JP4641616B2 - Method for producing acrylic polymer composition, and pressure-sensitive adhesive sheet for member processing - Google Patents

Method for producing acrylic polymer composition, and pressure-sensitive adhesive sheet for member processing Download PDF

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Publication number
JP4641616B2
JP4641616B2 JP2000383065A JP2000383065A JP4641616B2 JP 4641616 B2 JP4641616 B2 JP 4641616B2 JP 2000383065 A JP2000383065 A JP 2000383065A JP 2000383065 A JP2000383065 A JP 2000383065A JP 4641616 B2 JP4641616 B2 JP 4641616B2
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acrylic polymer
pressure
polymer composition
acrylic
sensitive adhesive
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JP2002179802A (en
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孝幸 山本
友浩 樽野
充宏 金田
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Nitto Denko Corp
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Nitto Denko Corp
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  • Adhesive Tapes (AREA)
  • Polymerisation Methods In General (AREA)
  • Adhesives Or Adhesive Processes (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、接着テープ又はシート用の接着剤などとして有用なアクリル系重合体組成物の製造方法、該アクリル系重合体組成物からなるアクリル系感圧性接着剤組成物、及び各種工業部材の製造に際して使用される部材加工用粘着シートに関する。
【0002】
【従来の技術】
従来,アクリル系感圧性接着剤組成物は、工業的には殆ど溶液重合によって製造される。この重合はラジカル開始剤によって熱的又は放射線的に開始される。溶液重合による方法では、アクリル系感圧性接着剤組成物は(メタ)アクリル酸アルキルエステルを、必要に応じてアクリル酸、スチレン、酢酸ビニル等の改質用単量体と共にトルエン等の有機溶媒中で重合させることにより調製される。
【0003】
しかし、有機溶媒を用いた溶液重合では成長したポリマー鎖の溶媒への連鎖移動が生じ、一般的には高分子量のポリマーを得にくく高い凝集力が得られにくい。また有機溶剤を多量に使用するため省資源、環境衛生などの観点からも好ましくない。
【0004】
一方、通常半導体集積回路の製造は、高純度シリコン単結晶などをスライスしてウエハとした後、ウエハ表面にICなどの所定の回路パターンをエッチング形成して集積回路を組み込み、ついでウエハ裏面を研削機により研削して、ウエハの厚さを100〜600μm程度まで薄くし、最後にダイシングしてチップ化することにより行われている。ここで上記研削時には、ウエハ表面に粘着シート類を貼り付けてウエハの破損を防止し、研削加工を容易にしている。また、上記ダイシング時には、ウエハ裏面側に粘着シート類を貼り付けて、ウエハを接着固定した状態でダイシングし、形成されるチップをフィルム基材側よりニードルで突き上げてピックアップし、ダイパッド上に固定している。
【0005】
このような目的で用いられる粘着シート類は、研削加工やダイシング加工中に剥離しない程度の粘着力が必要である一方、研削加工後やダイシング後のピックアップ時には容易に剥離でき、また半導体ウエハを破損しない程度の低い粘着力であることが要求される。さらに粘着シート類は、ウエハ表面やウエハ裏面に糊残りを生じず、これらの面を汚染しないものであることが望まれる。
【0006】
【発明が解決しようとする課題】
したがって、本発明の目的は、高分子量のポリマーからなり、凝集力及び接着力に優れ、さらに被着体に対して汚染の少ない、しかも有機溶剤を用いることなく調製できるアクリル系重合体組成物の製造方法、該アクリル系重合体組成物からなるアクリル系感圧性接着剤組成物及び部材加工用粘着シートを提供することにある。
【0007】
【課題を解決するための手段】
本発明者らは上記の目的を達成するために鋭意検討した結果、希釈剤に二酸化炭素を用いて重合させて得られる高分子量のポリマーから、安定な乳化又は分散液を調製することにより、凝集力及び接着力に優れ、且つ部材加工用粘着シートへ加工しやすい接着剤組成物が得られることを見出し、本発明を完成した。
【0008】
すなわち、この発明は、単量体として少なくとも(メタ)アクリル酸アルキルエステル及び環状又は非環状の(メタ)アクリルアミドを用い、希釈剤として二酸化炭素を用いて圧力5.7〜40MPa、温度20〜100℃の条件下でラジカル重合させて得られる、重量平均分子量が400,000以上のアクリル系重合体を含むポリマー組成物を、二酸化炭素を含んだ圧力5.7〜40MPaの状態から大気圧下に、前記アクリル系重合体の貧溶媒中へ噴出して、アクリル系重合体の乳化又は分散液を調製することを特徴とする、アクリル系重合体組成物の製造方法を提供する。前記ポリマー組成物は、分子量100,000以下の成分の比率が重合体全体の10重量%以下であるアクリル系重合体を含むのが好ましい。
【0009】
また、本発明は上記の製造方法で得られるアクリル系重合体組成物を提供する。
本発明は、さらに、上記アクリル系重合体組成物で構成された粘着剤層を有する部材加工用粘着シートを提供する。前記部材加工用粘着シートは、例えば半導体ウエハ加工用粘着シートとして用いられる。
なお、本明細書では、上記発明のほか、
希釈剤として二酸化炭素を用いてラジカル重合させて得られる、重量平均分子量が400,000以上のアクリル系重合体を含むポリマー組成物を、前記アクリル系重合体の貧溶媒中へ噴出して、アクリル系重合体の乳化又は分散液を調製することを特徴とするアクリル系重合体組成物の製造方法、についても説明する
【0010】
【発明の実施の形態】
この発明では単量体として(メタ)アクリル酸アルキルエステルが好適に用いられる。(メタ)アクリル酸アルキルエステルには、アルキル基の炭素数が1〜18のアクリル酸アルキルエステル及びメタクリル酸アルキルエステルが含まれる。具体的には、例えば、アクリル酸メチル、アクリル酸エチル、アクリル酸プロピル、アクリル酸ブチル、アクリル酸2−エチルヘキシル、アクリル酸オクチル、メタクリル酸ブチル、メタクリル酸2−エチルヘキシル、メタクリル酸オクチルなどが挙げられる。これらの(メタ)アクリル酸アルキルエステルは単独で又は2種以上を混合して使用できる。
【0011】
単量体としては、上記(メタ)アクリル酸アルキルエステルのみを用いてもよいが、上記(メタ)アクリル酸アルキルエステルを主成分とし、これと共重合可能な他のモノマーを併用してもよい。前記共重合可能なモノマーの代表的な例として、(メタ)アクリル酸、クロトン酸、イタコン酸、マレイン酸、フマル酸等のカルボキシル基含有エチレン性不飽和単量体が挙げられる。カルボキシル基含有エチレン性不飽和単量体の中でも特に好適なのはアクリル酸である。
【0012】
このカルボキシル基含有エチレン性不飽和単量体は重合体に架橋結合を生じされるのに重要な成分である。他の共重合可能なモノマーとしては、酢酸ビニル、スチレン、アクリロニトリル、環状の(メタ)アクリルアミド、非環状のメタアクリルアミドなどのアクリル系感圧性接着剤の改質用モノマーとして知られる各種モノマーのいずれも使用可能である。これらの共重合可能なモノマーの使用量は、前記(メタ)アクリル酸アルキルエステルとを合わせた総モノマー中、50重量%以下とするのが接着特性上好ましい。
【0013】
重合反応は、分解してラジカルを生成させる開始剤の助けによって行うことができ、ラジカル重合に通常用いられる開始剤を使用できる。例を挙げれば、特に40〜100℃の温度で重合する場合には、ジベンゾイルパーオキシド、ジーtert−ブチルパーオキシド、クメンハイドロパーオキシド、ラウロイルパーオキシドなどの有機過酸化物や、2,2′−アゾビスイソブチロニトリル及びアゾビスイソバレロニトリル等が用いられる。また、20〜40℃の温度で重合を行う場合には、二元開始剤(Redox開始剤)が用いられ、例としてジベンゾイルパーオキシドとジメチルアニリンの二元系等が挙げられる。
【0014】
開始剤の使用量は、アクリル系モノマーの重合の際に通常用いられる量でよく、例えば、前記モノマーの総量100重量部に対して、0.005〜10重量部程度、好ましくは0.1〜5重量部程度である。
【0015】
本発明において希釈剤として用いる二酸化炭素の使用量は、前記モノマーの総量100重量部に対して、例えば5〜2000重量部、好ましくは20〜900重量部である。希釈剤としては通常は二酸化炭素のみで充分であるが、必要に応じて混合性の改良などのために少量の有機溶媒を含んでいても良い。
【0016】
重合は、例えば5.7〜40MPa程度の圧力に調整した二酸化炭素中、例えば20〜100℃程度の温度の範囲で行われる。例えば、超臨界状態の二酸化炭素中で重合を行うことができる。重合時間は通常2〜20時間程度(例えば4〜10時間程度)である。重合の圧力、温度は必要に応じて数段階に設定されてもよい。
【0017】
上記のように、希釈剤として二酸化炭素を用いてアクリル系単量体をラジカル重合すると、成長したポリマー鎖の溶媒への連鎖移動反応が生じない。そのため、溶液重合に比べて比較的高分子のポリマー、すなわち重合平均分子量400,000以上(例えば、400,000〜2,000,000)のアクリル系重合体が得られる。また、この方法により、分子量100,000以下の成分の比率が重合体全体の10重量%以下であるアクリル系重合体を得ることができる。このようなポリマーを含むアクリル系感圧性接着剤は高い凝集力を示す。なお、重量平均分子量や分子量分布は、モノマーの種類や割合、重合開始剤の種類や割合、重合温度、重合時間などにより調整できる。ポリマー中の前記低分子量成分含有量は、ゲルパーミュエーションクロマトグラフィ法(GPC法)により求めることができる。
【0018】
本発明ではこうして得られる重量平均分子量が400,000以上のアクリル系重合体を含むポリマー組成物を、該アクリル系重合体の貧溶媒中へ噴出してアクリル系重合体の乳化又は分散液を調製する。貧溶媒としては、ポリマーが不溶の溶媒であればよいが、なかでも水が好ましい。
【0019】
安定な乳化又は分散液を得るため、通常、乳化剤を前記溶媒中に添加する。乳化剤としては、例えば、ラウリル硫酸ナトリウム、ラウリル硫酸アンモニウム、ドデシルベンゼンスルホン酸ナトリウム、ポリオキシエチレンアルキルエーテル硫酸ナトリウム、ポリオキシエチレンアルキルフェニルエーテル硫酸ナトリウムなどのアニオン系乳化剤が挙げられる。また、プロペニル基などを有するラジカル重合性の乳化剤を用いても良い。乳化剤の使用量は、アクリル系重合体100重量部に対して、10重量部以下(例えば0.001重量部〜10重量部)である。乳化剤の使用量が10重量部を超えると、感圧性接着剤の耐水性に好結果が得られにくくなり好ましくない。
【0020】
ポリマー組成物の噴出方法は特に限定されないが、例えば、二酸化炭素を含んだ高圧の状態からダイスなどの口より、大気圧下に放出しながらポリマー不溶の溶媒中へ噴出する方法が挙げられる。
【0021】
こうして得られるアクリル系重合体組成物はそのまま、又は必要に応じて各種の添加剤を添加してアクリル系感圧性接着剤組成物として使用できる。例えば、前記アクリル系重合体を主接着性成分として用い、これに接着特性を調整するため、公知乃至慣用の粘着付与樹脂(例えば、ロジン系樹脂、テルペン系樹脂、石油樹脂、クマロン・インデン樹脂、スチレン系樹脂など)を配合してもよい。また、粘着付与樹脂以外の添加剤として、可塑剤や炭酸カルシウム、微粉末シリカなどの充てん剤、着色剤、紫外線吸収剤などの公知の各種添加剤を配合することもできる。これらの添加剤の使用量は、いずれもアクリル系感圧性接着剤に適用される通常の量でよい。添加剤は、重合前にモノマーと共に添加しても良いし、重合後のポリマー組成物又はこれを噴出して得た乳化又は分散液に添加しても良い。
【0022】
また、アクリル系感圧性接着剤組成物には架橋剤を配合でき、この架橋剤で前記アクリル系重合体を架橋させることにより接着剤として凝集力をさらに大きくすることができる。
【0023】
前記架橋剤には従来公知のものが広く包含されるが、このうちメチル化トリメチロールメラミンなどの多官能性メラミン化合物;ジグリシジルアニリン、グリセリンジグリシジルエーテルなどの多官能性エポキシ化合物などが特に好ましい。多官能性メラミン化合物と多官能性エポキシ化合物とを併用することもできる。架橋剤の使用量は、前記アクリル系重合体100重量部に対して、例えば0.001〜10重量部、好適には0.01〜5重量部の範囲である。
【0024】
また、多官能性イソシアネート化合物の使用も好ましく、このような化合物としては、例えば、トリレンジイソシアネート、ヘキサメチレンジイソシアネート、ポリメチレンポリフェニルイソシアネート、ジフェニルメタンジイソシアネート、ジフェニルメタンジイソシアネートの二重体、トリメチロールプロパンとトリレンジイソシアネートとの反応生成物、トリメチロールプロパンとヘキサメチレンジイソシアネートとの反応生成物、ポリエーテルポリイソシアネート、ポリエステルポリイソシアネートなどが挙げられる。これら化合物の使用量は、前記のアクリル系重合体100重量部に対して、例えば、0.01〜20重量部、好適には0.05〜15重量部の範囲である。
【0025】
本発明の部材加工用粘着シートは、上記のアクリル系感圧性接着剤組成物で構成される接着剤層を有する。この接着剤層は、例えば、上記アクリル系感圧性接着剤組成物を、従来のロールコーターなどを用いた塗工法を用いて薄膜化することにより形成される。部材加工用シートは、例えば、紙、不織布、プラスチックシート、発泡体シートなどの各種基材の片面又は両面に上記接着剤組成物を塗工して、所定厚みの接着剤層を形成した接着テープ、あるいは剥離紙上に上記接着剤組成物を塗工して所定厚みの接着剤層を形成した基材レス接着テープなどの各種形態をとり得る。
【0026】
被着体、基材又は剥離紙などに塗工された接着剤層を形成するアクリル系重合体は、塗工後の乾燥工程やこの工程後の光照射や電子線照射工程などにおいて適宜架橋処理し使用に供してもよい。
【0027】
【発明の効果】
本発明のアクリル系重合体組成物の製造方法によれば、希釈剤としてラジカル連鎖移動のない溶媒である二酸化炭素を使用するため、従来の有機溶剤で合成されるポリマーと比較して、低分子量成分の少ない高分子量のポリマーを含むアクリル系重合体組成物が得られる。
本発明のアクリル系感圧性接着剤組成物は、このようなアクリル系重合体組成物からなるため、凝集力に優れ、なおかつ接着力にも優れている。また、ポリマー組成物をアクリル系重合体の貧溶媒中へ噴出して、乳化又は分散液として調製するため、部材加工用粘着シートへ加工しやすいという利点があると共に、有機溶媒を用いる必要がないので環境衛生の面でも好ましい。
また本発明の部材加工用粘着シートは、粘着剤が低分子量成分の少ない高分子量ポリマーで構成されているので低汚染性であり、各種工業部材、詳しくは半導体、回路、各種プリント基板、各種マスク、リードフレームなどの微細加工部品の製造に際して極めて有用である。
【0028】
【実施例】
以下に、この発明の実施例を記載して、より具体的に説明する。なお、以下において、部とあるのは重量部を、%とあるのは重量%をそれぞれ意味する。
【0029】
参考例1
アクリル酸n−ブチル100部、2,2′−アゾビスイソブチロニトリル0.1部を、25℃の状態で、内容量が500mlのステンレス製の耐圧容器に、全体が150gとなるように配合して投入し、攪拌羽根により攪拌しながら徐々に高純度二酸化炭素を流し込み、2MPaの圧力に一旦保持した。数秒後、排出口から二酸化炭素を排出し耐圧容器に残存する空気を二酸化炭素で置換した。
上記操作の後、同様にして25℃の状態で高純度二酸化炭素を投入し、一旦7MPaの圧力に保持した。
その後、容器を加温して内部の温度を65℃まで上昇させた。温度が65℃に到達した時点でもう一度高純度二酸化炭素を投入し、内部の圧力を20MPaに調節した。この状態で約6時間保持して重合を行い、参考例1のポリマー組成物を得た。このポリマーのGPC法により測定される重量平均分子量は130万であり、分子量が10万以下の成分の含有率は3.3%であった。
【0030】
参考例2
アクリル酸2−エチルヘキシル80部、N−アクリロイルモルホリン20部、2,2′−アゾビスイソブチロニトリル0.1部を、25℃の状態で、内容量が500mlのステンレス製の耐圧容器に、全体が150gとなるように配合して投入し、攪拌羽根により攪拌しながら徐々に高純度二酸化炭素を流し込み、2MPaの圧力に一旦保持した。数秒後、排出口から二酸化炭素を排出し耐圧容器中に残存する空気を二酸化炭素で置換した。
上記操作の後、同様にして25℃の状態で高純度二酸化炭素を投入し、一旦7MPaの圧力に保持した。
その後、容器を加温して内部の温度を65℃まで上昇させた。温度が65℃に到達した時点でもう一度高純度二酸化炭素を投入し内部の圧力を20MPaに調節した。その後この状態で内部の温度を65℃にし、この状態で約6時間保持して重合を行い、参考例2のポリマー組成物を得た。このポリマーのGPC法により測定される重量平均分子量は90万であり、分子量10万以下の成分の含有率は6.2%であった。
【0031】
実施例1
参考例1で得たポリマー組成物を、予めポリマー固形分100部に対して3部となるようにポリオキシノニルフェニルエーテル硫酸ナトリウム塩を配合したイオン交換水中に、耐圧容器中から大気中に解放しながら吐出し、ホモジナイザーで攪拌しながら乳化して安定な乳化液を調製した。
【0032】
実施例2
参考例2で得たポリマー組成物を、予めポリマー固形分100部に対して3部となるようにポリオキシノニルフェニルエーテル硫酸ナトリウム塩を配合したイオン交換水中に、耐圧容器中から大気中に解放しながら吐出し、ホモジナイザーで攪拌しながら乳化して安定な乳化液を調製した。
【0033】
比較例1
温度計、撹拌機、窒素導入管および還流冷却管を備えた内容量が500mlの三つ口フラスコ型反応器内に、アクリル酸n−ブチル100部、2,2′−アゾビスイソブチロニトリル0.1部、トルエン200部を全体が300gとなるように配合して投入し、窒素ガスを約1時間導入しながら攪拌し、内部の空気を窒素で置換した。
その後内部の温度を65℃にし、この状態で約6時間保持して重合を行い、比較例1のポリマー組成物を得た。このポリマーのGPC法により測定される重量平均分子量は27万であり、分子量10万以下の成分の含有率は33.2%であった。
【0034】
以上より、実施例では、低分子量成分が少ない高分子量のアクリル系重合体をポリマー成分として含むので、粘着シートの粘着剤層を構成する感圧性接着剤として用いた場合、高い凝集力が得られると共に、被着体に対する汚染が極めて少ない。また、ポリマー組成物を噴出してアクリル系重合体の乳化液を調整するため、塗工が容易であり、しかも、有機溶媒を用いる必要がないので、環境衛生上有利である。
これに対し、比較例では、低分子量のアクリル系重合体しか得られないので、粘着シートの粘着剤層を構成する感圧性接着剤として用いた場合、高い凝集力が得られない。また、有機溶媒を使用しているので、環境衛生上好ましくない。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for producing an acrylic polymer composition useful as an adhesive for an adhesive tape or sheet, an acrylic pressure-sensitive adhesive composition comprising the acrylic polymer composition, and production of various industrial members. The present invention relates to a member processing pressure-sensitive adhesive sheet used at the time.
[0002]
[Prior art]
Conventionally, acrylic pressure-sensitive adhesive compositions are industrially produced almost by solution polymerization. This polymerization is initiated thermally or radiationally by a radical initiator. In the solution polymerization method, the acrylic pressure-sensitive adhesive composition comprises (meth) acrylic acid alkyl ester in an organic solvent such as toluene together with a modifying monomer such as acrylic acid, styrene, or vinyl acetate as necessary. It is prepared by polymerizing with.
[0003]
However, solution polymerization using an organic solvent causes chain transfer of the grown polymer chain to the solvent, and generally it is difficult to obtain a high molecular weight polymer and high cohesive force is difficult to obtain. Moreover, since a large amount of organic solvent is used, it is not preferable from the viewpoints of resource saving, environmental hygiene and the like.
[0004]
On the other hand, semiconductor integrated circuits are usually manufactured by slicing a high-purity silicon single crystal or the like into a wafer, etching a predetermined circuit pattern such as an IC on the wafer surface, incorporating the integrated circuit, and then grinding the backside of the wafer It is performed by grinding with a machine to reduce the thickness of the wafer to about 100 to 600 μm, and finally dicing into chips. Here, at the time of the grinding, an adhesive sheet is attached to the wafer surface to prevent the wafer from being damaged and to facilitate the grinding process. At the time of dicing, an adhesive sheet is attached to the back side of the wafer, the wafer is bonded and fixed, and the formed chip is picked up by a needle from the film substrate side and picked up and fixed on the die pad. ing.
[0005]
Adhesive sheets used for this purpose need to have adhesive strength that does not peel during grinding or dicing, but can be easily peeled off after picking up after grinding or dicing, and damage the semiconductor wafer. It is required that the adhesive strength is as low as possible. Furthermore, it is desirable that the adhesive sheets do not cause adhesive residue on the wafer surface or the wafer back surface and do not contaminate these surfaces.
[0006]
[Problems to be solved by the invention]
Therefore, an object of the present invention is an acrylic polymer composition comprising a high molecular weight polymer, excellent in cohesion and adhesion, and less contaminating the adherend, and can be prepared without using an organic solvent. It is in providing the manufacturing method, the acrylic pressure-sensitive adhesive composition which consists of this acrylic polymer composition, and the adhesive sheet for member processing.
[0007]
[Means for Solving the Problems]
As a result of intensive investigations to achieve the above-mentioned object, the inventors of the present invention agglomerated by preparing a stable emulsion or dispersion from a high molecular weight polymer obtained by polymerization using carbon dioxide as a diluent. The present inventors have found that an adhesive composition that is excellent in strength and adhesive force and can be easily processed into a pressure-sensitive adhesive sheet for member processing is obtained, and the present invention has been completed.
[0008]
That is, this invention uses at least (meth) acrylic acid alkyl ester and cyclic or acyclic (meth) acrylamide as a monomer, uses carbon dioxide as a diluent, pressure 5.7-40 MPa, temperature 20-100. A polymer composition containing an acrylic polymer having a weight average molecular weight of 400,000 or more obtained by radical polymerization under the condition of ° C is changed from a pressure of 5.7 to 40 MPa containing carbon dioxide under atmospheric pressure. The method for producing an acrylic polymer composition is characterized in that an acrylic polymer emulsion or dispersion is prepared by jetting into a poor solvent of the acrylic polymer . Before SL polymer composition preferably comprises a molecular weight of 100,000 or less in the ratio of components is less than 10% by weight of the total polymer acrylic polymer is preferred.
[0009]
Further, the present invention provides an acrylic polymer composition obtained by the above manufacturing method.
The present invention further provides a pressure-sensitive adhesive sheet for member processing having a pressure-sensitive adhesive layer composed of the acrylic polymer composition. The member processing adhesive sheet is used, for example, as a semiconductor wafer processing adhesive sheet.
In this specification, in addition to the above invention,
A polymer composition containing an acrylic polymer having a weight average molecular weight of 400,000 or more obtained by radical polymerization using carbon dioxide as a diluent is jetted into a poor solvent for the acrylic polymer, and then acrylic A method for producing an acrylic polymer composition, characterized by preparing an emulsion or dispersion of the polymer, will also be described .
[0010]
DETAILED DESCRIPTION OF THE INVENTION
In the present invention, (meth) acrylic acid alkyl ester is preferably used as the monomer. (Meth) acrylic acid alkyl ester includes alkyl alkyl ester having 1 to 18 carbon atoms and alkyl methacrylate. Specific examples include methyl acrylate, ethyl acrylate, propyl acrylate, butyl acrylate, 2-ethylhexyl acrylate, octyl acrylate, butyl methacrylate, 2-ethylhexyl methacrylate, octyl methacrylate, and the like. . These (meth) acrylic acid alkyl esters can be used alone or in admixture of two or more.
[0011]
As the monomer, only the above (meth) acrylic acid alkyl ester may be used, but the above (meth) acrylic acid alkyl ester as a main component may be used in combination with another monomer copolymerizable therewith. . Representative examples of the copolymerizable monomer include carboxyl group-containing ethylenically unsaturated monomers such as (meth) acrylic acid, crotonic acid, itaconic acid, maleic acid and fumaric acid. Among the carboxyl group-containing ethylenically unsaturated monomers, acrylic acid is particularly suitable.
[0012]
This ethylenically unsaturated monomer containing a carboxyl group is an important component for causing a cross-linking bond to the polymer. As other copolymerizable monomers, any of various monomers known as modifying monomers for acrylic pressure-sensitive adhesives such as vinyl acetate, styrene, acrylonitrile, cyclic (meth) acrylamide, and acyclic methacrylamide It can be used. The amount of these copolymerizable monomers used is preferably 50% by weight or less in the total monomer combined with the alkyl (meth) acrylate.
[0013]
The polymerization reaction can be carried out with the aid of an initiator that decomposes to generate radicals, and initiators usually used for radical polymerization can be used. Examples include organic peroxides such as dibenzoyl peroxide, di-tert-butyl peroxide, cumene hydroperoxide, and lauroyl peroxide, particularly when polymerizing at a temperature of 40 to 100 ° C. '-Azobisisobutyronitrile and azobisisovaleronitrile are used. Moreover, when superposing | polymerizing at the temperature of 20-40 degreeC, a binary initiator (Redox initiator) is used and the binary system of dibenzoyl peroxide and dimethylaniline etc. are mentioned as an example.
[0014]
The amount of the initiator used may be an amount usually used in the polymerization of the acrylic monomer. For example, about 0.005 to 10 parts by weight, preferably 0.1 to 100 parts by weight of the total amount of the monomers. About 5 parts by weight.
[0015]
The amount of carbon dioxide used as a diluent in the present invention is, for example, 5 to 2000 parts by weight, preferably 20 to 900 parts by weight with respect to 100 parts by weight of the total amount of the monomers. As the diluent, carbon dioxide alone is usually sufficient, but a small amount of an organic solvent may be included as necessary for improving the mixing property.
[0016]
Polymerization is performed in a temperature range of, for example, about 20 to 100 ° C. in carbon dioxide adjusted to a pressure of about 5.7 to 40 MPa, for example. For example, the polymerization can be performed in carbon dioxide in a supercritical state. The polymerization time is usually about 2 to 20 hours (for example, about 4 to 10 hours). The polymerization pressure and temperature may be set in several stages as required.
[0017]
As described above, when an acrylic monomer is radically polymerized using carbon dioxide as a diluent, the chain transfer reaction of the grown polymer chain to the solvent does not occur. Therefore, a relatively high molecular weight polymer compared to solution polymerization, that is, an acrylic polymer having a polymerization average molecular weight of 400,000 or more (for example, 400,000 to 2,000,000) is obtained. Also, by this method, an acrylic polymer in which the ratio of components having a molecular weight of 100,000 or less is 10% by weight or less of the whole polymer can be obtained. An acrylic pressure-sensitive adhesive containing such a polymer exhibits high cohesive strength. The weight average molecular weight and molecular weight distribution can be adjusted by the type and ratio of the monomer, the type and ratio of the polymerization initiator, the polymerization temperature, the polymerization time, and the like. The content of the low molecular weight component in the polymer can be determined by a gel permeation chromatography method (GPC method).
[0018]
In the present invention, a polymer composition containing an acrylic polymer having a weight average molecular weight of 400,000 or more thus obtained is ejected into a poor solvent for the acrylic polymer to prepare an emulsion or dispersion of the acrylic polymer. To do. The poor solvent may be a solvent in which the polymer is insoluble, but water is particularly preferable.
[0019]
In order to obtain a stable emulsification or dispersion, an emulsifier is usually added to the solvent. Examples of the emulsifier include anionic emulsifiers such as sodium lauryl sulfate, ammonium lauryl sulfate, sodium dodecylbenzenesulfonate, sodium polyoxyethylene alkyl ether sulfate, and sodium polyoxyethylene alkylphenyl ether sulfate. Moreover, you may use the radically polymerizable emulsifier which has a propenyl group etc. The usage-amount of an emulsifier is 10 weight part or less (for example, 0.001 weight part-10 weight part) with respect to 100 weight part of acrylic polymers. If the amount of the emulsifier used exceeds 10 parts by weight, it is difficult to obtain good results in the water resistance of the pressure-sensitive adhesive, which is not preferable.
[0020]
The method for ejecting the polymer composition is not particularly limited, and examples thereof include a method in which the polymer composition is ejected from a high-pressure state containing carbon dioxide into the solvent insoluble in the polymer while being released at atmospheric pressure from the mouth of a die or the like.
[0021]
The acrylic polymer composition thus obtained can be used as an acrylic pressure-sensitive adhesive composition as it is or by adding various additives as required. For example, the acrylic polymer is used as a main adhesive component, and in order to adjust the adhesive properties thereof, a known or commonly used tackifier resin (for example, rosin resin, terpene resin, petroleum resin, coumarone indene resin, You may mix | blend a styrene-type resin etc.). As additives other than the tackifying resin, various known additives such as a plasticizer, a filler such as calcium carbonate and fine powder silica, a colorant, and an ultraviolet absorber can be blended. The amount of these additives used may be a normal amount applied to an acrylic pressure sensitive adhesive. The additive may be added together with the monomer before polymerization, or may be added to the polymer composition after polymerization or an emulsification or dispersion obtained by ejecting the polymer composition.
[0022]
Moreover, a crosslinking agent can be mix | blended with an acrylic pressure-sensitive adhesive composition, and cohesion force can further be enlarged as an adhesive agent by bridge | crosslinking the said acrylic polymer with this crosslinking agent.
[0023]
Conventionally known cross-linking agents are widely included in the crosslinking agent, and among them, polyfunctional melamine compounds such as methylated trimethylol melamine; polyfunctional epoxy compounds such as diglycidyl aniline and glycerin diglycidyl ether are particularly preferable. . A polyfunctional melamine compound and a polyfunctional epoxy compound can also be used in combination. The amount of the crosslinking agent used is, for example, in the range of 0.001 to 10 parts by weight, preferably 0.01 to 5 parts by weight with respect to 100 parts by weight of the acrylic polymer.
[0024]
In addition, the use of a polyfunctional isocyanate compound is also preferable. Examples of such a compound include tolylene diisocyanate, hexamethylene diisocyanate, polymethylene polyphenyl isocyanate, diphenylmethane diisocyanate, diphenylmethane diisocyanate duplex, trimethylolpropane and tolylene diene. The reaction product with isocyanate, the reaction product of trimethylolpropane and hexamethylene diisocyanate, polyether polyisocyanate, polyester polyisocyanate and the like can be mentioned. The amount of these compounds used is, for example, in the range of 0.01 to 20 parts by weight, preferably 0.05 to 15 parts by weight, with respect to 100 parts by weight of the acrylic polymer.
[0025]
The pressure-sensitive adhesive sheet for member processing of the present invention has an adhesive layer composed of the above acrylic pressure-sensitive adhesive composition. This adhesive layer is formed, for example, by thinning the acrylic pressure-sensitive adhesive composition using a coating method using a conventional roll coater or the like. The member processing sheet is, for example, an adhesive tape in which an adhesive layer having a predetermined thickness is formed by coating the adhesive composition on one or both surfaces of various substrates such as paper, nonwoven fabric, plastic sheet, and foam sheet. Alternatively, it can take various forms such as a base-less adhesive tape in which the adhesive composition is coated on a release paper to form an adhesive layer having a predetermined thickness.
[0026]
The acrylic polymer that forms the adhesive layer coated on the adherend, substrate, or release paper is appropriately crosslinked in the drying step after coating, the light irradiation or electron beam irradiation step after this step, etc. It may be used.
[0027]
【The invention's effect】
According to the method for producing an acrylic polymer composition of the present invention, since carbon dioxide, which is a solvent without radical chain transfer, is used as a diluent, it has a low molecular weight compared to a polymer synthesized with a conventional organic solvent. An acrylic polymer composition containing a high molecular weight polymer with few components is obtained.
Since the acrylic pressure-sensitive adhesive composition of the present invention is composed of such an acrylic polymer composition, it has excellent cohesive strength and excellent adhesive strength. In addition, since the polymer composition is jetted into an acrylic polymer poor solvent and prepared as an emulsified or dispersed liquid, there is an advantage that it can be easily processed into a pressure-sensitive adhesive sheet for member processing, and there is no need to use an organic solvent. Therefore, it is preferable also in terms of environmental sanitation.
The pressure-sensitive adhesive sheet for processing members according to the present invention is low in contamination because the pressure-sensitive adhesive is composed of a high molecular weight polymer having a low low molecular weight component, and various industrial members, specifically semiconductors, circuits, various printed boards, various masks. It is extremely useful when manufacturing microfabricated parts such as lead frames.
[0028]
【Example】
Examples of the present invention will be described below in more detail. In the following, “parts” means parts by weight, and “%” means percent by weight.
[0029]
Reference example 1
100 parts of n-butyl acrylate and 0.1 part of 2,2′-azobisisobutyronitrile are placed in a stainless steel pressure vessel with an internal volume of 500 ml at 25 ° C. so that the total is 150 g. After mixing and charging, high purity carbon dioxide was gradually poured while stirring with a stirring blade, and the pressure was temporarily maintained at 2 MPa. After a few seconds, carbon dioxide was discharged from the outlet and the air remaining in the pressure vessel was replaced with carbon dioxide.
After the above operation, high-purity carbon dioxide was introduced in the same manner at 25 ° C., and once maintained at a pressure of 7 MPa.
Thereafter, the container was heated to raise the internal temperature to 65 ° C. When the temperature reached 65 ° C., high-purity carbon dioxide was introduced once again, and the internal pressure was adjusted to 20 MPa. In this state, the polymerization was carried out for about 6 hours to obtain a polymer composition of Reference Example 1. The weight average molecular weight of this polymer measured by the GPC method was 1.3 million, and the content of components having a molecular weight of 100,000 or less was 3.3%.
[0030]
Reference example 2
80 parts of 2-ethylhexyl acrylate, 20 parts of N-acryloylmorpholine, and 0.1 part of 2,2′-azobisisobutyronitrile were placed in a stainless steel pressure vessel having an internal volume of 500 ml at 25 ° C. The mixture was blended so that the whole became 150 g, and high-purity carbon dioxide was gradually poured while stirring with a stirring blade, and the pressure was temporarily maintained at 2 MPa. After a few seconds, carbon dioxide was discharged from the discharge port, and the air remaining in the pressure vessel was replaced with carbon dioxide.
After the above operation, high-purity carbon dioxide was introduced in the same manner at 25 ° C., and once maintained at a pressure of 7 MPa.
Thereafter, the container was heated to raise the internal temperature to 65 ° C. When the temperature reached 65 ° C., high-purity carbon dioxide was introduced again to adjust the internal pressure to 20 MPa. Thereafter, the internal temperature was set to 65 ° C. in this state, and the polymerization was carried out while maintaining this state for about 6 hours to obtain a polymer composition of Reference Example 2. The weight average molecular weight of this polymer measured by the GPC method was 900,000, and the content of components having a molecular weight of 100,000 or less was 6.2%.
[0031]
Example 1
The polymer composition obtained in Reference Example 1 is released from the pressure vessel into the atmosphere in ion-exchanged water that is premixed with polyoxynonyl phenyl ether sulfate sodium salt so as to be 3 parts with respect to 100 parts of the polymer solid content. The mixture was discharged while being emulsified while stirring with a homogenizer to prepare a stable emulsion.
[0032]
Example 2
The polymer composition obtained in Reference Example 2 was released from the pressure vessel into the atmosphere in ion-exchanged water previously blended with polyoxynonylphenyl ether sulfate sodium salt so as to be 3 parts with respect to 100 parts of the polymer solid content. The mixture was discharged while being emulsified while stirring with a homogenizer to prepare a stable emulsion.
[0033]
Comparative Example 1
In a three-necked flask type reactor having an internal volume of 500 ml equipped with a thermometer, a stirrer, a nitrogen inlet tube and a reflux condenser, n-butyl acrylate 100 parts, 2,2'-azobisisobutyronitrile 0.1 part and 200 parts of toluene were blended in a total amount of 300 g, stirred while introducing nitrogen gas for about 1 hour, and the air inside was replaced with nitrogen.
Thereafter, the internal temperature was set to 65 ° C., and the polymerization was carried out in this state for about 6 hours to obtain a polymer composition of Comparative Example 1. The weight average molecular weight of this polymer measured by the GPC method was 270,000, and the content of components having a molecular weight of 100,000 or less was 33.2%.
[0034]
As described above, in the examples, since a high molecular weight acrylic polymer with a small amount of low molecular weight component is included as a polymer component, a high cohesive force can be obtained when used as a pressure sensitive adhesive constituting the pressure sensitive adhesive layer of the pressure sensitive adhesive sheet. At the same time, there is very little contamination on the adherend. Moreover, since the polymer composition is ejected to adjust the emulsion of the acrylic polymer, coating is easy, and it is not necessary to use an organic solvent, which is advantageous in terms of environmental hygiene.
On the other hand, in the comparative example, only a low molecular weight acrylic polymer can be obtained. Therefore, when used as a pressure-sensitive adhesive constituting the pressure-sensitive adhesive layer of the pressure-sensitive adhesive sheet, a high cohesive force cannot be obtained. Moreover, since an organic solvent is used, it is not preferable in terms of environmental hygiene.

Claims (5)

単量体として少なくとも(メタ)アクリル酸アルキルエステル及び環状又は非環状の(メタ)アクリルアミドを用い、希釈剤として二酸化炭素を用いて圧力5.7〜40MPa、温度20〜100℃の条件下でラジカル重合させて得られる、重量平均分子量が400,000以上のアクリル系重合体を含むポリマー組成物を、二酸化炭素を含んだ圧力5.7〜40MPaの状態から大気圧下に、前記アクリル系重合体の貧溶媒中へ噴出して、アクリル系重合体の乳化又は分散液を調製することを特徴とするアクリル系重合体組成物の製造方法。 Using at least (meth) acrylic acid alkyl ester and cyclic or acyclic (meth) acrylamide as the monomer, and using carbon dioxide as the diluent, the pressure is 5.7 to 40 MPa and the temperature is 20 to 100 ° C. The acrylic polymer obtained by polymerizing a polymer composition containing an acrylic polymer having a weight average molecular weight of 400,000 or more from a pressure of 5.7 to 40 MPa containing carbon dioxide under atmospheric pressure. A method for producing an acrylic polymer composition, which comprises jetting into a poor solvent and preparing an emulsion or dispersion of an acrylic polymer. 分子量100,000以下の成分の比率が重合体全体の10重量%以下であるアクリル系重合体を含むポリマー組成物を噴出して、アクリル系重合体の乳化又は分散液を調製する請求項1記載のアクリル系重合体組成物の製造方法。And jetting a polymer composition ratio of molecular weight of 100,000 or less components containing an acrylic polymer is 10 wt% or less of the total polymer, according to claim 1 Symbol for preparing an emulsion or dispersion of acrylic polymer The manufacturing method of the acrylic polymer composition of mounting. 請求項1又は2に記載の製造方法で得られるアクリル系重合体組成物。 Acrylic polymer composition obtained by the production method according to claim 1 or 2. 請求項記載のアクリル系重合体組成物で構成された粘着剤層を有する部材加工用粘着シート。The adhesive sheet for member processing which has an adhesive layer comprised with the acrylic polymer composition of Claim 3 . 半導体ウエハ加工用として用いられる請求項記載の部材加工用粘着シート。The pressure-sensitive adhesive sheet for member processing according to claim 4, which is used for processing a semiconductor wafer.
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