JPS6143394B2 - - Google Patents
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- Publication number
- JPS6143394B2 JPS6143394B2 JP58033843A JP3384383A JPS6143394B2 JP S6143394 B2 JPS6143394 B2 JP S6143394B2 JP 58033843 A JP58033843 A JP 58033843A JP 3384383 A JP3384383 A JP 3384383A JP S6143394 B2 JPS6143394 B2 JP S6143394B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- parts
- aqueous suspension
- particle size
- microspheres
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
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- 239000002245 particle Substances 0.000 claims description 42
- 239000004005 microsphere Substances 0.000 claims description 31
- 239000007900 aqueous suspension Substances 0.000 claims description 29
- 239000000178 monomer Substances 0.000 claims description 24
- 238000010557 suspension polymerization reaction Methods 0.000 claims description 14
- 229920000642 polymer Polymers 0.000 claims description 13
- 238000006243 chemical reaction Methods 0.000 claims description 10
- 239000000203 mixture Substances 0.000 claims description 10
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 239000004820 Pressure-sensitive adhesive Substances 0.000 claims description 8
- 239000002998 adhesive polymer Substances 0.000 claims description 8
- 229920002554 vinyl polymer Polymers 0.000 claims description 8
- 239000000084 colloidal system Substances 0.000 claims description 6
- 230000001681 protective effect Effects 0.000 claims description 6
- 239000002253 acid Substances 0.000 claims description 5
- 239000005018 casein Substances 0.000 claims description 5
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 claims description 5
- 235000021240 caseins Nutrition 0.000 claims description 5
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 claims description 4
- 125000005907 alkyl ester group Chemical group 0.000 claims description 3
- 125000000217 alkyl group Chemical group 0.000 claims description 3
- 239000012736 aqueous medium Substances 0.000 claims description 3
- 125000004432 carbon atom Chemical group C* 0.000 claims description 3
- 230000000379 polymerizing effect Effects 0.000 claims description 2
- 239000000853 adhesive Substances 0.000 description 28
- 230000001070 adhesive effect Effects 0.000 description 28
- 238000006116 polymerization reaction Methods 0.000 description 15
- 239000000725 suspension Substances 0.000 description 8
- 239000010419 fine particle Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 239000011248 coating agent Substances 0.000 description 6
- 238000000576 coating method Methods 0.000 description 6
- 238000001704 evaporation Methods 0.000 description 6
- 230000008020 evaporation Effects 0.000 description 6
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 5
- 238000004873 anchoring Methods 0.000 description 5
- 229920001577 copolymer Polymers 0.000 description 5
- 239000000839 emulsion Substances 0.000 description 5
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 4
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 4
- 239000003945 anionic surfactant Substances 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- 230000000704 physical effect Effects 0.000 description 4
- 239000003381 stabilizer Substances 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 3
- 239000000123 paper Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 2
- GOXQRTZXKQZDDN-UHFFFAOYSA-N 2-Ethylhexyl acrylate Chemical compound CCCCC(CC)COC(=O)C=C GOXQRTZXKQZDDN-UHFFFAOYSA-N 0.000 description 2
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 239000004342 Benzoyl peroxide Substances 0.000 description 2
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 2
- SOGAXMICEFXMKE-UHFFFAOYSA-N Butylmethacrylate Chemical compound CCCCOC(=O)C(C)=C SOGAXMICEFXMKE-UHFFFAOYSA-N 0.000 description 2
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 description 2
- 235000019400 benzoyl peroxide Nutrition 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- LDHQCZJRKDOVOX-NSCUHMNNSA-N crotonic acid Chemical compound C\C=C\C(O)=O LDHQCZJRKDOVOX-NSCUHMNNSA-N 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000009775 high-speed stirring Methods 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 239000002736 nonionic surfactant Substances 0.000 description 2
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 description 2
- 229920002401 polyacrylamide Polymers 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 229910052709 silver Inorganic materials 0.000 description 2
- 239000004332 silver Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- LDHQCZJRKDOVOX-UHFFFAOYSA-N trans-crotonic acid Natural products CC=CC(O)=O LDHQCZJRKDOVOX-UHFFFAOYSA-N 0.000 description 2
- JAHNSTQSQJOJLO-UHFFFAOYSA-N 2-(3-fluorophenyl)-1h-imidazole Chemical compound FC1=CC=CC(C=2NC=CN=2)=C1 JAHNSTQSQJOJLO-UHFFFAOYSA-N 0.000 description 1
- DPBJAVGHACCNRL-UHFFFAOYSA-N 2-(dimethylamino)ethyl prop-2-enoate Chemical compound CN(C)CCOC(=O)C=C DPBJAVGHACCNRL-UHFFFAOYSA-N 0.000 description 1
- DXPPIEDUBFUSEZ-UHFFFAOYSA-N 6-methylheptyl prop-2-enoate Chemical compound CC(C)CCCCCOC(=O)C=C DXPPIEDUBFUSEZ-UHFFFAOYSA-N 0.000 description 1
- CUXGDKOCSSIRKK-UHFFFAOYSA-N 7-methyloctyl prop-2-enoate Chemical compound CC(C)CCCCCCOC(=O)C=C CUXGDKOCSSIRKK-UHFFFAOYSA-N 0.000 description 1
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 230000005653 Brownian motion process Effects 0.000 description 1
- GAWIXWVDTYZWAW-UHFFFAOYSA-N C[CH]O Chemical group C[CH]O GAWIXWVDTYZWAW-UHFFFAOYSA-N 0.000 description 1
- CNCOEDDPFOAUMB-UHFFFAOYSA-N N-Methylolacrylamide Chemical compound OCNC(=O)C=C CNCOEDDPFOAUMB-UHFFFAOYSA-N 0.000 description 1
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 1
- 239000002202 Polyethylene glycol Chemical class 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- DWAQJAXMDSEUJJ-UHFFFAOYSA-M Sodium bisulfite Chemical compound [Na+].OS([O-])=O DWAQJAXMDSEUJJ-UHFFFAOYSA-M 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- QYKIQEUNHZKYBP-UHFFFAOYSA-N Vinyl ether Chemical class C=COC=C QYKIQEUNHZKYBP-UHFFFAOYSA-N 0.000 description 1
- DPXJVFZANSGRMM-UHFFFAOYSA-N acetic acid;2,3,4,5,6-pentahydroxyhexanal;sodium Chemical compound [Na].CC(O)=O.OCC(O)C(O)C(O)C(O)C=O DPXJVFZANSGRMM-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000001252 acrylic acid derivatives Chemical class 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 239000002390 adhesive tape Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000000443 aerosol Substances 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000002280 amphoteric surfactant Substances 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 238000005537 brownian motion Methods 0.000 description 1
- 239000001768 carboxy methyl cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 229920006184 cellulose methylcellulose Polymers 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 229940061607 dibasic sodium phosphate Drugs 0.000 description 1
- BNIILDVGGAEEIG-UHFFFAOYSA-L disodium hydrogen phosphate Chemical compound [Na+].[Na+].OP([O-])([O-])=O BNIILDVGGAEEIG-UHFFFAOYSA-L 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- GMSCBRSQMRDRCD-UHFFFAOYSA-N dodecyl 2-methylprop-2-enoate Chemical compound CCCCCCCCCCCCOC(=O)C(C)=C GMSCBRSQMRDRCD-UHFFFAOYSA-N 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000010556 emulsion polymerization method Methods 0.000 description 1
- UIWXSTHGICQLQT-UHFFFAOYSA-N ethenyl propanoate Chemical compound CCC(=O)OC=C UIWXSTHGICQLQT-UHFFFAOYSA-N 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 150000002334 glycols Chemical class 0.000 description 1
- -1 hydroxypropyl Chemical group 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229920000831 ionic polymer Polymers 0.000 description 1
- PBOSTUDLECTMNL-UHFFFAOYSA-N lauryl acrylate Chemical compound CCCCCCCCCCCCOC(=O)C=C PBOSTUDLECTMNL-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- LVHBHZANLOWSRM-UHFFFAOYSA-N methylenebutanedioic acid Natural products OC(=O)CC(=C)C(O)=O LVHBHZANLOWSRM-UHFFFAOYSA-N 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- OMNKZBIFPJNNIO-UHFFFAOYSA-N n-(2-methyl-4-oxopentan-2-yl)prop-2-enamide Chemical compound CC(=O)CC(C)(C)NC(=O)C=C OMNKZBIFPJNNIO-UHFFFAOYSA-N 0.000 description 1
- UTSYWKJYFPPRAP-UHFFFAOYSA-N n-(butoxymethyl)prop-2-enamide Chemical compound CCCCOCNC(=O)C=C UTSYWKJYFPPRAP-UHFFFAOYSA-N 0.000 description 1
- ULYOZOPEFCQZHH-UHFFFAOYSA-N n-(methoxymethyl)prop-2-enamide Chemical compound COCNC(=O)C=C ULYOZOPEFCQZHH-UHFFFAOYSA-N 0.000 description 1
- 238000005580 one pot reaction Methods 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 229920001223 polyethylene glycol Chemical class 0.000 description 1
- 239000003505 polymerization initiator Substances 0.000 description 1
- 239000001267 polyvinylpyrrolidone Substances 0.000 description 1
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 description 1
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 235000019812 sodium carboxymethyl cellulose Nutrition 0.000 description 1
- 229920001027 sodium carboxymethylcellulose Polymers 0.000 description 1
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000004834 spray adhesive Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Description
本発明は粘着シートもしくは粘着テープに使用
する粘着剤に関するものある。更に詳しくは多種
多様の被着体に貼付―剥離のサイクルを繰り返し
行うことのできる粘着性微細球と重合体微粒子を
有する再剥離型粘着剤に関するものである。この
ような粘着剤は多くの好ましい性質をもつてい
る。例えば従来の粘着シート類は紙、プラスチツ
ク、金属、ガラスなどの被着体に貼布することは
容易にできるが剥離する際に被着体の破断または
粘着シート、テープの破断することが非常に多く
発生する。
本発明で得られた再剥離型粘着剤を粘着シート
等に利用することによつて繰り返して貼つたり、
剥離したりすることが可能になる。このような微
細球の粘着剤は1972年9月12日付でシルバーに与
えられた米国特許第3691140号に開示されてい
る。該米国特許はアクリル酸アルキルエステルと
水溶解性イオンモノマー及び無水マレイン酸から
なるモノマーを、保護コロイドまたはそれに属す
るもののない状態で水性懸濁重合によつて得られ
た共重合体微細球を種々の溶剤に分散してエアロ
ゾルスプレー粘着剤の用途に使用し、紙などの被
着体の表面に貼付―剥離のサイクルを回数多く行
うことができるとされている。しかしながら保護
コロイドを用いないで重合反応を行うために粒子
と粒子との凝集を起し易く目的の水性懸濁液が得
られ難い。また粒子径を希望するところのサイズ
に任意に変えたり、均一の大きさにすることは極
めて難しい。特に粘着剤を塗布、乾燥したときの
接着力、凝集力、粘着力及び投錨性のバランスが
とれず貼付―剥離の繰り返しができない。また、
特開昭54―41988号に記載されている粘着性重合
体微細球は上記のシルバーの米国特許に類似して
いるが、その特徴は微細球がノニオン性モノマー
からつくられる非イオン性のアクリル系共重合体
からなるものであること、またその製造方法は安
定化剤してポリアクリル酸塩、カルボキシ変性ポ
リアクリルアミド、アクリル酸―ジメチルアミノ
エチルメタクリレート共重合体、4級化ポリビニ
ル―ピロリドン共重合体、4級化アミン置換セル
ロージツク、カルボキシ変性セルロージツク、ナ
トリウムカルボキシメチルセルローズ等のイオン
性懸濁安定化剤と乳化剤を使用し懸濁重合を行う
こととしている。しかしながら粘着剤組成の懸濁
重合においてはイオン性モノマーを使用しないと
重合時に粒子の凝集が起り易く懸濁液が凝集する
危険がある。これを防ぐために上記の如き安定化
剤を多量に使用すると凝集力と粘着力のバランス
がくずれ物性面に悪影響を及ぼす。何故ならば上
記の如きイオン性ポリマーからなる懸濁安定化剤
はそれ自体の皮膜が強靭で接着力の弱いものであ
るから、その使用量の増大が原因で粘着剤の物性
に顕著にでてしまう欠陥がある。
また米国特許第3691140号及び特開昭54―41988
号は実用上において大きな欠陥がある。これらの
用途の懸濁液は平均粒子径が5〜150μ範囲のも
のが良いとされている。しかしこの範囲で希望の
粒子径が5〜150μのものを得ようとすると、水
性懸濁液中のより小さい微細球は上に浮いてクリ
ーム状になり、また平均で50〜150μの粒子径の
ものを得ようとすると沈降してしまう。水性懸濁
重合によつて得られた微細球を水洗後乾燥して溶
剤に分散せしめて目的の粘着剤を得ようとする場
合においては微細球が分離する方が好適である
が、本発明のように、得られた水性懸濁液をその
まま使用しようとしても塗工適性が非常に悪く、
また放置安定性が不良であるため実用上製品化で
きない。
本発明者らは上記の如き欠陥を除くために研究
した結果、極めて工業的に製造し易く、かつ放置
安定性と基材への密着性、塗工性等にすぐれた粘
着性重合体の水性懸濁液を得ることを見出し、本
発明に至つたものである。
即ち本発明は、
1 (A) (a)炭素数4〜12のアルキル基を有する
(メタ)アクリル酸のアルキルエステル70〜
99.9重量%(以下重量%及び重量部を各々%及
び部と記す)、(b)α―モノオレフインカルボン
酸0.1〜10%及び(c)上記(a),(b)両成分以外のビ
ニル化合物0〜29.9%とからなる単量体成分の
100部を水性懸濁重合することによつて得られ
た平均粒子径が10〜100μの粘着性重合体微細
球と、(B)ビニル系単量体の20〜300部を水性媒
体中で重合することによつて得られた平均粒子
径が0.1〜4μの重合体微粒子を含有してなる
再剥離性粘着剤組成物。
2 第1段階の反応工程において、上記(A)成分の
平均粒子径10〜100μの粘着性重合体微細球を
水性懸濁重合によつて製造し、次いで第2段階
以降の反応工程において、第1段階の反応で得
られた水性懸濁液中で(B)ビニル系単量体を重合
して平均粒子径0.1〜4μの重合体微粒子を製
造することからなる再剥離性粘着剤組成物の製
造法の2発明からなるものである。
本発明で使用される(a)成分の(メタ)アクリル
酸アルキルエステルとしてはブチルアクリレー
ト、2―エチルヘキシルアクリレート、イソオク
チルアクリレート、イソノニルアクリレート、ラ
ウリルアクリレート、ブチルメタクリレート、ラ
ウリルメタクリレートなどが挙げられる。(b)成分
のα―モノオレフインカルボン酸してはアクリル
酸、メタクリル酸、イタコン酸、マレイン酸、ク
ロトン酸などがある。また(c)成分のビニル系単重
体は粘着力と凝集力の調整を図るために用いられ
るものでメチル(メタ)アクリレート、エチル
(メタ)アクリレート、酢酸ビニル、プロピオン
酸ビニル、スチレン、アクリロニトリル、(メ
タ)アクリル酸ヒドロキシエチル、(メタ)アク
リル酸ヒドロキシプロピル、N,N―ジメチルア
ミノエチルアクリレート、アクリル酸アミド、ダ
イアセトンアクリルアミド、N―メチロールアク
リルアミド、N―メトキシメチルアクリルアミ
ド、N―n―ブトキシメチルアクリルアミドなど
を29.9%まで、好ましくは0.5〜10%を単独でま
たは併用することもできる。(a)成分の(メタ)ア
クリレートは粘着力と内部凝集力を与える成分で
あり、高い弾性体を得るためには少なくとも70%
が必要であり、好ましくは80〜99%である。(b)成
分のα―モノオレフインカルボン酸の使用量が10
%を越えると重合反応が難しく、また内部凝集力
が高くなり過ぎるので粘着力が弱くなり、被着体
に対して接着不能になる。また使用量が0.1%よ
り少ないと重合反応時に粒子の凝固が生じ易い。
好ましい使用量は1〜5%である。
(B)成分のビニル系単量体としては各種の(メ
タ)アクリレート、ビニルエステル、ビニルエー
テル、スチレン、アクリロニトリルその他の単量
体を単独または適当に併用して、粘着性重合体微
細球の結合剤となりうるものであればよく、特に
限定されない。
本発明の水性懸濁重合を行うに当つては保護コ
ロイドは必須成分ではないが、単量体成分によつ
てはカゼイン、ポリアクリルアミド、ポリエチレ
ングリコール誘導体などを単独使用又は併用する
ことも効果的である。殊にカゼインを保護コロイ
ドとして使用することによつて極めて工業的に製
造し易く、かつ高い品質特性を具備した水性懸濁
液を得ることができる。その使用量は要求される
物性によつて異なるが、単量体100部に対して2
〜8部で充分である。カゼインの使用に当つては
アンモニア又はアミンの水溶液にて完全なる安定
液にしておくのがよい。また界面活性剤はアニオ
ン性、ノニオン性もしくは両性イオン界面活性剤
を使用するが、特にアニオン性界面活性剤が特長
ある物性が得られる。
本発明の再剥離性粘着剤組成物を製造するに当
つては、(A)成分の粘着剤重合体微細球を含有する
水性懸濁液と(B)成分の重合体微粒子を含有する水
性懸濁液又は水性分散液を予め別個に製造した後
それらを配合することもできるが、製造工程を簡
略化して製造コストを低減するためにも一連の段
階的重合方法によつ製造することが望ましい。段
階的重合方法による場合は、まず第1段階の反応
工程において上記(a),(b)及び(c)の単量体成分をベ
ンゾイルパーオキサイドなどの油溶性重合開始剤
の存在下に保護コロイド又は界面活性剤などを使
用して水性媒体中で懸濁重合反応を行い、平均粒
子径が10〜100μの微細球の懸濁液を得る。この
懸濁重合反応においては、各単量体成分をその性
状によつて分割して段階的に重合反応を進めてい
く多層重合方法なども採用されうる。
次いで第1段階の反応で得られた水性懸濁液中
で上記(B)成分の単量体をモノマー添加法あるいは
予め高速撹拌によつて擬似エマルシヨン化された
ものを添加するエマルシヨン添加法などによつて
添加して重合反応させ、平均粒子径が0.1〜4μ
の重合体微粒子を含有させる。
本発明の水性懸濁重合で得られる粘着性重合体
微細球はその粒子径が大きい程再剥離性は良くな
るが、その反面接着力と投錨性及び放置安定性と
塗工性が悪くなる。これらを勘案すると10〜100
μの粒子径を有するものが好適である。しかし、
10〜100μの粒子径をもつ微細球を含む水性懸濁
液でも長期の保存安定性は十分でなく、微細球の
沈降は避けられない。従つてこの沈降現象を防止
するためにも、本発明ではブラウン運動によつて
沈降及び浮上しにくい、粒子径が0.1〜4μの重
合体微粒子を10〜100μの粒子径を有する微細球
間に包含させるものである。またこの粒子径が
0.1〜4μの微粒子は本発明で得られた水性懸濁
液を塗工した後の投錨性と粘着効果を改善する特
長を有するものである。水性懸濁液から微細球を
分離して一度洗い出し、更に乾燥して同一サイズ
の微細球のみを使用するのであれば塗工後の粒子
が均一に並列した状態に塗工することができる。
しかし粒子径の大きさが10〜100μのものを直接
塗工すると塗工面が凹凸になる。従つてミクロ的
に見れば粘着性微細球の塗工されていないところ
ができてしまうために、これが原因で投錨性不良
が生じる。理想とされる塗工面は、微細球が等間
隔に5〜10μの間隙を開けていた方が加圧された
ときに微細球が横に拡がり易く均一に接触されて
接着力が上昇し、また剥したときに復元し、繰り
返し使用できる。その反面微細球と微細球の間が
開き過ぎると微細球が復元力のある弾性体のため
に被着体及び基材に対して接触面積が減つて投錨
性及び接着力が極端に低下する。従つてこれらの
投錨効果及び接着力をもたらす結合層が必要にな
つてくる。この働きをするのが0.1〜4μの粒子
径を有する重合体微粒子である。該重合体微粒子
は基材への接着剤の働きをすると同時に微細球を
固着する重要な働きをするものである。その含有
される割合は、(A)成分の単量体100部からなる粘
着性微細球に対して(B)成分の単量体20〜300部か
らなる重合体微粒子が包含されるようなものがよ
い。
本発明の粘着剤組成物は理論通りに74%以上の
固形分を含有する水性懸濁液とすることもできる
が、安定性及び塗工適性上不都合が生じるため45
%前後の有効成分を含有するように製造するのが
もつとも好ましい。以下に実施例を挙げて説明す
る。尚、実施例中部とあるものは重量部を、%と
あるものは重量%を意味するものである。
実施例 1
温度計、環流冷却器、変速機付撹拌機を備えた
1の三つ口フラスコを用いて、下記なる(A),
(B),(C)の各成分を段階的に重合反応を行つた。
The present invention relates to an adhesive for use in adhesive sheets or adhesive tapes. More specifically, the present invention relates to a removable adhesive having adhesive microspheres and polymer particles that can be repeatedly applied to and peeled off from a wide variety of adherends. Such adhesives have many desirable properties. For example, conventional adhesive sheets can be easily applied to adherends such as paper, plastic, metal, and glass, but when peeled off, the adherend or the adhesive sheet or tape may break. Occurs often. By using the removable adhesive obtained in the present invention in adhesive sheets etc., it can be pasted repeatedly,
It becomes possible to peel it off. Such a microsphere adhesive is disclosed in U.S. Pat. No. 3,691,140 to Silver, dated September 12, 1972. The US patent discloses that copolymer microspheres obtained by aqueous suspension polymerization of a monomer consisting of an acrylic acid alkyl ester, a water-soluble ionic monomer, and maleic anhydride in the absence of a protective colloid or anything belonging thereto are used to form various copolymer microspheres. It is said that it can be used as an aerosol spray adhesive by dispersing it in a solvent, and can be applied and peeled off many times on the surface of an adherend such as paper. However, since the polymerization reaction is carried out without using a protective colloid, particles tend to aggregate, making it difficult to obtain the desired aqueous suspension. Furthermore, it is extremely difficult to arbitrarily change the particle size to a desired size or to make the particle size uniform. In particular, when the adhesive is applied and dried, the adhesive strength, cohesive strength, adhesion strength, and anchorage properties are not balanced, making it impossible to repeat pasting and peeling. Also,
The adhesive polymer microspheres described in JP-A No. 54-41988 are similar to those in Silver's U.S. patent mentioned above, but the feature is that the microspheres are nonionic acrylic microspheres made from nonionic monomers. It must be made of a copolymer, and its manufacturing method uses polyacrylate, carboxy-modified polyacrylamide, acrylic acid-dimethylaminoethyl methacrylate copolymer, and quaternized polyvinyl-pyrrolidone copolymer as stabilizers. Suspension polymerization is carried out using ionic suspension stabilizers and emulsifiers such as , quaternized amine-substituted cellulose, carboxy-modified cellulose, and sodium carboxymethyl cellulose. However, in suspension polymerization of the adhesive composition, if an ionic monomer is not used, particles tend to aggregate during polymerization, and there is a risk that the suspension will aggregate. In order to prevent this, if a large amount of the above-mentioned stabilizer is used, the balance between cohesive force and adhesive force will be disrupted, and the physical properties will be adversely affected. This is because the suspension stabilizer made of an ionic polymer as mentioned above has a strong film and weak adhesive strength, so an increase in the amount used will significantly affect the physical properties of the adhesive. There is a flaw. Also, U.S. Patent No. 3691140 and Japanese Patent Application Publication No. 54-41988
The issue has a major flaw in practical use. Suspensions for these uses are said to have an average particle size in the range of 5 to 150 microns. However, if one tries to obtain the desired particle size in this range from 5 to 150μ, the smaller microspheres in the aqueous suspension will float to the top and become creamy, and the particles with an average size of 50 to 150μ If you try to get something, it will sink. When the desired adhesive is obtained by washing microspheres obtained by aqueous suspension polymerization with water, drying them, and dispersing them in a solvent, it is preferable that the microspheres are separated. Therefore, even if you try to use the obtained aqueous suspension as it is, it will have very poor coating suitability.
In addition, it cannot be commercialized in practical use because of its poor storage stability. As a result of research to eliminate the above-mentioned defects, the present inventors have found that an aqueous adhesive polymer that is extremely easy to manufacture industrially and has excellent storage stability, adhesion to substrates, and coating properties. It was discovered that a suspension can be obtained, leading to the present invention. That is, the present invention provides: 1 (A) (a) an alkyl ester of (meth)acrylic acid having an alkyl group having 4 to 12 carbon atoms;
99.9% by weight (hereinafter referred to as % and parts by weight), (b) 0.1 to 10% of α-monoolefincarboxylic acid, and (c) vinyl compounds other than both components (a) and (b) above. of monomer components consisting of 0 to 29.9%.
Adhesive polymer microspheres with an average particle diameter of 10 to 100 μ obtained by aqueous suspension polymerization of 100 parts and 20 to 300 parts of (B) vinyl monomer are polymerized in an aqueous medium. A removable pressure-sensitive adhesive composition containing fine polymer particles having an average particle diameter of 0.1 to 4 μm. 2 In the first reaction step, adhesive polymer microspheres of the above component (A) with an average particle diameter of 10 to 100 μ are produced by aqueous suspension polymerization, and then in the second and subsequent reaction steps, A removable pressure-sensitive adhesive composition comprising polymerizing (B) a vinyl monomer in an aqueous suspension obtained in a one-step reaction to produce fine polymer particles having an average particle size of 0.1 to 4μ. This invention consists of two manufacturing method inventions. Examples of the (meth)acrylic acid alkyl ester as component (a) used in the present invention include butyl acrylate, 2-ethylhexyl acrylate, isooctyl acrylate, isononyl acrylate, lauryl acrylate, butyl methacrylate, lauryl methacrylate, and the like. The α-monoolefincarboxylic acids of component (b) include acrylic acid, methacrylic acid, itaconic acid, maleic acid, and crotonic acid. In addition, the vinyl monopolymers of component (c) are used to adjust adhesive strength and cohesive force, and include methyl (meth)acrylate, ethyl (meth)acrylate, vinyl acetate, vinyl propionate, styrene, acrylonitrile, ( Hydroxyethyl meth)acrylate, hydroxypropyl (meth)acrylate, N,N-dimethylaminoethyl acrylate, acrylic acid amide, diacetone acrylamide, N-methylolacrylamide, N-methoxymethylacrylamide, N-n-butoxymethylacrylamide up to 29.9%, preferably 0.5 to 10%, alone or in combination. The (meth)acrylate component (a) is a component that provides adhesive strength and internal cohesive force, and in order to obtain a high elasticity, at least 70%
is required, preferably 80-99%. (b) The amount of α-monoolefincarboxylic acid used is 10
If it exceeds %, the polymerization reaction will be difficult and the internal cohesive force will become too high, resulting in weak adhesive strength and failure to adhere to the adherend. Furthermore, if the amount used is less than 0.1%, particles tend to coagulate during the polymerization reaction.
The preferred amount used is 1-5%. As the vinyl monomer of component (B), various (meth)acrylates, vinyl esters, vinyl ethers, styrene, acrylonitrile, and other monomers may be used alone or in appropriate combinations to form adhesive polymer microspheres. It is not particularly limited as long as it can be. Although a protective colloid is not an essential component in performing the aqueous suspension polymerization of the present invention, depending on the monomer components, it may be effective to use casein, polyacrylamide, polyethylene glycol derivatives, etc. alone or in combination. be. In particular, by using casein as a protective colloid, it is possible to obtain aqueous suspensions that are extremely easy to produce industrially and have high quality characteristics. The amount used varies depending on the required physical properties, but 2 parts per 100 parts of monomer.
~8 parts is sufficient. When using casein, it is best to make it a completely stable solution with an aqueous solution of ammonia or amine. Further, as the surfactant, anionic, nonionic or amphoteric surfactants are used, and particularly anionic surfactants can provide characteristic physical properties. In producing the removable pressure-sensitive adhesive composition of the present invention, an aqueous suspension containing adhesive polymer microspheres as component (A) and an aqueous suspension containing polymer fine particles as component (B) are used. Although it is possible to prepare the suspension or aqueous dispersion separately in advance and then blend them, it is preferable to manufacture the suspension by a series of stepwise polymerization methods in order to simplify the manufacturing process and reduce manufacturing costs. . In the case of a stepwise polymerization method, first, in the first step reaction step, the above monomer components (a), (b) and (c) are treated with a protective colloid in the presence of an oil-soluble polymerization initiator such as benzoyl peroxide. Alternatively, a suspension polymerization reaction is carried out in an aqueous medium using a surfactant or the like to obtain a suspension of microspheres with an average particle size of 10 to 100 μm. In this suspension polymerization reaction, a multilayer polymerization method may be adopted in which each monomer component is divided according to its properties and the polymerization reaction is proceeded in stages. Next, in the aqueous suspension obtained in the first step reaction, the monomer of the component (B) is added using a monomer addition method or an emulsion addition method in which a pseudo-emulsion that has been previously formed by high-speed stirring is added. Then, add it and cause a polymerization reaction, and the average particle size is 0.1 to 4μ.
of polymer fine particles. The larger the particle size of the adhesive polymer microspheres obtained by the aqueous suspension polymerization of the present invention, the better the re-peelability, but the worse the adhesive strength, anchoring ability, storage stability, and coating properties. 10-100 considering these
Those having a particle size of μ are preferred. but,
Even aqueous suspensions containing microspheres with a particle size of 10 to 100 μm do not have sufficient long-term storage stability, and sedimentation of the microspheres is unavoidable. Therefore, in order to prevent this sedimentation phenomenon, in the present invention, polymer fine particles with a particle size of 0.1 to 4μ, which are difficult to sediment or float due to Brownian motion, are included between microspheres with a particle size of 10 to 100μ. It is something that makes you Also, this particle size
The fine particles having a size of 0.1 to 4 μm have the feature of improving the anchoring property and adhesion effect after coating the aqueous suspension obtained in the present invention. If the microspheres are separated from the aqueous suspension, washed out once, and further dried, and only microspheres of the same size are used, the particles can be coated in a uniformly arranged state after coating.
However, if particles with a particle size of 10 to 100 μm are applied directly, the coated surface will become uneven. Therefore, from a microscopic perspective, there are areas where the adhesive microspheres are not coated, which causes poor anchoring performance. The ideal coated surface is one in which the microspheres are spaced evenly apart with gaps of 5 to 10μ, so that when pressure is applied, the microspheres will spread laterally more easily and will be in even contact, increasing adhesive strength. It restores its original shape when removed and can be used repeatedly. On the other hand, if the space between the fine spheres is too large, the fine spheres are elastic bodies with restoring force, so the contact area with the adherend and the base material decreases, resulting in an extremely low anchoring ability and adhesive force. Therefore, a bonding layer is required to provide these anchoring effects and adhesion. This function is performed by polymer fine particles having a particle size of 0.1 to 4 μm. The polymer fine particles act as an adhesive to the substrate and at the same time play an important role in fixing the microspheres. The content ratio is such that polymer fine particles consisting of 20 to 300 parts of component (B) monomer are included in adhesive microspheres consisting of 100 parts of component (A) monomer. Good. The pressure-sensitive adhesive composition of the present invention can be made into an aqueous suspension containing 74% or more of solids as per theory, but this will cause problems in terms of stability and coating suitability.
It is also preferable to manufacture the product so that the active ingredient content is around 10%. Examples will be described below. It should be noted that "middle part" in the examples refers to parts by weight, and "%" refers to % by weight. Example 1 Using a three-necked flask equipped with a thermometer, a reflux condenser, and a variable speed stirrer, the following (A) was prepared.
The polymerization reaction of each component (B) and (C) was carried out stepwise.
【表】
(A)なる成分を三つ口フラスコ内に全量投入す
る。撹拌速度300回転前後で溶解または混合後N2
ガスをパージする。その後徐々に昇温すると70〜
75℃で重合反応が始まり、80〜82℃位から急に激
しくなり85〜88℃まで発熱する。その後冷却し81
〜82℃を保持させ2時間重合反応する。フラスコ
中には20〜60μの粒子径を持つた重合体微細球の
水性懸濁液が生成する。続いて次の重合工程に入
る。別の容器にて溶解または混合された(B)なる成
分を高速撹拌にて擬似エマルシヨンにする。この
ようにして得られた(B)成分を先に生成された水性
懸濁液に60分で滴下して、引続き81〜82℃で1時
間反応する。続いて(C)なる成分を30分で滴下して
同様に段階的重合反応を3時間続ける。その後生
成した水性懸濁液を30℃まで冷却させ、その蒸発
残分、粘度、および粒子径を確認した。蒸発残分
40.0%、粘度1400cp/20℃粒子径は小さい方で
0.5〜2μ、大きい方で20〜60μであつた。
実施例 2
実施例1に記述した装置及び手続きを用いて
(A),(B)なる成分を段階的重合反応で実施例1と同
様に行つた。ただし、反応温度は75〜78℃、(A)成
分の反応時間は4時間、(B)成分の滴下時間は1時
間、その後の反応時間は2時間で行つた。[Table] Pour the entire amount of ingredient (A) into a three-necked flask. N2 after dissolving or mixing at a stirring speed of around 300 rpm
Purge gas. After that, when the temperature is gradually increased, it becomes 70~
The polymerization reaction begins at 75°C and suddenly becomes more intense at around 80-82°C, generating heat up to 85-88°C. Then cool down 81
The temperature is maintained at ~82°C and the polymerization reaction is carried out for 2 hours. An aqueous suspension of polymer microspheres with a particle size of 20-60 microns is formed in the flask. Next, the next polymerization step begins. Component (B) dissolved or mixed in a separate container is made into a pseudo-emulsion by high-speed stirring. The component (B) thus obtained was added dropwise to the previously produced aqueous suspension over 60 minutes, followed by reaction at 81-82°C for 1 hour. Subsequently, component (C) was added dropwise over 30 minutes, and the same stepwise polymerization reaction was continued for 3 hours. The resulting aqueous suspension was then cooled to 30°C, and its evaporation residue, viscosity, and particle size were confirmed. Evaporation residue
40.0%, viscosity 1400cp/20℃ Particle size is smaller
The diameter was 0.5 to 2μ, and the larger one was 20 to 60μ. Example 2 Using the apparatus and procedure described in Example 1
Components (A) and (B) were subjected to a stepwise polymerization reaction in the same manner as in Example 1. However, the reaction temperature was 75 to 78°C, the reaction time for component (A) was 4 hours, the time for dropping component (B) was 1 hour, and the subsequent reaction time was 2 hours.
【表】
得られた水性懸濁液は蒸発残分51.5%、粘度
1500cp/20℃、粒子径は小さい微粒子が0.3〜1
μ、大きい微細球が10〜40μの粒子径の分布を持
つ水性懸濁液であつた。
実施例 3
実施例1に記述した装置及び手続きを用いて、
予め溶解しておいた15%濃度のカゼインアンモニ
ア水溶液20部、分子量10〜15万のポリエチレンオ
キサイド(PEO―1、製鉄化学工業製)2部、
アニオン性界面活性剤1部及び水250部を投入し
充分撹拌して水溶液とする。
次に2―エチルヘキシルアクリレート100部、
ブチルアクリレート90部、エチルアクリレート10
部、クロトン酸1.5部、過酸化ベンゾイル0.5部を
別の容器にて撹拌溶解する。
次いでこのモノマー混合液を先に準備された水
溶液に添加して撹拌する。撹拌速度200回転前
後、反応温度は80〜82℃で2時間水性懸濁重合を
行つた。フラスコ中には粒子径25〜70μの微細球
を含む水性懸濁液が生成した。その蒸発残分は
43.0%、粘度は1800cp/20℃であつた。次いで別
の容器にてアニオン性界面活性剤1部、ノニオン
性界面活性剤4部、水300部、過硫酸カリウム1
部、第二リン酸ソーダ2部、亜硫酸水素ナトリウ
ム0.5部、アクリル酸5部、ブチルアクリレート
100部、エチルアクリレート100部を通常の乳化重
合方法で行い蒸発残分41.0%、粘度100cp/20
℃、粒子径0.1〜0.5μのエマルシヨン液を得た。
このエマルシヨン液を先に生成した水性懸濁液10
部に対して20部添加し混合液を得た。得られた混
合液は蒸発残分43.0%、粘度1650cp/20℃であつ
た。実施例1、2、3、で得られた再剥離性粘着
剤を上質紙(55K)に卓上塗布器を用いて、乾燥
後10〜15gr/m2になるように直接塗布乾燥させ
た。このようにして用意された粘着シートをステ
ンレス板に貼り合わせ、JIS Z 0237―1980に従
つて粘着力、保持力、タツクを調べた。その結果
を下表に記す。[Table] The obtained aqueous suspension has an evaporation residue of 51.5% and a viscosity of
1500cp/20℃, particle size is small particles 0.3~1
μ, the large microspheres were an aqueous suspension with a particle size distribution of 10 to 40 μ. Example 3 Using the apparatus and procedure described in Example 1,
20 parts of a pre-dissolved 15% casein ammonia aqueous solution, 2 parts of polyethylene oxide (PEO-1, manufactured by Seitetsu Kagaku Kogyo) with a molecular weight of 100,000 to 150,000,
Add 1 part of anionic surfactant and 250 parts of water and stir thoroughly to form an aqueous solution. Next, 100 parts of 2-ethylhexyl acrylate,
90 parts of butyl acrylate, 10 parts of ethyl acrylate
1 part, 1.5 parts of crotonic acid, and 0.5 part of benzoyl peroxide in a separate container. Next, this monomer mixture is added to the previously prepared aqueous solution and stirred. Aqueous suspension polymerization was carried out for 2 hours at a stirring speed of around 200 revolutions and a reaction temperature of 80 to 82°C. An aqueous suspension containing microspheres with a particle size of 25-70 microns was formed in the flask. The evaporation residue is
43.0%, and the viscosity was 1800 cp/20°C. Next, in a separate container, add 1 part of anionic surfactant, 4 parts of nonionic surfactant, 300 parts of water, and 1 part of potassium persulfate.
parts, dibasic sodium phosphate 2 parts, sodium bisulfite 0.5 parts, acrylic acid 5 parts, butyl acrylate
100 parts of ethyl acrylate using the usual emulsion polymerization method, evaporation residue: 41.0%, viscosity: 100 cp/20
An emulsion liquid with a particle size of 0.1 to 0.5 μm was obtained.
This emulsion was previously produced as an aqueous suspension10
20 parts per part was added to obtain a mixed solution. The resulting mixed solution had an evaporation residue of 43.0% and a viscosity of 1650 cp/20°C. The removable adhesives obtained in Examples 1, 2, and 3 were directly coated onto high-quality paper (55K) using a tabletop applicator to a drying weight of 10 to 15 gr/m 2 and allowed to dry. The pressure-sensitive adhesive sheet prepared in this manner was bonded to a stainless steel plate, and its adhesive strength, holding power, and tack were examined in accordance with JIS Z 0237-1980. The results are shown in the table below.
【表】【table】
Claims (1)
(メタ)アクリル酸のアルキルエステル70〜
99.9重量%、(b)α―モノオレフインカルボン酸
0.1〜10重量%及び(c)上記(a),(b)両成分以外の
ビニル系単量体0〜29.9重量%とからなる単量
体成分の100重量部を水性懸濁重合することに
よつて得られた平均粒子径が10〜100μの粘着
性重合体微細球と、 (B) ビニル系単量体の20〜300重量部を水性媒体
中で重合することによつて得られた平均粒子径
が0.1〜4μの重合体微粒子を含有してなる再
剥離性粘着剤組成物。 2 第1段階の反応工程において、(A) (a)炭素数
4〜12のアルキル基を有する(メタ)アクリル酸
のアルキルエステル70〜99.9重量%、(b)α―モノ
オレフインカルボン酸0.1〜10重量%及び(c)上記
(a),(b)両成分以外のビニル系単量体0〜29.9重量
%とからなる単量体成分の100重量部を水性懸濁
重合して平均粒子径が10〜100μの粘着性重合体
微細球を製造し、次いで第2段階以降の反応工程
において、前記第1段階の反応で得られた水性懸
濁液中で(B)ビニル系単量体の20〜300重量部を重
合して平均粒子径が0.1〜4μの重合体微粒子を
製造することを特徴とする再剥離性粘着剤組成物
の製造法。 3 水性懸濁重合に際し、保護コロイドとしてカ
ゼインを使用することを特徴とする特許請求の範
囲第2項記載の再剥離性粘着剤組成物の製造法。[Scope of Claims] 1 (A) (a) Alkyl ester of (meth)acrylic acid having an alkyl group having 4 to 12 carbon atoms 70 to
99.9% by weight, (b) α-monoolefincarboxylic acid
100 parts by weight of a monomer component consisting of 0.1 to 10% by weight and (c) 0 to 29.9% by weight of a vinyl monomer other than both components (a) and (b) above are subjected to aqueous suspension polymerization. The average particle size obtained by polymerizing the thus obtained adhesive polymer microspheres with an average particle diameter of 10 to 100μ and (B) 20 to 300 parts by weight of vinyl monomer in an aqueous medium. A removable pressure-sensitive adhesive composition containing fine polymer particles having a particle size of 0.1 to 4μ. 2 In the first stage reaction step, (A) (a) 70 to 99.9% by weight of an alkyl ester of (meth)acrylic acid having an alkyl group having 4 to 12 carbon atoms, (b) 0.1 to 0.1 to 99.9% by weight of α-monoolefincarboxylic acid; 10% by weight and (c) above
(a) and (b) 100 parts by weight of a monomer component consisting of 0 to 29.9% by weight of vinyl monomers other than both components are subjected to aqueous suspension polymerization to form a sticky polymer with an average particle size of 10 to 100μ. Coalesced microspheres are produced, and then in the second and subsequent reaction steps, 20 to 300 parts by weight of the vinyl monomer (B) is polymerized in the aqueous suspension obtained in the first step reaction. 1. A method for producing a removable pressure-sensitive adhesive composition, which comprises producing fine polymer particles having an average particle diameter of 0.1 to 4 μm. 3. The method for producing a removable pressure-sensitive adhesive composition according to claim 2, characterized in that casein is used as a protective colloid during aqueous suspension polymerization.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3384383A JPS59159869A (en) | 1983-03-03 | 1983-03-03 | Repeelable pressure-sensitive adhesive composition and production thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3384383A JPS59159869A (en) | 1983-03-03 | 1983-03-03 | Repeelable pressure-sensitive adhesive composition and production thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59159869A JPS59159869A (en) | 1984-09-10 |
JPS6143394B2 true JPS6143394B2 (en) | 1986-09-27 |
Family
ID=12397771
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3384383A Granted JPS59159869A (en) | 1983-03-03 | 1983-03-03 | Repeelable pressure-sensitive adhesive composition and production thereof |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59159869A (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61152779A (en) * | 1984-12-27 | 1986-07-11 | Toyo Ink Mfg Co Ltd | Repeatedly releasable type pressure-sensitive adhesive composition |
JPH0684490B2 (en) * | 1985-05-15 | 1994-10-26 | ニチバン株式会社 | Removable adhesive composition |
JPH0684491B2 (en) * | 1985-05-15 | 1994-10-26 | ニチバン株式会社 | Removable adhesive composition |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS502736A (en) * | 1973-04-06 | 1975-01-13 |
-
1983
- 1983-03-03 JP JP3384383A patent/JPS59159869A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS502736A (en) * | 1973-04-06 | 1975-01-13 |
Also Published As
Publication number | Publication date |
---|---|
JPS59159869A (en) | 1984-09-10 |
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