に対し、常温及び常圧で気体である成分25〜80容量部を添加して混練する混合工程と、
混合工程後、粘着剤原料に印加された圧力を開放する圧力開放工程と、
粘着剤原料又は気泡入り粘着剤を、少なくとも基材の一方に適用する積層工程と
を含む。以下、当該製造方法について詳述する。
The method for producing a bubble-containing hot melt pressure-sensitive adhesive tape or sheet according to this embodiment is as follows:
A melting step in which a pressure-sensitive adhesive material containing a thermoplastic resin is heated and melted until the melt viscosity becomes 5000 to 200000 mPa · s;
In an environment where the liquid pressure is maintained at 3 to 10 MPa, a mixing step of adding and kneading 25 to 80 parts by volume of a gaseous component at normal temperature and normal pressure with respect to 100 parts by volume of the pressure-sensitive adhesive raw material,
After the mixing step, a pressure releasing step for releasing the pressure applied to the adhesive raw material,
A laminating step in which the pressure-sensitive adhesive material or the bubble-containing pressure-sensitive adhesive is applied to at least one of the substrates. Hereinafter, the manufacturing method will be described in detail.

≪1.原料≫
<1−1.粘着剤原料>
本形態での製造方法で使用する粘着剤原料は、熱可塑性樹脂を主成分として含む。更に、必要に応じ、他の成分を含有してもよい。以下、各成分及び組成について詳述する。
<< 1. Raw material >>
<1-1. Adhesive raw material>
The pressure-sensitive adhesive raw material used in the production method according to this embodiment contains a thermoplastic resin as a main component. Furthermore, you may contain another component as needed. Hereinafter, each component and composition will be described in detail.

(1−1−1.熱可塑性樹脂)
本形態で使用可能な熱可塑性樹脂は、特に限定されず、例えば、スチレン−イソプレン−スチレンブロック共重合体(SIS)、スチレン−ブチレン−スチレンブロック共重合体(SBS)、スチレン−エチレン/ブチレン−スチレンブロック共重合体(SEBS)、スチレン−エチレン/プロピレン−スチレンブロック共重合体(SEPS)、スチレン−イソプレン/プロピレン−スチレン(SIPS)等のスチレン系エラストマー;ポリエチレン、特に超低密度ポリエチレンやポリプロピレン、エチレン・酢酸ビニル共重合体等のオレフィン系ポリマー;アクリル酸やメタクリル酸等のアルキルエステルを成分とするアクリル系ポリマー;ポリエステル系;ポリアミド系;ウレタン系;等の熱可塑性樹脂を挙げることができる。これらを1種又は2種以上組み合わせて用いてもよい。これらの中では、スチレン系エラストマーを使用することが、粘着特性及び実用性の観点から好ましい。
(1-1-1. Thermoplastic resin)
The thermoplastic resin that can be used in this embodiment is not particularly limited. For example, styrene-isoprene-styrene block copolymer (SIS), styrene-butylene-styrene block copolymer (SBS), styrene-ethylene / butylene- Styrenic elastomers such as styrene block copolymer (SEBS), styrene-ethylene / propylene-styrene block copolymer (SEPS), styrene-isoprene / propylene-styrene (SIPS); polyethylene, particularly ultra-low density polyethylene and polypropylene, Examples include olefin polymers such as ethylene / vinyl acetate copolymers; acrylic polymers containing alkyl esters such as acrylic acid and methacrylic acid as components; polyester systems; polyamide systems; urethane systems; These may be used alone or in combination of two or more. Among these, it is preferable to use a styrene-based elastomer from the viewpoints of adhesive properties and practicality.

(1−1−2.他の成分)
他の成分としては、例えば、粘着付与樹脂、軟化剤、充填剤、顔料、老化防止剤、安定剤等を挙げることができる。ここで、まず、粘着付与樹脂としては、例えば、脂肪族系石油樹脂、クマロンーインデン系樹脂、脂環族系石油樹脂、テルペン系樹脂、テルペンフェノール系樹脂、ロジン樹脂等が挙げられる。これらを1種又は2種以上組み合わせて用いてもよい。また、軟化剤としては、例えば、パラフィン系類、ポリブテン、ポリイソブチレンやテルペン系等の各種オイル類、あるいはそれらの水素添加物や部分水素添加物などが挙げられる。これらを1種又は2種以上組み合わせて用いてもよい。更に、充填剤としては、酸化チタン、酸化鉄等の金属酸化物、タルク、炭酸カルシウム、クレー、カーボンブラック等を挙げることができる。これらを1種又は2種以上組み合わせて用いてもよい。
(1-1-2. Other components)
Examples of other components include tackifier resins, softeners, fillers, pigments, anti-aging agents, stabilizers, and the like. First, examples of the tackifier resin include aliphatic petroleum resins, coumarone-indene resins, alicyclic petroleum resins, terpene resins, terpene phenol resins, and rosin resins. These may be used alone or in combination of two or more. Examples of the softening agent include various oils such as paraffins, polybutenes, polyisobutylenes and terpenes, or hydrogenated products or partially hydrogenated products thereof. These may be used alone or in combination of two or more. Furthermore, examples of the filler include metal oxides such as titanium oxide and iron oxide, talc, calcium carbonate, clay, and carbon black. These may be used alone or in combination of two or more.

(1−1−3.配合量)
まず、熱可塑性樹脂は、例えば、本形態に係る粘着剤原料の全質量を基準として、17〜67質量%含有する。また、粘着付与樹脂は、例えば、本形態に係る粘着剤原料の全質量を基準として、9〜73質量%含有する。更に、軟化剤は、例えば、本形態に係る粘着剤原料の全質量を基準として、2〜61質量%含有する。但し、当該量は前述のようにあくまで本発明の一形態に過ぎず当該範囲には何ら限定されない。
(1-1-3. Compounding amount)
First, a thermoplastic resin contains 17-67 mass% on the basis of the total mass of the adhesive raw material which concerns on this form, for example. Moreover, tackifying resin contains 9-73 mass%, for example on the basis of the total mass of the adhesive raw material which concerns on this form. Furthermore, a softener contains 2-61 mass% on the basis of the total mass of the adhesive raw material which concerns on this form, for example. However, the amount is merely an embodiment of the present invention as described above, and is not limited to the range.

<1−2.常温常圧で気体である成分>
本形態に係る常温及び常圧で気体である成分は、粘着剤原料に溶解可能なガスであれば特に限定されず、例えば、窒素、空気、二酸化炭素等の無機性ガス類、ヘリウム、アルゴン等の希ガス類、プロパン、ブタン、フロン等の有機性ガス類が挙げられる。ここで、常温常圧とは、温度23℃、絶対圧力101325Paを意味する。
<1-2. Ingredients that are gaseous at normal temperature and pressure>
The component that is a gas at normal temperature and normal pressure according to the present embodiment is not particularly limited as long as it is a gas that can be dissolved in the pressure-sensitive adhesive material. For example, inorganic gases such as nitrogen, air, and carbon dioxide, helium, argon, and the like Noble gases and organic gases such as propane, butane and chlorofluorocarbon. Here, the normal temperature and normal pressure mean a temperature of 23 ° C. and an absolute pressure of 101325 Pa.

<1−3.基材>
本形態に係る基材は、特に限定されず、例えば、ポリエチレン、ポリプロピレン、エチレン−酢酸ビニル共重合体、軟質ポリ塩化ビニル、ポリウレタン、ポリエチレンテレフタレート(PET)に代表されるポリエステル等からなる合成樹脂フィルムや、不織布、織布、上質紙、クラフト紙、グラシン紙、コート紙、キャストコート紙、樹脂含浸紙、金属箔ラミネートフィルム、金属蒸着フィルム等が挙げられる。これらを1種又は2種以上、積層あるいはラミネートしてもよい。尚、塗布される粘着剤は高温であるので、基材の軟化点は留意する必要がある。
<1-3. Base material>
The base material according to the present embodiment is not particularly limited. For example, a synthetic resin film made of polyethylene, polypropylene, ethylene-vinyl acetate copolymer, soft polyvinyl chloride, polyurethane, polyester represented by polyethylene terephthalate (PET), or the like. And non-woven fabric, woven fabric, high-quality paper, craft paper, glassine paper, coated paper, cast coated paper, resin-impregnated paper, metal foil laminate film, metal vapor-deposited film and the like. One or more of these may be laminated or laminated. In addition, since the applied adhesive is high temperature, it is necessary to pay attention to the softening point of the substrate.

≪2.プロセス≫
<2−1.装置構成>
図1を参照しながら、本形態で使用し得る押出機を説明する。尚、当該押出機はあくまで一例であり、本発明を限定するものではない。当該押出機Aは、溶融状態の粘着剤原料をストックしておく粘着剤原料タンク1−1と、液化ガス(例えば液化窒素)をストックしておくガスタンク1−2と、粘着剤原料タンク1−1内の溶融状態の粘着剤原料を下流に送るための第一ポンプ2−1と、粘着剤原料とガスとを所定比で混合させるための二軸スクリュー3と、混合体(気体と粘着剤原料との混合体)を下流に定量的に送るための第二ポンプ2−2と、その混合体を吐出するためのヘッド5と、各流体を通すためのライン6と、から構成される。尚、圧力は塗工ヘッド先端部まで保たれている(但し、距離による圧損は除く)。
≪2. Process >>
<2-1. Device configuration>
An extruder that can be used in this embodiment will be described with reference to FIG. In addition, the said extruder is an example to the last, and does not limit this invention. The extruder A includes an adhesive raw material tank 1-1 in which a molten adhesive raw material is stocked, a gas tank 1-2 in which liquefied gas (for example, liquefied nitrogen) is stocked, and an adhesive raw material tank 1- 1, a first pump 2-1 for sending a molten adhesive material in the downstream, a twin screw 3 for mixing the adhesive material and gas at a predetermined ratio, and a mixture (gas and adhesive) A second pump 2-2 for quantitatively sending the mixture with the raw material) downstream, a head 5 for discharging the mixture, and a line 6 for passing each fluid. The pressure is maintained up to the tip of the coating head (however, pressure loss due to distance is excluded).

<2−2.溶融工程>
本形態に係る溶融工程は、熱可塑性樹脂を含む粘着剤原料を加熱し、溶融粘度が5000〜200000mPa・s、好適には5000〜150000mPa・s、より好適には10000〜100000mPa・sとなるまで溶融させる。尚、ここで規定した溶融粘度は、二軸スクリュー3にて気体と混合される直前の粘着剤原料の粘度である。溶融粘度が低いと、発泡させた場合に気泡径が大きくなるため発泡倍率が上昇する傾向があり、溶融粘度が高いと、発泡させた場合に気泡径が小さくなるため発泡倍率が減少する傾向がある。特に、粘度が200000mPa・sを超えた場合には、発泡倍率が著しく低下してしまう。また、粘度が5000mPa・s未満の場合には、溶融した粘着剤中に含有させた気体が抜けやすくなるため、好ましくない。ここで、スチレン系ホットメルト型粘着剤の場合、当該粘度を実現するための好適温度は、140〜230℃であり、より好適には150〜230℃である。ここで、本明細書における「溶融粘度」は、混練温度(図1中の1−1の温度)において、メルター内(図1中の1−1)で完全に溶融した粘着剤の粘度であり、粘度計(ビスコテスタVT−03F、又は、ビスコテスタVT−04F、リオン(株)製)を用いて求められる。
<2-2. Melting process>
In the melting step according to this embodiment, the pressure-sensitive adhesive material containing a thermoplastic resin is heated until the melt viscosity becomes 5000 to 200000 mPa · s, preferably 5000 to 150,000 mPa · s, and more preferably 10000 to 100000 mPa · s. Melt. In addition, the melt viscosity prescribed | regulated here is a viscosity of the adhesive raw material just before mixing with gas with the twin screw 3. FIG. If the melt viscosity is low, the foam diameter tends to increase when the foam is expanded, and the expansion ratio tends to increase. If the melt viscosity is high, the foam diameter tends to decrease because the foam diameter becomes small when foamed. is there. In particular, when the viscosity exceeds 200,000 mPa · s, the expansion ratio is remarkably lowered. On the other hand, when the viscosity is less than 5000 mPa · s, the gas contained in the melted pressure-sensitive adhesive tends to escape, which is not preferable. Here, in the case of a styrene-based hot-melt pressure-sensitive adhesive, a suitable temperature for realizing the viscosity is 140 to 230 ° C, and more preferably 150 to 230 ° C. Here, “melt viscosity” in the present specification is the viscosity of the adhesive completely melted in the melter (1-1 in FIG. 1) at the kneading temperature (temperature 1-1 in FIG. 1). And a viscometer (Viscotester VT-03F or Viscotester VT-04F, manufactured by Rion Co., Ltd.).

<2−3.混合工程>
本形態に係る混合工程は、系(2−1と2−2の経路内)の圧力(液圧)が3〜10MPa(好適には5〜7MPa)に維持された環境下、二軸スクリュー3の回転により、粘着剤原料と常温及び常圧で気体である成分とを、溶融した粘着剤原料100容量部に対し、常温及び常圧で気体である成分25〜80容量部(好適には30〜50容量部)を送り込んで混合する工程である。尚、粘着剤原料と常温及び常圧で気体である成分との混合比の調整は、二軸スクリュー3の回転比を変更することで適宜実施し得る。ここで、スチレン系ホットメルト型粘着剤の場合、当該混合工程における好適温度は、140〜230℃である。また、液圧が3MPa未満では装置の系内の圧力と大気圧との差圧が小さく、大きな気泡径を有する気泡が得られず、発泡倍率が低下してしまい、好ましくない。また、10MPaを超えると装置への負荷が大きいため、長時間の連続塗工が難しくなるばかりか最悪装置が破損するおそれがあるため、好ましくない。特に、安定的に塗工するという観点から、7MPa以下で実施することが好ましい。溶融した粘着剤原料100容量部に対し、常温及び常圧で気体である成分が25容量部未満の場合には、気体の量が少なすぎるため発泡倍率が低下するし、80容量部を超えた場合には、気体の量をそれ以上増加させても発泡倍率の変化は非常にわずかであるため非効率である。
<2-3. Mixing process>
The mixing step according to the present embodiment includes a twin screw 3 in an environment in which the pressure (hydraulic pressure) of the system (in the path of 2-1 and 2-2) is maintained at 3 to 10 MPa (preferably 5 to 7 MPa). Rotation of the pressure sensitive adhesive raw material and the component that is gaseous at normal temperature and normal pressure with respect to 100 parts by volume of the molten pressure sensitive adhesive raw material, 25 to 80 parts by volume (preferably 30 parts by volume) of the gaseous component at normal temperature and normal pressure To 50 parts by volume) and mixing. In addition, adjustment of the mixing ratio between the pressure-sensitive adhesive raw material and a component that is a gas at normal temperature and normal pressure can be appropriately performed by changing the rotation ratio of the twin screw 3. Here, in the case of a styrene-based hot melt adhesive, a suitable temperature in the mixing step is 140 to 230 ° C. On the other hand, if the hydraulic pressure is less than 3 MPa, the differential pressure between the pressure in the system of the apparatus and the atmospheric pressure is small, bubbles having a large bubble diameter cannot be obtained, and the expansion ratio is lowered, which is not preferable. On the other hand, if the pressure exceeds 10 MPa, the load on the apparatus is large, so that continuous coating for a long time becomes difficult and the worst apparatus may be damaged. In particular, it is preferable to carry out at 7 MPa or less from the viewpoint of stable coating. When the component that is gaseous at normal temperature and normal pressure is less than 25 parts by volume with respect to 100 parts by volume of the melted adhesive raw material, the amount of gas is too small, and the expansion ratio decreases, and exceeds 80 parts by volume. In some cases, increasing the amount of gas further is inefficient because the change in expansion ratio is very small.

<2−4.圧力開放工程>
本形態に係る圧力開放工程は、二軸スクリュー3で気体を混合したもの(粘着剤原料+常温及び常圧で気体である成分)に印加された圧力を開放する工程である。例示した押出機を使用した場合、高温及び高圧状態にある二軸スクリュー3から第二ポンプ2−2、ヘッド5を介して、気体が溶け込んだ粘着剤原料を押し出すことにより実施する。当該粘着剤原料には、常温常圧で気体である物質に印加された圧力が低下するため、圧力が解放されると、粘着剤内部で発泡し、微細な気泡が形成される。
<2-4. Pressure release process>
The pressure release process according to this embodiment is a process of releasing the pressure applied to the gas mixed with the twin screw 3 (adhesive raw material + component at normal temperature and normal pressure). When the illustrated extruder is used, it is carried out by extruding the adhesive material in which the gas is dissolved through the second pump 2-2 and the head 5 from the twin screw 3 in a high temperature and high pressure state. In the pressure-sensitive adhesive raw material, the pressure applied to the substance that is a gas at normal temperature and normal pressure is reduced, so that when the pressure is released, foaming occurs inside the pressure-sensitive adhesive and fine bubbles are formed.

<2−4.積層工程>
本形態に係る積層工程は、典型的には、圧力開放工程と同時又は直後に実施する。典型的には、内部が高温・高圧である押出機から、ヘッド5を介して、気体が溶け込んだ粘着剤組成物を基材上に押し出す態様(典型的には面塗工)を挙げることができる。尚、粘着剤を二層にしたり、基材も溶融させておき、粘着剤と基材とを同時に押し出して積層させる共押出法を採用してもよい。また、塗工パターンも特に限定されず、例えば、スロットコート、カーテンコート、フォーム、ビード、ドット、ポーラスコート、スプレー、スパイラルスプレー、糸ゴム用スプレー、サミットスプレー等を挙げることができる。
<2-4. Lamination process>
The lamination process according to this embodiment is typically performed simultaneously with or immediately after the pressure release process. A typical example is an embodiment (typically surface coating) in which an adhesive composition in which a gas is melted is extruded onto a substrate from an extruder having a high temperature and high pressure inside through a head 5. it can. A coextrusion method in which the pressure-sensitive adhesive is made into two layers or the base material is melted and the pressure-sensitive adhesive and the base material are extruded and laminated at the same time may be employed. The coating pattern is not particularly limited, and examples thereof include slot coat, curtain coat, foam, bead, dot, porous coat, spray, spiral spray, thread rubber spray, and summit spray.

ここで、積層後、クーリングロールにて、高温の粘着剤層を冷却することが好適である。当該冷却により、気泡径の過剰な成長を抑制することが可能となる。ここで、スチレン系ホットメルト型粘着剤の場合、クーリングロールの温度を10〜40℃に設定することが好適である。   Here, after lamination, it is preferable to cool the high-temperature pressure-sensitive adhesive layer with a cooling roll. By this cooling, it is possible to suppress excessive growth of the bubble diameter. Here, in the case of a styrene-based hot-melt pressure-sensitive adhesive, it is preferable to set the temperature of the cooling roll to 10 to 40 ° C.

≪3.気泡入り粘着テープ又はシート≫
<3−1.構造>
まず、粘着剤層の厚さは、特に限定されず、例えば、1〜1000μm(好ましくは10〜500μm)程度の範囲から選択することができる。一般的に粘着剤の厚さが薄いほど気泡が抜けやすい傾向があり、発砲させることが難しい。また、基材の厚さは、特に限定されず、例えば、10〜300μm、好ましくは30〜200μm程度の範囲から選択することができる。また、本形態に係る粘着テープ又はシートは、基材の一方の面のみ粘着剤層が形成されていても両面に形成されていてもよい。また、基材層は積層体であってもよい。更には、基材層及び粘着剤層以外の層(例えば、剥離ライナー、プライマー層、他の機能層)が存在していてもよい。
≪3. Foamed adhesive tape or sheet >>
<3-1. Structure>
First, the thickness of an adhesive layer is not specifically limited, For example, it can select from the range of about 1-1000 micrometers (preferably 10-500 micrometers). In general, the thinner the adhesive, the easier it is for bubbles to escape and it is difficult to fire. Moreover, the thickness of a base material is not specifically limited, For example, it can select from the range of about 10-300 micrometers, Preferably about 30-200 micrometers. Moreover, the adhesive tape or sheet which concerns on this form may be formed in both surfaces, even if the adhesive layer is formed only in the one surface of a base material. The base material layer may be a laminate. Furthermore, layers (for example, a release liner, a primer layer, and other functional layers) other than the base material layer and the pressure-sensitive adhesive layer may exist.

<3−2.性質(特に粘着剤層の性質)>
気泡入り粘着テープ又はシートにおける粘着層における発泡倍率は、好適には20〜50%、より好適には25〜50%である。このように発泡倍率が高いため、SUS板、プローリングに対する再剥離性試験にて、残留なくきれいに剥がすことができる。ここで、本明細書での発泡倍率(気泡占有率)は、以下の式により、算出される。
<3-2. Properties (especially properties of the adhesive layer)>
The expansion ratio of the pressure-sensitive adhesive layer in the bubble-containing pressure-sensitive adhesive tape or sheet is preferably 20 to 50%, more preferably 25 to 50%. Thus, since the expansion ratio is high, it can be peeled cleanly without residue in a re-peelability test for SUS plate and proling. Here, the expansion ratio (bubble occupancy) in this specification is calculated by the following equation.

図1に示す装置を用い、表1(粘着剤原料の組成)及び表2に示す条件で、実施例及び比較例に係る気泡入りホットメルト型粘着テープを製造した。ここで、いずれの実施例及び比較例に関しても、熱可塑性樹脂としてはスチレン系熱可塑性樹脂組成物(スチレン−イソプレンブロック共重合体)を用い、ガスとしては窒素を用いた。尚、混練温度はメルター温度(メルター温度:図1中の、「1−1」の温度)である。結果を表2に示す。尚、表2中、「ガス比率」は、溶融した粘着剤原料100容量部に対する、常温及び常圧で気体である成分の容量部(%)である。また、図2は、実施例8に係る気泡入りホットメルト型粘着テープの表面写真であり、図3は、水発泡の場合(布基材)の気泡入りホットメルト型粘着テープの表面写真である。これら図から分かるように、前者は均一に気泡が分布しているのに対し、後者はスフ−モスの周辺のみしか発泡しない。また、図4〜図6から分かるように、実施例に係るホットメルト型粘着テープは、熱分解型化学発泡剤で発泡させた場合と対比し、気泡径が大きいことが分かる。   Using the apparatus shown in FIG. 1, bubbled hot-melt pressure-sensitive adhesive tapes according to Examples and Comparative Examples were produced under the conditions shown in Table 1 (composition of pressure-sensitive adhesive raw material) and Table 2. Here, for any of the examples and comparative examples, a styrene-based thermoplastic resin composition (styrene-isoprene block copolymer) was used as the thermoplastic resin, and nitrogen was used as the gas. The kneading temperature is the melter temperature (melter temperature: the temperature of “1-1” in FIG. 1). The results are shown in Table 2. In Table 2, the “gas ratio” is the volume part (%) of the component that is a gas at normal temperature and normal pressure with respect to 100 parts by volume of the melted adhesive raw material. Moreover, FIG. 2 is a surface photograph of the hot-melt adhesive tape with bubbles according to Example 8, and FIG. 3 is a photograph of the surface of the hot-melt adhesive tape with bubbles in the case of water foaming (cloth base material). . As can be seen from these drawings, bubbles are uniformly distributed in the former, whereas the latter foams only around the smoky moss. Further, as can be seen from FIGS. 4 to 6, it can be seen that the hot-melt pressure-sensitive adhesive tape according to the example has a larger cell diameter as compared with the case of foaming with a pyrolytic chemical foaming agent.

産業上利用可能性Industrial applicability

本発明により、気泡径が大きく、発泡倍率の大きな気泡入り粘着剤の製造が可能になる。本発明を用いて製造された粘着剤は、粗面接着性や低温特性など粘着諸特性に優れることが期待される。


According to the present invention, it is possible to produce a bubble-containing pressure-sensitive adhesive having a large cell diameter and a large expansion ratio. The pressure-sensitive adhesive produced using the present invention is expected to be excellent in various adhesive properties such as rough surface adhesion and low-temperature properties.


Claims (4)

基材の少なくとも一方面上に気泡入り粘着剤層が形成された気泡入り粘着シート又はテープの製造方法において、
熱可塑性樹脂を含む粘着剤原料を加熱し、溶融粘度が5000〜200000mPa・sとなるまで溶融させる溶融工程と、
液圧が3〜10MPaに維持された環境下、溶融した粘着剤原料100容量部に対し、常温及び常圧で気体である成分25〜80容量部を添加して混練する混合工程と、
混合工程後、粘着剤原料に印加された圧力を開放する圧力開放工程と
を含むことを特徴とする、気泡入り粘着剤の製造方法。
In the method for producing a foamed pressure-sensitive adhesive sheet or tape in which a foamed pressure-sensitive adhesive layer is formed on at least one surface of the substrate,
A melting step in which a pressure-sensitive adhesive material containing a thermoplastic resin is heated and melted until the melt viscosity becomes 5000 to 200000 mPa · s;
In an environment where the liquid pressure is maintained at 3 to 10 MPa, a mixing step of adding and kneading 25 to 80 parts by volume of a gaseous component at normal temperature and normal pressure with respect to 100 parts by volume of the pressure-sensitive adhesive raw material,
A method for producing a bubble-containing pressure-sensitive adhesive, comprising a pressure release step of releasing a pressure applied to the pressure-sensitive adhesive material after the mixing step.
粘着剤原料が、スチレン系エラストマー及び粘着付与樹脂を含む、請求項1記載の製造方法。   The manufacturing method of Claim 1 with which an adhesive raw material contains a styrene-type elastomer and tackifying resin. 基材が、プラスチックフィルム、織布及び不織布からなる群より選ばれる1種類又は2種類以上である、請求項1又は2記載の製造方法。   The manufacturing method of Claim 1 or 2 whose base material is 1 type, or 2 or more types chosen from the group which consists of a plastic film, a woven fabric, and a nonwoven fabric. 溶融粘度が10000〜100000mPa・sの範囲である、請求項1〜3のいずれか一項記載の製造方法。   The manufacturing method as described in any one of Claims 1-3 whose melt viscosity is the range of 10,000-100,000 mPa * s.
JP2012211620A 2012-09-26 2012-09-26 Manufacturing method of bubble-enclosed adhesive tape or sheet Pending JP2014065810A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016130283A (en) * 2015-01-13 2016-07-21 ニチバン株式会社 Adhesive tape
US20180210333A1 (en) * 2017-01-24 2018-07-26 Shin-Etsu Chemical Co., Ltd. Method of procuring an agglutinant structure and a method of manufacturing a pellicle including said agglutinant procuring method

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016130283A (en) * 2015-01-13 2016-07-21 ニチバン株式会社 Adhesive tape
US20180210333A1 (en) * 2017-01-24 2018-07-26 Shin-Etsu Chemical Co., Ltd. Method of procuring an agglutinant structure and a method of manufacturing a pellicle including said agglutinant procuring method
CN108345172A (en) * 2017-01-24 2018-07-31 信越化学工业株式会社 The manufacturing method of the forming method of adhesive and pellicle component with the forming method
KR20180087184A (en) * 2017-01-24 2018-08-01 신에쓰 가가꾸 고교 가부시끼가이샤 Method of forming an adhesive and method of producing pellicle using the same
JP2018120053A (en) * 2017-01-24 2018-08-02 信越化学工業株式会社 Adhesive molding method and pellicle production method by the molding method
US10712658B2 (en) 2017-01-24 2020-07-14 Shin-Etsu Chemical Co., Ltd. Method of procuring an agglutinant structure and a method of manufacturing a pellicle including said agglutinant procuring method
KR102408294B1 (en) * 2017-01-24 2022-06-10 신에쓰 가가꾸 고교 가부시끼가이샤 Method of forming an adhesive and method of producing pellicle using the same

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