JPH0127116B2 - - Google Patents
Info
- Publication number
- JPH0127116B2 JPH0127116B2 JP12786279A JP12786279A JPH0127116B2 JP H0127116 B2 JPH0127116 B2 JP H0127116B2 JP 12786279 A JP12786279 A JP 12786279A JP 12786279 A JP12786279 A JP 12786279A JP H0127116 B2 JPH0127116 B2 JP H0127116B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- vinyl acetate
- acetate copolymer
- ethylene
- parts
- 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
Links
- 229920001577 copolymer Polymers 0.000 claims description 51
- 230000001070 adhesive effect Effects 0.000 claims description 48
- 239000000853 adhesive Substances 0.000 claims description 46
- 229920002554 vinyl polymer Polymers 0.000 claims description 33
- -1 aromatic vinyl compound Chemical group 0.000 claims description 29
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 21
- 239000005977 Ethylene Substances 0.000 claims description 21
- 125000000816 ethylene group Chemical group [H]C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 21
- 239000000203 mixture Substances 0.000 claims description 21
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 claims description 10
- 150000001732 carboxylic acid derivatives Chemical group 0.000 claims description 10
- 238000006243 chemical reaction Methods 0.000 claims description 8
- 150000001993 dienes Chemical class 0.000 claims description 7
- 229920006026 co-polymeric resin Polymers 0.000 claims description 6
- 229920001169 thermoplastic Polymers 0.000 claims description 6
- 239000004416 thermosoftening plastic Substances 0.000 claims description 6
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 35
- 238000000034 method Methods 0.000 description 15
- 229920000642 polymer Polymers 0.000 description 14
- 229910052751 metal Inorganic materials 0.000 description 12
- 239000002184 metal Substances 0.000 description 12
- 239000002245 particle Substances 0.000 description 12
- 229920005989 resin Polymers 0.000 description 10
- 239000011347 resin Substances 0.000 description 10
- 239000008188 pellet Substances 0.000 description 9
- 239000003505 polymerization initiator Substances 0.000 description 9
- 239000011888 foil Substances 0.000 description 8
- 150000002739 metals Chemical class 0.000 description 8
- 229920005990 polystyrene resin Polymers 0.000 description 8
- 239000004793 Polystyrene Substances 0.000 description 7
- 229920002223 polystyrene Polymers 0.000 description 7
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- 150000008064 anhydrides Chemical class 0.000 description 6
- 239000007900 aqueous suspension Substances 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 6
- 229920001971 elastomer Polymers 0.000 description 6
- 239000005038 ethylene vinyl acetate Substances 0.000 description 6
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 5
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 5
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 5
- 229910052782 aluminium Inorganic materials 0.000 description 5
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 5
- MTAZNLWOLGHBHU-UHFFFAOYSA-N butadiene-styrene rubber Chemical compound C=CC=C.C=CC1=CC=CC=C1 MTAZNLWOLGHBHU-UHFFFAOYSA-N 0.000 description 5
- 239000000806 elastomer Substances 0.000 description 5
- 238000001125 extrusion Methods 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- 238000005470 impregnation Methods 0.000 description 4
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 4
- 238000006116 polymerization reaction Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical compound C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 description 3
- 238000010559 graft polymerization reaction Methods 0.000 description 3
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 3
- 238000003475 lamination Methods 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- QEQBMZQFDDDTPN-UHFFFAOYSA-N (2-methylpropan-2-yl)oxy benzenecarboperoxoate Chemical compound CC(C)(C)OOOC(=O)C1=CC=CC=C1 QEQBMZQFDDDTPN-UHFFFAOYSA-N 0.000 description 2
- BTOVVHWKPVSLBI-UHFFFAOYSA-N 2-methylprop-1-enylbenzene Chemical compound CC(C)=CC1=CC=CC=C1 BTOVVHWKPVSLBI-UHFFFAOYSA-N 0.000 description 2
- KFGFVPMRLOQXNB-UHFFFAOYSA-N 3,5,5-trimethylhexanoyl 3,5,5-trimethylhexaneperoxoate Chemical compound CC(C)(C)CC(C)CC(=O)OOC(=O)CC(C)CC(C)(C)C KFGFVPMRLOQXNB-UHFFFAOYSA-N 0.000 description 2
- JLBJTVDPSNHSKJ-UHFFFAOYSA-N 4-Methylstyrene Chemical compound CC1=CC=C(C=C)C=C1 JLBJTVDPSNHSKJ-UHFFFAOYSA-N 0.000 description 2
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-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
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- 239000004831 Hot glue Substances 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- 239000002174 Styrene-butadiene Substances 0.000 description 2
- 238000000862 absorption spectrum Methods 0.000 description 2
- XECAHXYUAAWDEL-UHFFFAOYSA-N acrylonitrile butadiene styrene Chemical compound C=CC=C.C=CC#N.C=CC1=CC=CC=C1 XECAHXYUAAWDEL-UHFFFAOYSA-N 0.000 description 2
- 239000004676 acrylonitrile butadiene styrene Substances 0.000 description 2
- 239000012790 adhesive layer Substances 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 239000012736 aqueous medium Substances 0.000 description 2
- 235000019400 benzoyl peroxide Nutrition 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 150000001735 carboxylic acids Chemical class 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 229920005669 high impact polystyrene Polymers 0.000 description 2
- 239000004797 high-impact polystyrene Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 239000011115 styrene butadiene Substances 0.000 description 2
- 229920003048 styrene butadiene rubber Polymers 0.000 description 2
- 239000000375 suspending agent Substances 0.000 description 2
- 238000010557 suspension polymerization reaction Methods 0.000 description 2
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- JHPBZFOKBAGZBL-UHFFFAOYSA-N (3-hydroxy-2,2,4-trimethylpentyl) 2-methylprop-2-enoate Chemical compound CC(C)C(O)C(C)(C)COC(=O)C(C)=C JHPBZFOKBAGZBL-UHFFFAOYSA-N 0.000 description 1
- UICXTANXZJJIBC-UHFFFAOYSA-N 1-(1-hydroperoxycyclohexyl)peroxycyclohexan-1-ol Chemical compound C1CCCCC1(O)OOC1(OO)CCCCC1 UICXTANXZJJIBC-UHFFFAOYSA-N 0.000 description 1
- XMNIXWIUMCBBBL-UHFFFAOYSA-N 2-(2-phenylpropan-2-ylperoxy)propan-2-ylbenzene Chemical compound C=1C=CC=CC=1C(C)(C)OOC(C)(C)C1=CC=CC=C1 XMNIXWIUMCBBBL-UHFFFAOYSA-N 0.000 description 1
- 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
- SBYMUDUGTIKLCR-UHFFFAOYSA-N 2-chloroethenylbenzene Chemical compound ClC=CC1=CC=CC=C1 SBYMUDUGTIKLCR-UHFFFAOYSA-N 0.000 description 1
- WFUGQJXVXHBTEM-UHFFFAOYSA-N 2-hydroperoxy-2-(2-hydroperoxybutan-2-ylperoxy)butane Chemical compound CCC(C)(OO)OOC(C)(CC)OO WFUGQJXVXHBTEM-UHFFFAOYSA-N 0.000 description 1
- CEBRPXLXYCFYGU-UHFFFAOYSA-N 3-methylbut-1-enylbenzene Chemical compound CC(C)C=CC1=CC=CC=C1 CEBRPXLXYCFYGU-UHFFFAOYSA-N 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- YIVJZNGAASQVEM-UHFFFAOYSA-N Lauroyl peroxide Chemical compound CCCCCCCCCCCC(=O)OOC(=O)CCCCCCCCCCC YIVJZNGAASQVEM-UHFFFAOYSA-N 0.000 description 1
- 229920001890 Novodur Polymers 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- SQHOHKQMTHROSF-UHFFFAOYSA-N but-1-en-2-ylbenzene Chemical compound CCC(=C)C1=CC=CC=C1 SQHOHKQMTHROSF-UHFFFAOYSA-N 0.000 description 1
- MPMBRWOOISTHJV-UHFFFAOYSA-N but-1-enylbenzene Chemical compound CCC=CC1=CC=CC=C1 MPMBRWOOISTHJV-UHFFFAOYSA-N 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 229910000389 calcium phosphate Inorganic materials 0.000 description 1
- 235000011010 calcium phosphates Nutrition 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- LSXWFXONGKSEMY-UHFFFAOYSA-N di-tert-butyl peroxide Chemical compound CC(C)(C)OOC(C)(C)C LSXWFXONGKSEMY-UHFFFAOYSA-N 0.000 description 1
- QZYRMODBFHTNHF-UHFFFAOYSA-N ditert-butyl benzene-1,2-dicarboperoxoate Chemical compound CC(C)(C)OOC(=O)C1=CC=CC=C1C(=O)OOC(C)(C)C QZYRMODBFHTNHF-UHFFFAOYSA-N 0.000 description 1
- GVGUFUZHNYFZLC-UHFFFAOYSA-N dodecyl benzenesulfonate;sodium Chemical compound [Na].CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 GVGUFUZHNYFZLC-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 125000005843 halogen group Chemical group 0.000 description 1
- 239000008240 homogeneous mixture Substances 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 230000005865 ionizing radiation Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 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
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229920000609 methyl cellulose Polymers 0.000 description 1
- 239000001923 methylcellulose Substances 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
- SRSFOMHQIATOFV-UHFFFAOYSA-N octanoyl octaneperoxoate Chemical compound CCCCCCCC(=O)OOC(=O)CCCCCCC SRSFOMHQIATOFV-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000005502 peroxidation Methods 0.000 description 1
- 229920001084 poly(chloroprene) Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 229920000036 polyvinylpyrrolidone Polymers 0.000 description 1
- 239000001267 polyvinylpyrrolidone Substances 0.000 description 1
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000007870 radical polymerization initiator Substances 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 150000003440 styrenes Chemical class 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 229920003051 synthetic elastomer Polymers 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 239000005061 synthetic rubber Substances 0.000 description 1
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 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
- 235000019731 tricalcium phosphate Nutrition 0.000 description 1
- 229920006163 vinyl copolymer Polymers 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Adhesives Or Adhesive Processes (AREA)
Description
本発明は、スチレン系樹脂と金属の貼合せに好
適な新規な接着剤組成物に関し、詳しくは耐衝撃
ポリスチレン(HIPS)、アクリロニトリル・ブ
タジエン・スチレン共重合体(ABS)などのス
チレン系樹脂とアルミニウム、鉄などの金属との
貼合せ用に用いることのできるホツトメルト型接
着剤組成物に関するものである。
一般にスチレン系樹脂は他樹脂、他材料との接
着性に乏しく、接着剤の選定が非常にむずかし
い。現在よく用いられる接着剤としては酢酸ビニ
ル樹脂やネオプレンゴム等の合成樹脂、合成ゴム
を溶剤に溶解した溶剤型接着剤、あるいはエポキ
シ系やポリエステル系などの反応硬化型接着剤が
ある。前者の場合は溶剤型であり、接着後の乾燥
が必要であるため、溶剤取扱いに伴なう公害、安
全衛生面の問題及び溶剤によるポリスチレン系樹
脂表面の化学劣化に伴なう品質への影響、更には
脱溶剤のためのオープンタイムが長い等、種々の
問題点を有している。また後者の反応硬化型の場
合は硬化剤の配合、塗布等が必要となりアプリケ
ーターに工夫がいること、ポツトライフが短か
く、接着剤の適用範囲がせまいこと、更には接着
層が三次元構造を形成するため剪断接着力と剥離
接着力のバランスが悪い等、種々の問題点を有し
ている。
本発明の第一の目的は、スチレン系樹脂と金属
の貼合せに十分な接着力を与えるホツトメルト型
接着剤組成物を提供するにある。
本発明の第二の目的は、ポツトライフが半永久
的であり、フイルム状、ペレツト状等の所望の状
態で保存することができ、接着プロセスに最適の
形式を選択しうる接着剤組成物を提供するにあ
る。
本発明の第三の目的は、剪断接着強度と剥離接
着強度のバランスの良好な接着剤組成物を提供す
るにある。
本発明は上記の目的を達成するものであつて、
次の3種類の樹脂
(a) エチレン・酢酸ビニル共重合体と芳香族ビニ
ル化合物をグラフト反応条件に付して得られ
る、芳香族ビニル化合物単位濃度が10〜70重量
%の改質エチレン・酢酸ビニル共重合体を10〜
100重量%の割合で含むエチレン・酢酸ビニル
共重合体樹脂60〜95重量部、
(b) 共役ジオレフインと芳香族ビニル化合物より
なる熱可塑性ブロツク弾性共重合体樹脂5〜40
重量部、および
(c) エチレン・酢酸ビニル共重合体とエチレン性
不飽和カルボン酸をグラフト反応条件に付して
得られる、エチレン性不飽和カルボン酸単位濃
度が0.01〜10重量%の改質エチレン・酢酸ビニ
ル共重合体を0.5〜100重量%の割合で含むエチ
レン・酢酸ビニル共重合体樹脂の(a)+(b)100重
量部に対して5〜50重量部
を配合してなることを特徴とする接着剤組成物で
ある。
以下本発明を各項に分けて具体的に説明する。
(1) 芳香族ビニル化合物改質エチレン・酢酸ビニ
ル共重合体
この共重合体は、芳香族ビニル化合物とエチレ
ン・酢酸ビニル共重合体をグラフト反応条件に付
して得られるが、好適には次の方法で得られる。
即ち、酢酸ビニル含量が2〜50重量%でメルトイ
ンデツクスが0.1〜200g/10分のエチレン・酢酸
ビニル重合体粒子100重量部と芳香族ビニル化合
物5〜230重量部、および10時間の半減期を得る
ための分解温度が50〜130℃であるラジカル重合
開始剤を芳香族ビニル化合物100重量部に対し
0.01〜5.0重量部を、水性懸濁重合に使用される
懸濁剤、例えばポリビニルアルコール、ポリビニ
ルピロリドン、メチルセルロースその他、或は難
溶性無機物質例えばリン酸カルシウム、酸化マグ
ネシウムその他の存在下に、水性媒体中に系のか
くはんが容易に行われる任意の濃度で(一般に水
100重量部に対して重合体および芳香族ビニル化
合物5〜100重量部)添加し、かくはん分散する。
次いでこの水性懸濁液を使用重合開始剤の分解が
実質的におこらない範囲内で加熱して、芳香族ビ
ニル化合物を重合体粒子中に含浸させる。含浸処
理は含浸促進の点から考えれば加熱温度は高い方
が良いが、重合開始剤の過早分解によつて含浸前
の芳香族ビニル化合物が単独で重合するのを防止
する点からは加熱温度は低い方が良く、好ましく
は室温から50℃である。このような温度条件に芳
香族ビニル化合物の80重量%以上、好ましくは90
重量%以上が重合体粒子中に含浸または附着され
る迄、すなわち遊離の芳香族ビニル化合物液滴が
20重量%、好ましくは10重量%未満の量となるま
で、水性懸濁液を好ましくはかくはん下に1〜5
時間程度放置する。未含浸の芳香族ビニル化合物
が20重量%以上の場合には、独立のビニル重合体
粒子が析出する可能性があり、また重合体粒子中
のビニル重合体の分散が不均一となる。なお、遊
離の芳香族ビニル化合物は次の重合工程において
重合体粒子内に含浸され、或は重合体粒子表面に
附着して重合するため、生成物中にはビニル重合
体粒子がエチレン・酢酸ビニル共重合体粒子と独
立して存在することは事実上認められない。この
ようにして用意した水性懸濁液を更に高温に加熱
して芳香族ビニル化合物の重合を完成させること
により、改質エチレン・酢酸ビニル共重合体が得
られる。この際加熱温度は使用重合開始剤の充分
な分解が生じる温度であるべきである。しかし
130℃を越えないことが好ましい。130℃を越える
と生成改質重合体中にゲル状物質が生じる傾向が
ある。一般には50〜130℃の温度が適当である。
芳香族ビニル化合物としては、一般式
(式中R1は水素原子または炭素数1〜4のア
ルキル基、R2〜R6はそれぞれ単独に水素原子、
塩素原子または炭素数1〜4のアルキル基を示
す)で表わされるスチレン系モノマー、たとえば
スチレン、核置換スチレンたとえばメチルスチレ
ン、ジメチルスチレン、エチルスチレン、イソプ
ロピルスチレン、およびクロルスチレン、α置換
スチレン例えばαメチルスチレン、およびαエチ
ルスチレンなどが挙げられる。またスチレンとア
クリル酸エステル、スチレンとメタクリル酸エス
テル、スチレンとアクリロニトリルなどの混合系
も適用される。
重合開始剤としては、水性懸濁重合の技術に従
うものによるため油溶性のものが使用される。重
合開始剤は10時間の半減期を得るための分解温度
が50〜130℃であるものでなければならない。特
に55〜110℃の範囲内にあるのが好ましい。50℃
未満では含浸工程中に芳香族ビニルモノマーの重
合が生じるため均質な生成物が得られない。130
℃以上では生成物にゲルが生じ物性上好まくな
い。これは過度に温度を上げる結果、該エチレ
ン・酢酸ビニル共重合体の分子間架橋反応が起き
るためと考えられる。重合開始剤の具体例として
は、オクタノイルパーオキサイド、ベンゾイルパ
ーオキサイド、シクロヘキサノンパーオキサイ
ド、t―ブチルパーオキシベンゾエート、メチル
エチルケトンパーオキサイド、ジクミルパーオキ
サイド、ジ―t―ブチルパーオキサイド、2,5
―ジメチル―2,5―ジベンゾイルパーオキシヘ
キサン、ジ―t―ブチル―ジ―パーオキシフタレ
ート、ラウロイルパーオキサイド、t―ブチルパ
ーオキシピパレート、3,5,5―トリメチルヘ
キサノイルパーオキサイドなどが挙げられる。重
合開始剤の使用量は芳香族ビニル化合物100重量
部に対して0.01〜5.0重量部である。
このようにして得られた芳香族ビニル化合物改
質エチレン・酢酸ビニル共重合体は、芳香族ビニ
ル化合物単位濃度が10〜70重量%のものであり、
本発明においてはこれを10〜100重量%の割合で
含むエチレン・酢酸ビニル共重合体として用いる
ものである。
この芳香族ビニル化合物改質エチレン・酢酸ビ
ニル共重合体の芳香族ビニル化合物濃度が10重量
%未満では、上記(b)成分との良好な相溶性が得ら
れず、また、組成物として特にポリスチレン系樹
脂に対しての十分な接着強度が得られない。一
方、70重量%超過では、接着剤自体が硬くなるた
め、接着剤としての物性を損ねることとなる。
また、(a)成分における配合量が10重量%未満で
は、特にポリスチレン系樹脂に対しての接着強度
の改良効果が見られないほか、上記(b)成分との相
溶性も悪化して層剥離等の原因となる傾向があ
る。
(2) 熱可塑性ブロツク弾性体
共役ジオレフインと芳香族ビニル化合物よりな
る一般式が次式で表わされる熱可塑性ブロツク弾
性体であり、例えば特公昭42−17492号公報の方
法で作られるものである。
(A−B)n+1、B−(A−B)n+1、
A−B−(B−A)n+1および/または
A−(B−A)n。
ここにAは芳香族ビニル化合物よりなる非弾性
的なポリマーブロツクを表わし、Bは共役ジオレ
フインの弾性的ポリマーブロツクを表わす。ま
た、nは1から20の整数を表わし、Aブロツクの
全体の分子に占める割合は1〜50重量%である。
この弾性体の平均分子量は10000ないし1000000
好ましくは50000ないし250000である。本発明に
使用される共役ジオレフインとしては、1,3―
ブタジエン、イソプレン、n―1―3―ペンタジ
エン等が使用される。更に芳香族ビニル化合物と
してはスチレン、メチルスチレン、ジメチルスチ
レン等が使用される。なお、共役ジオレフイン重
合体ブロツクを水添した熱可塑性ブロツク弾性体
も本発明に適用される。
(3) エチレン性不飽和カルボン酸またはその無水
物改質エチレン・酢酸ビニル共重合体
好適には酢酸ビニル含量が2〜50重量%でメル
トインデツクスが0.1〜200g/10分のエチレン・
酢酸ビニル共重合体をエチレン性不飽和カルボン
酸またはその無水物で変性するものであつて、後
者をグラフト重合することによつて改質する。
エチレン性不飽和カルボン酸またはその無水物
としてはアクリル酸、マレイン酸、イタコン酸、
ハイミツク酸またはこれらの無水物が適用され
る。特に無水マレイン酸、アクリル酸を用いるこ
とが好ましい。
エチレン・酢酸ビニル共重合体をこれらエチレ
ン性不飽和カルボン酸またはその無水物で改質す
るにはイオン化性放射線、紫外線等の照射による
方法、ラジカル開始剤を使用する方法、酸素、オ
ゾン、熱等の作用で過酸化する方法、混練機中で
熱と剪断力を利用する方法等種々の開始方法によ
つてグラフト重合をおこなう。該グラフト重合
は、溶液状態、スラリー状態、溶融状態等公知の
方法でおこなうことができる。
このようにしてえられた改質エチレン・酢酸ビ
ニル共重合体は、エチレン性不飽和カルボン酸単
位濃度が0.01〜10重量%のものであり、本発明に
おいてはこれを0.5〜100重量%の割合で含むエチ
レン・酢酸ビニル共重合体として用いるものであ
る。
この改質エチレン・酢酸ビニル共重合体のエチ
レン性不飽和カルボン酸単位濃度が0.01重量%未
満では、特に金属に対しての十分な接着強度が得
られず、一方、10重量%超過のものを得ようとす
ると、架橋ゲルや劣化を生じて好ましくない。
また、これの(c)成分中への配合量が0.5重量%
未満では、特に金属に対しての接着強度が劣り好
ましくない。
エチレン性不飽和カルボン酸またはこの無水物
を作用して改質する場合、変性を受けないエチレ
ン・酢酸ビニル共重合体が残存することがある。
このような未改質エチレン・酢酸ビニル共重合体
は、上記の改質エチレン・酢酸ビニル共重合体に
配合したものとして取扱う。
本発明の接着剤組成物は特にポリスチレン系樹
脂に対してすぐれた接着性を示す。ここでポリス
チレン系樹脂とは下記一般式で示される構造単位
を樹脂中に少くとも25重量%以上含有する樹脂で
ある。
(ここでRは水素原子またはメチル基を、Zは
ハロゲン原子またはメチル基を、pは0または1
〜3の整数である。)
具体的にはポリスチレン、ゴム変性ポリスチレ
ン、スチレン・アクリルニトリル共重合体、スチ
レン・ブタジエン・アクリルニトリル共重合体、
スチレン・ブタジエン・メチルメタアクリレート
共重合体、スチレン・αオレフインゴム・アクリ
ルニトリル共重合体、スチレン・αメチルスチレ
ン共重合体などで例示されるスチレンおよびその
誘導体の単独重合体および共重合体が挙げられ
る。特にポリスチレン、ゴム変性ポリスチレン、
スチレン・ブタジエン・アクリルニトリル共重合
体が好ましい。
以上に述べた本発明の接着剤組成物の各構成成
分は以下の様な配合で実施される。即ち、(a)芳香
族ビニル化合物単位濃度が10〜70重量%の改質エ
チレン・酢酸ビニル共重合体を10〜100重量%の
割合で含むエチレン・酢酸ビニル共重合体60〜95
重量%と、(b)共役ジオレフインと芳香族ビニル化
合物よりなる(b)熱可塑性ブロツク弾性体5〜40重
量%とからなる樹脂100重量部に対し、(c)エチレ
ン性不飽和カルボン酸単位濃度が0.01〜10重量%
の改質エチレン・酢酸ビニル共重合体を0.5〜100
重量%の割合で含むエチレン・酢酸ビニル共重合
体を5〜50重量部配合したものである。
ここで、(a)成分が95重量%超過、すなわち(b)成
分が5重量%未満では、特にポリスチレン系樹脂
に対しての接着強度が十分で無く、一方、(a)成分
が60重量%未満、すなわち(b)成分が40重量%超過
では、押出成形性を損ねる欠点を有する。また、
(c)成分が5重量部未満では、特に金属との接着性
が劣り、一方、50重量部超過では、金属との接着
強度の改質効果が飽和するばかりでなく、逆にポ
リスチレン系樹脂との接着強度が低下して好まし
くない。
以上のように、本発明はおのおの異なる接着特
性を有する3つの成分が均質に混合されており、
ポリスチレン系樹脂および金属の双方にきわめて
優れた接着性を示す接着剤組成物であり、その均
質性の故に、溶融混練してフイルム状、シート
状、粒状、ペレツト状に自由に成形することがで
きる。溶融混練法としては、押出機、バンバリ
ー、ロール等の公知の方法を用いることができ
る。この種の方法によつて均質化した接着剤組成
物は、インフレーシヨン法、T―ダイ法等の公知
のフイルム成形法によりフイルム状に成形し、フ
イルム状接着剤として使用することができる。ま
た押出機等によつてペレツト状にし、ペレツト状
の接着剤として使用するか、機械粉砕、化学粉砕
等の公知の手法によつて微粉化し、粉状接着剤と
して使用し、ポリスチレン系樹脂と金属を積層す
ることが出来る。また本発明の接着性組成物とポ
リスチレン系樹脂を公知のダイ内、ダイ外ラミネ
ート法などの共押出法で積層し、接着剤層面に金
属を圧着積層することもできる。
積層の際の加熱温度は、各樹脂の融点以上、分
解温度以下すなわち70〜300℃、好ましくは100〜
250℃であり、圧力は1Kg/cm2以上、150Kg/cm2以
下、好ましくは10〜50Kg/cm2でおこなうことが望
ましい。また本発明の接着剤は上記の性能から見
て、ポリスチレン系樹脂同志、または金属と金属
との間の接着剤としてもも使用し得ることは自明
である。また接着に当つては必ずしもベタ付(積
層型)による必要はなく、場合によつては必要個
所を点接着することもできる。
以下、本発明の実施例について説明する。
実施例 1
内容量50のオートクレーブ内に純水20Kg及び
懸濁剤として第三リン酸カルシウム600gとドデ
シルベンゼンスルホン酸ナトリウム0.65gとを加
えて水性媒質となし、これにエチレン・酢酸ビニ
ル共重合体(MI12゜、密度0.948、酢酸ビニル含量
20重量%)粒子6Kgをかくはんにより懸濁させ
た。別に重合開始剤として過酸化ベンゾイル8g
およびt―ブチルパーオキシベンゾエート4gを
スチレン4Kg(エチレン・酢酸ビニル共重合体に
対し60重量%)に溶解させ、これを前記懸濁系に
投入し、オートクレーブ内温度を45℃に昇温さ
せ、該温度で3時間保持して重合開始剤を含むス
チレンをエチレン・酢酸ビニル共重合体粒子中に
含浸させた。
この水性懸濁液を80℃に昇温し、該温度で5時
間、更に125℃で5時間維持して重合を完結させ
た。得られた改質粒子中にはポリスチレンがほぼ
定量的に60重量%存在することが確認された。ま
た、エチレン・酢酸ビニル共重合体(MI12゜、密
度0.948、酢酸ビニル含量20重量%)に2,5―
ジメチル―ヘキサン―2,5―ジハイドロパーオ
キサイド0.6重量%と無水マレイン酸1.0重量%を
ヘンシエルミキサーを用いて充分に混合し、40mm
φ押出機(L/D=28)を用いて押出温度150℃
でペレツト化した。得られたペレツトを粉砕後、
アセトンにて未反応の無水マレイン酸を充分抽出
したのち、赤外線吸収スペクトルによつて0.76重
量%の無水マレイン酸が付加していることを確認
した。以上のようにして得られたスチレン改質エ
チレ・酢酸ビニル共重合体と無水マレイン酸改質
エチレン・酢酸ビニル共重合体と、スチレン・ブ
タジエンブロツク弾性体(シエル化学社、カリフ
レツクスTR−1102)および/または未変性エチ
レン・酢酸ビニル共重合体を所定量ブレンドし、
40mmφ押出機にて160℃の温度で溶融混練し、均
質に混合されたペレツトを得た。このペレツトを
Tダイフイルム成形機を用いて厚み50μのフイル
ムに成形し、このフイルムを接着剤として、別途
作製したABS樹脂(三菱モンモント社、タフレ
ツクス410)の1mm厚シートと50μ厚のアルミ箔
をヒートシーラーを用いて熱圧着した。ヒートシ
ール条件は、温度160℃、圧力1.4Kg/cm2、時間10
秒である。圧着面積は200mm×15mmである。この
ようにして得られたABS樹脂/アルミ箔積層物
を20mm巾にカツトし、180℃剥離テストを行なつ
た(剥離スピード500mm/分)。結果を表−1に示
す。
比較例 1
実施例1において接着剤としてエチレン・酢酸
ビニル共重合体のみを用いた結果を表−1に示
す。
比較例 2
実施例1において、接着剤として該スチレン改
質エチレン・酢酸ビニル共重合体のみを用いた結
果を表−1に示す。
比較例 3
実施例1において、接着剤として該スチレン改
質エチレン・酢酸ビニル共重合体80重量%とブロ
ツク弾性体(シエル化学社、カリフレツクス、
TR−1102)20重量%のブレンド物を用いた結果
を表−1に示す。
比較例 4
実施例1において、接着剤として該無水マレイ
ン酸改質エチレン・酢酸ビニル共重合体を用いた
結果を表−1に示す。
比較例 5
実施例1において、接着剤として該スチレン改
質エチレン・酢酸ビニル共重合体100重量部と該
無水マレイン酸改質エチレン・酢酸ビニル共重合
体20重量部のブレンド物を用いた結果を表−1に
示す。
実施例 2
実施例1において、スチレン3Kgとアクリルニ
トリル1Kgを用いて重合したスチレン・アクリル
ニトリル改質エチレン・酢酸ビニル共重合体と、
スチレン・ブタジエンブロツク弾性体(旭化成、
タフプレン)と、無水マレイン酸改質エチレン・
酢酸ビニル共重合体とを所定量ブレンドした接着
剤を、50mmφラミネーターを用いて210℃の押出
温度で50μのアルミ箔上に30μの厚さで押出ラミ
ネートした。この接着剤がコートされたアルミ箔
とABS樹脂の0.5mm厚シートとをプレス成形機に
て、温度200℃、圧力10Kg/cm2の条件下で熱圧着
し、20mm巾の180゜剥離テスト(剥離スピード500
mm/分)を行なつた。結果を表−2に示す。また
このものを0℃の低温下、90゜の折れ曲げテスト
を行なつたが、曲げR部分での剥離現象もみられ
ず、低温でも良好な接着性を有することが確認さ
れた。
比較例 6
実施例2において、接着剤としてエチレン・酢
酸ビニル共重合体100重量部と無水マレイン酸改
質エチレン・酢酸ビニル共重合体20重量部のブレ
ンド物を用いた結果を表−2に示す。
実施例 3
エチレン・酢酸ビニル共重合体(MI4、密度
0.938、酢酸ビニル含量15重量%)100部をトルエ
ンに懸濁させ、これにアクリル酸3部を添加し、
室温にて30分間かくはんした。その後かくはんし
ながら100℃迄昇温し、3,5,5―トリメチル
ヘキサノイルパーオキサイド2部をトルエンに希
釈し、30分で滴下した。滴下後2時間30分100℃
に保持し反応を続けた。反応完了後、過剰のアセ
トンを用いてポリマーを再沈し、かつ未反応モノ
マーを充分に除き、遠心分離によつて粉末状ポリ
マーを得た。このポリマーのアクリル酸含量を赤
外線吸収スペクトルによつて定量したところ、
0.9重量%のアクリル酸が付加していた。このよ
うにして得られたアクリル酸改質エチレン・酢酸
ビニル共重合体と実施例1に用いたエチレン改質
エチレン・酢酸ビニル共重合体及びスチレン・ブ
タジエンブロツク弾性体を所定量配合し、40mmφ
押出機(L/D=28)を用いて190℃で溶融混練
して均質なペレツトを得た。このペレツトをTダ
イフイルム成形機を用いて厚み50μのフイルムに
成形し、このフイルムを接着剤として、別途作製
したゴム変性ポリスチレン(三菱モンサント社、
ダイヤレツクスHT190)の1mm厚シートと金属
箔をプレス成形によつて、接着条件140℃、40
Kg/cm2、3分間で貼合せて、180゜剥離強度を測定
した。結果を表−3に示す。(箔として、鋼箔、
Al箔を使用)
The present invention relates to a new adhesive composition suitable for bonding styrene resin and metal, and more specifically, styrenic resin such as high impact polystyrene (HIPS), acrylonitrile-butadiene-styrene copolymer (ABS), and aluminum. , relates to a hot melt adhesive composition that can be used for lamination with metals such as iron. Generally, styrene resins have poor adhesion with other resins and materials, making it extremely difficult to select an adhesive. Adhesives commonly used at present include synthetic resins such as vinyl acetate resin and neoprene rubber, solvent-based adhesives in which synthetic rubber is dissolved in a solvent, and reaction-curing adhesives such as epoxy and polyester adhesives. In the case of the former, it is solvent-based and requires drying after adhesion, resulting in pollution and health and safety issues associated with handling the solvent, as well as the impact on quality due to chemical deterioration of the polystyrene resin surface caused by the solvent. Furthermore, it has various problems such as long open time for solvent removal. In addition, in the case of the latter reaction-curing type, it is necessary to mix and apply a curing agent, which requires ingenuity in the applicator, the pot life is short, the range of application of the adhesive is narrow, and the adhesive layer forms a three-dimensional structure. Therefore, it has various problems such as poor balance between shear adhesive strength and peel adhesive strength. The first object of the present invention is to provide a hot melt adhesive composition that provides sufficient adhesive strength for bonding styrene resin and metal. A second object of the present invention is to provide an adhesive composition that has a semi-permanent pot life, can be stored in a desired form such as film or pellet form, and allows the selection of the most suitable form for the adhesion process. It is in. A third object of the present invention is to provide an adhesive composition with a good balance between shear adhesive strength and peel adhesive strength. The present invention achieves the above objects,
The following three types of resins (a) Modified ethylene/acetic acid with an aromatic vinyl compound unit concentration of 10 to 70% by weight, obtained by subjecting an ethylene/vinyl acetate copolymer and an aromatic vinyl compound to graft reaction conditions. Vinyl copolymer from 10 to
60 to 95 parts by weight of an ethylene/vinyl acetate copolymer resin containing 100% by weight; (b) 5 to 40 parts by weight of a thermoplastic block elastic copolymer resin consisting of a conjugated diolefin and an aromatic vinyl compound;
parts by weight, and (c) modified ethylene with an ethylenically unsaturated carboxylic acid unit concentration of 0.01 to 10% by weight, obtained by subjecting an ethylene/vinyl acetate copolymer and an ethylenically unsaturated carboxylic acid to graft reaction conditions.・It is made by blending 5 to 50 parts by weight to 100 parts by weight of (a) + (b) of ethylene/vinyl acetate copolymer resin containing vinyl acetate copolymer at a ratio of 0.5 to 100% by weight. This is a characteristic adhesive composition. Hereinafter, the present invention will be explained in detail by dividing into each section. (1) Aromatic vinyl compound-modified ethylene/vinyl acetate copolymer This copolymer is obtained by subjecting an aromatic vinyl compound and an ethylene/vinyl acetate copolymer to graft reaction conditions, but preferably the following It can be obtained by the following method.
That is, 100 parts by weight of ethylene-vinyl acetate polymer particles with a vinyl acetate content of 2 to 50% by weight and a melt index of 0.1 to 200 g/10 minutes, 5 to 230 parts by weight of an aromatic vinyl compound, and a half-life of 10 hours. Add a radical polymerization initiator with a decomposition temperature of 50 to 130°C to obtain 100 parts by weight of the aromatic vinyl compound.
0.01 to 5.0 parts by weight in an aqueous medium in the presence of suspending agents used in aqueous suspension polymerization, such as polyvinyl alcohol, polyvinylpyrrolidone, methylcellulose, etc., or sparingly soluble inorganic substances, such as calcium phosphate, magnesium oxide, etc. at any concentration where the system is easily agitated (generally water
5 to 100 parts by weight of the polymer and aromatic vinyl compound are added to 100 parts by weight, and the mixture is stirred and dispersed.
This aqueous suspension is then heated within a range that does not substantially cause decomposition of the polymerization initiator used to impregnate the aromatic vinyl compound into the polymer particles. In impregnation treatment, the higher the heating temperature, the better from the viewpoint of promoting impregnation, but from the viewpoint of preventing the aromatic vinyl compound before impregnation from polymerizing alone due to premature decomposition of the polymerization initiator, the heating temperature is higher. The lower the temperature, the better, preferably between room temperature and 50°C. At least 80% by weight of the aromatic vinyl compound, preferably 90% by weight, under such temperature conditions.
Until more than % by weight of the aromatic vinyl compound droplets are impregnated or attached to the polymer particles, that is, free aromatic vinyl compound droplets are
The aqueous suspension is dissolved, preferably with stirring, in an amount of 1 to 5% by weight, preferably less than 20% by weight, preferably less than 10% by weight.
Leave it for about an hour. If the amount of unimpregnated aromatic vinyl compound is 20% by weight or more, independent vinyl polymer particles may be precipitated, and the vinyl polymer in the polymer particles may be non-uniformly dispersed. In addition, free aromatic vinyl compounds are impregnated into the polymer particles in the next polymerization step or attached to the surface of the polymer particles and polymerized, so the vinyl polymer particles are mixed with ethylene/vinyl acetate in the product. It is practically not recognized that it exists independently of the copolymer particles. A modified ethylene/vinyl acetate copolymer can be obtained by further heating the aqueous suspension prepared in this way to a high temperature to complete polymerization of the aromatic vinyl compound. In this case, the heating temperature should be such that sufficient decomposition of the polymerization initiator used occurs. but
Preferably, the temperature does not exceed 130°C. When the temperature exceeds 130°C, gel-like substances tend to form in the resulting modified polymer. Generally, a temperature of 50 to 130°C is suitable. As an aromatic vinyl compound, the general formula (In the formula, R 1 is a hydrogen atom or an alkyl group having 1 to 4 carbon atoms, R 2 to R 6 are each independently a hydrogen atom,
chlorine atom or an alkyl group having 1 to 4 carbon atoms) such as styrene, nuclear-substituted styrene such as methylstyrene, dimethylstyrene, ethylstyrene, isopropylstyrene, and chlorstyrene, α-substituted styrene such as α-methyl Examples include styrene and α-ethylstyrene. Mixed systems such as styrene and acrylic ester, styrene and methacrylic ester, and styrene and acrylonitrile are also applicable. As the polymerization initiator, an oil-soluble one is used because it follows the technique of aqueous suspension polymerization. The polymerization initiator should have a decomposition temperature of 50-130°C to obtain a half-life of 10 hours. In particular, it is preferably within the range of 55 to 110°C. 50℃
If it is less than this, polymerization of the aromatic vinyl monomer will occur during the impregnation process, making it impossible to obtain a homogeneous product. 130
If the temperature is higher than 0.degree. C., the product will form a gel, which is unfavorable in terms of physical properties. This is considered to be because an intermolecular crosslinking reaction of the ethylene/vinyl acetate copolymer occurs as a result of excessively raising the temperature. Specific examples of the polymerization initiator include octanoyl peroxide, benzoyl peroxide, cyclohexanone peroxide, t-butyl peroxybenzoate, methyl ethyl ketone peroxide, dicumyl peroxide, di-t-butyl peroxide, 2,5
-dimethyl-2,5-dibenzoyl peroxyhexane, di-t-butyl-di-peroxyphthalate, lauroyl peroxide, t-butyl peroxypiparate, 3,5,5-trimethylhexanoyl peroxide, etc. Can be mentioned. The amount of the polymerization initiator used is 0.01 to 5.0 parts by weight per 100 parts by weight of the aromatic vinyl compound. The aromatic vinyl compound-modified ethylene/vinyl acetate copolymer thus obtained has an aromatic vinyl compound unit concentration of 10 to 70% by weight,
In the present invention, this is used as an ethylene/vinyl acetate copolymer containing 10 to 100% by weight. If the aromatic vinyl compound concentration of the aromatic vinyl compound-modified ethylene/vinyl acetate copolymer is less than 10% by weight, good compatibility with the above component (b) will not be obtained, and the composition will not be suitable for polystyrene. Sufficient adhesive strength to the resin cannot be obtained. On the other hand, if it exceeds 70% by weight, the adhesive itself becomes hard, which impairs its physical properties as an adhesive. Furthermore, if the blending amount of component (a) is less than 10% by weight, there will be no improvement in adhesive strength, especially for polystyrene resins, and the compatibility with component (b) will also deteriorate, resulting in layer peeling. There is a tendency to cause such things. (2) Thermoplastic block elastic body This is a thermoplastic block elastic body whose general formula consisting of a conjugated diolefin and an aromatic vinyl compound is represented by the following formula, and is produced, for example, by the method disclosed in Japanese Patent Publication No. 17492/1983. (A-B)n+1, B-(A-B)n+1, A-B-(B-A)n+1 and/or A-(B-A)n. Here, A represents an inelastic polymer block made of an aromatic vinyl compound, and B represents an elastic polymer block of conjugated diolefin. Further, n represents an integer from 1 to 20, and the proportion of the A block to the entire molecule is 1 to 50% by weight. The average molecular weight of this elastic body is 10,000 to 1,000,000
Preferably it is 50,000 to 250,000. The conjugated diolefin used in the present invention includes 1,3-
Butadiene, isoprene, n-1-3-pentadiene, etc. are used. Further, as the aromatic vinyl compound, styrene, methylstyrene, dimethylstyrene, etc. are used. Incidentally, a thermoplastic block elastomer obtained by hydrogenating a conjugated diolefin polymer block is also applicable to the present invention. (3) Ethylene-vinyl acetate copolymer modified with ethylenically unsaturated carboxylic acid or its anhydride, preferably an ethylene-vinyl acetate copolymer with a vinyl acetate content of 2 to 50% by weight and a melt index of 0.1 to 200 g/10 min.
A vinyl acetate copolymer is modified with an ethylenically unsaturated carboxylic acid or its anhydride, and the latter is modified by graft polymerization. Ethylenically unsaturated carboxylic acids or their anhydrides include acrylic acid, maleic acid, itaconic acid,
Hymic acid or their anhydrides are applied. In particular, it is preferable to use maleic anhydride and acrylic acid. To modify the ethylene/vinyl acetate copolymer with these ethylenically unsaturated carboxylic acids or their anhydrides, there are several methods: irradiation with ionizing radiation, ultraviolet rays, etc., methods using radical initiators, oxygen, ozone, heat, etc. Graft polymerization can be carried out by various initiation methods, such as peroxidation by the action of oxidation, or use of heat and shear force in a kneader. The graft polymerization can be carried out by any known method such as in a solution state, slurry state, or melt state. The modified ethylene/vinyl acetate copolymer thus obtained has an ethylenically unsaturated carboxylic acid unit concentration of 0.01 to 10% by weight, and in the present invention, the concentration is 0.5 to 100% by weight. It is used as an ethylene/vinyl acetate copolymer containing If the concentration of ethylenically unsaturated carboxylic acid units in this modified ethylene/vinyl acetate copolymer is less than 0.01% by weight, sufficient adhesive strength cannot be obtained, especially for metals, whereas if it exceeds 10% by weight, If you try to obtain it, it will cause cross-linked gel and deterioration, which is not preferable. In addition, the amount of this added to component (c) is 0.5% by weight.
If it is less than this, the adhesive strength, especially to metals, will be poor, which is undesirable. When modifying with an ethylenically unsaturated carboxylic acid or its anhydride, an unmodified ethylene/vinyl acetate copolymer may remain.
Such an unmodified ethylene/vinyl acetate copolymer is treated as one blended with the above-mentioned modified ethylene/vinyl acetate copolymer. The adhesive composition of the present invention exhibits excellent adhesion to polystyrene resins in particular. Here, the polystyrene resin is a resin containing at least 25% by weight of a structural unit represented by the following general formula. (Here, R is a hydrogen atom or a methyl group, Z is a halogen atom or a methyl group, and p is 0 or 1
It is an integer of ~3. ) Specifically, polystyrene, rubber-modified polystyrene, styrene/acrylonitrile copolymer, styrene/butadiene/acrylonitrile copolymer,
Examples include homopolymers and copolymers of styrene and its derivatives, such as styrene/butadiene/methyl methacrylate copolymer, styrene/α-olefin rubber/acrylonitrile copolymer, and styrene/α-methylstyrene copolymer. It will be done. Especially polystyrene, rubber-modified polystyrene,
Styrene-butadiene-acrylonitrile copolymer is preferred. The constituent components of the adhesive composition of the present invention described above are formulated as follows. That is, (a) an ethylene/vinyl acetate copolymer 60 to 95 containing a modified ethylene/vinyl acetate copolymer having an aromatic vinyl compound unit concentration of 10 to 70% by weight in a proportion of 10 to 100% by weight;
and (c) ethylenically unsaturated carboxylic acid unit concentration relative to 100 parts by weight of a resin consisting of (b) a thermoplastic block elastomer of 5 to 40% by weight consisting of a conjugated diolefin and an aromatic vinyl compound. is 0.01~10% by weight
of modified ethylene/vinyl acetate copolymer from 0.5 to 100
It contains 5 to 50 parts by weight of ethylene/vinyl acetate copolymer in a proportion of 5 to 50 parts by weight. Here, if component (a) exceeds 95% by weight, that is, component (b) is less than 5% by weight, the adhesive strength, especially for polystyrene resins, will not be sufficient; If the amount of component (b) is less than 40% by weight, extrusion moldability may be impaired. Also,
If component (c) is less than 5 parts by weight, the adhesion to metals will be particularly poor, while if it exceeds 50 parts by weight, not only will the effect of modifying the adhesive strength with metals be saturated, but conversely, the adhesive strength with metals will be saturated. This is undesirable because the adhesive strength of the material decreases. As described above, the present invention includes a homogeneous mixture of three components each having different adhesive properties,
This is an adhesive composition that exhibits extremely excellent adhesion to both polystyrene resins and metals, and because of its homogeneity, it can be melt-kneaded and freely formed into films, sheets, granules, and pellets. . As the melt-kneading method, known methods such as an extruder, Banbury, and roll can be used. The adhesive composition homogenized by this type of method can be formed into a film by a known film forming method such as an inflation method or a T-die method, and used as a film adhesive. Alternatively, it can be made into pellets using an extruder or the like and used as a pellet-like adhesive, or it can be pulverized by known methods such as mechanical pulverization or chemical pulverization and used as a powdered adhesive. can be stacked. Alternatively, the adhesive composition of the present invention and the polystyrene resin may be laminated by a known co-extrusion method such as in-die or outside-die lamination, and metal may be laminated by pressure on the surface of the adhesive layer. The heating temperature during lamination is above the melting point of each resin and below the decomposition temperature, that is, 70 to 300°C, preferably 100 to 300°C.
The temperature is 250° C., and the pressure is preferably 1 Kg/cm 2 or more and 150 Kg/cm 2 or less, preferably 10 to 50 Kg/cm 2 . Furthermore, in view of the above performance, it is obvious that the adhesive of the present invention can also be used as an adhesive between polystyrene resins or between metals. Further, the bonding does not necessarily have to be done by solid adhesive (laminated type), and depending on the case, it is also possible to do point bonding at the necessary locations. Examples of the present invention will be described below. Example 1 20 kg of pure water and 600 g of tribasic calcium phosphate and 0.65 g of sodium dodecylbenzenesulfonate as suspending agents were added to an autoclave with a capacity of 50 mm to form an aqueous medium, and ethylene/vinyl acetate copolymer (MI12 °, density 0.948, vinyl acetate content
20% by weight) particles were suspended by stirring. Separately, 8 g of benzoyl peroxide as a polymerization initiator
and 4 g of t-butyl peroxybenzoate were dissolved in 4 kg of styrene (60% by weight based on the ethylene/vinyl acetate copolymer), and this was added to the suspension system, and the temperature inside the autoclave was raised to 45 ° C. The temperature was maintained for 3 hours to impregnate styrene containing a polymerization initiator into the ethylene/vinyl acetate copolymer particles. This aqueous suspension was heated to 80°C and maintained at this temperature for 5 hours and then at 125°C for 5 hours to complete polymerization. It was confirmed that polystyrene was almost quantitatively present at 60% by weight in the obtained modified particles. In addition, 2,5-
Thoroughly mix 0.6% by weight of dimethyl-hexane-2,5-dihydroperoxide and 1.0% by weight of maleic anhydride using a Henschel mixer to form a 40mm
Extrusion temperature 150℃ using φ extruder (L/D=28)
It was made into pellets. After crushing the obtained pellets,
After sufficiently extracting unreacted maleic anhydride with acetone, it was confirmed by infrared absorption spectrum that 0.76% by weight of maleic anhydride had been added. The styrene-modified ethylene-vinyl acetate copolymer and maleic anhydride-modified ethylene-vinyl acetate copolymer obtained as above, the styrene-butadiene block elastomer (Ciel Kagaku Co., Ltd., Califrex TR-1102) and /or blend a predetermined amount of unmodified ethylene/vinyl acetate copolymer,
The mixture was melt-kneaded using a 40 mmφ extruder at a temperature of 160°C to obtain homogeneously mixed pellets. This pellet was formed into a 50μ thick film using a T-die film molding machine, and using this film as an adhesive, a 1mm thick sheet of ABS resin (Mitsubishi Montmont, Toughflex 410) and 50μ thick aluminum foil were bonded together. It was thermocompressed using a heat sealer. Heat sealing conditions were: temperature 160℃, pressure 1.4Kg/cm 2 , time 10
Seconds. The crimped area is 200mm x 15mm. The ABS resin/aluminum foil laminate thus obtained was cut to a width of 20 mm and subjected to a 180°C peel test (peeling speed 500 mm/min). The results are shown in Table-1. Comparative Example 1 Table 1 shows the results of using only ethylene/vinyl acetate copolymer as the adhesive in Example 1. Comparative Example 2 Table 1 shows the results of using only the styrene-modified ethylene/vinyl acetate copolymer as the adhesive in Example 1. Comparative Example 3 In Example 1, 80% by weight of the styrene-modified ethylene/vinyl acetate copolymer and a block elastomer (Ciel Kagaku Co., Ltd., Califrex,
TR-1102) The results using a 20% by weight blend are shown in Table-1. Comparative Example 4 Table 1 shows the results of using the maleic anhydride-modified ethylene/vinyl acetate copolymer as the adhesive in Example 1. Comparative Example 5 In Example 1, a blend of 100 parts by weight of the styrene-modified ethylene/vinyl acetate copolymer and 20 parts by weight of the maleic anhydride-modified ethylene/vinyl acetate copolymer was used as the adhesive. It is shown in Table-1. Example 2 A styrene/acrylonitrile modified ethylene/vinyl acetate copolymer polymerized using 3 kg of styrene and 1 kg of acrylonitrile in Example 1,
Styrene-butadiene block elastic body (Asahi Kasei,
Toughprene) and maleic anhydride-modified ethylene.
An adhesive blended with a predetermined amount of vinyl acetate copolymer was extrusion laminated to a thickness of 30μ onto a 50μ aluminum foil at an extrusion temperature of 210°C using a 50mmφ laminator. Aluminum foil coated with this adhesive and a 0.5 mm thick sheet of ABS resin were thermocompressed using a press molding machine at a temperature of 200°C and a pressure of 10 kg/ cm2 , and a 20 mm wide 180° peel test ( Peeling speed 500
mm/min). The results are shown in Table-2. This product was also subjected to a 90° bending test at a low temperature of 0°C, but no peeling phenomenon was observed at the bent R portion, confirming that it had good adhesive properties even at low temperatures. Comparative Example 6 Table 2 shows the results of using a blend of 100 parts by weight of ethylene/vinyl acetate copolymer and 20 parts by weight of maleic anhydride-modified ethylene/vinyl acetate copolymer as the adhesive in Example 2. . Example 3 Ethylene-vinyl acetate copolymer (MI4, density
0.938, vinyl acetate content 15% by weight) was suspended in toluene, 3 parts of acrylic acid was added to this,
Stir for 30 minutes at room temperature. Thereafter, the temperature was raised to 100° C. while stirring, and 2 parts of 3,5,5-trimethylhexanoyl peroxide was diluted with toluene and added dropwise over 30 minutes. 100℃ for 2 hours and 30 minutes after dropping
The reaction was continued by maintaining the temperature at After the reaction was completed, the polymer was reprecipitated using excess acetone, unreacted monomers were thoroughly removed, and a powdery polymer was obtained by centrifugation. The acrylic acid content of this polymer was determined by infrared absorption spectrum.
0.9% by weight of acrylic acid was added. The thus obtained acrylic acid-modified ethylene/vinyl acetate copolymer, the ethylene-modified ethylene/vinyl acetate copolymer used in Example 1, and the styrene/butadiene block elastomer were blended in predetermined amounts to form a 40 mmφ
The mixture was melt-kneaded at 190°C using an extruder (L/D=28) to obtain homogeneous pellets. This pellet was molded into a film with a thickness of 50μ using a T-die film molding machine, and this film was used as an adhesive to form rubber-modified polystyrene (Mitsubishi Monsanto Co., Ltd.,
A 1 mm thick sheet of Dialex HT190) and metal foil were press-molded under bonding conditions of 140°C and 40°C.
Kg/cm 2 and bonded for 3 minutes, and the 180° peel strength was measured. The results are shown in Table-3. (As foil, steel foil,
(using Al foil)
【表】【table】
【表】【table】
【表】【table】
Claims (1)
ビニル化合物をグラフト反応条件に付して得ら
れる、芳香族ビニル化合物単位濃度が10〜70重
量%の改質エチレン・酢酸ビニル共重合体を10
〜100重量%の割合で含むエチレン・酢酸ビニ
ル共重合体樹脂60〜95重量部、 (b) 共役ジオレフインと芳香族ビニル化合物より
なる熱可塑性ブロツク弾性共重合体樹脂5〜40
重量部、および (c) エチレン・酢酸ビニル共重合体とエチレン性
不飽和カルボン酸をグラフト反応条件に付して
得られる、エチレン性不飽和カルボン酸単位濃
度が0.01〜10重量%の改質エチレン・酢酸ビニ
ル共重合体を0.5〜100重量%の割合で含むエチ
レン・酢酸ビニル共重合体樹脂の(a)+(b)100重
量部に対して5〜50重量部 を配合してなることを特徴とする接着剤組成物。[Claims] 1 (a) Modified ethylene with an aromatic vinyl compound unit concentration of 10 to 70% by weight, obtained by subjecting an ethylene/vinyl acetate copolymer and an aromatic vinyl compound to graft reaction conditions. Vinyl acetate copolymer 10
60 to 95 parts by weight of an ethylene/vinyl acetate copolymer resin containing ~100% by weight; (b) 5 to 40 parts by weight of a thermoplastic block elastic copolymer resin comprising a conjugated diolefin and an aromatic vinyl compound;
parts by weight, and (c) modified ethylene with an ethylenically unsaturated carboxylic acid unit concentration of 0.01 to 10% by weight, obtained by subjecting an ethylene/vinyl acetate copolymer and an ethylenically unsaturated carboxylic acid to graft reaction conditions.・5 to 50 parts by weight of ethylene/vinyl acetate copolymer resin (a) + (b) containing 0.5 to 100% by weight of vinyl acetate copolymer to 100 parts by weight of (a) + (b). Characteristic adhesive composition.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12786279A JPS5653165A (en) | 1979-10-05 | 1979-10-05 | Adhesive composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12786279A JPS5653165A (en) | 1979-10-05 | 1979-10-05 | Adhesive composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5653165A JPS5653165A (en) | 1981-05-12 |
JPH0127116B2 true JPH0127116B2 (en) | 1989-05-26 |
Family
ID=14970490
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12786279A Granted JPS5653165A (en) | 1979-10-05 | 1979-10-05 | Adhesive composition |
Country Status (1)
Country | Link |
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JP (1) | JPS5653165A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5924665A (en) * | 1982-07-31 | 1984-02-08 | 大日本印刷株式会社 | Laminate |
JPS59152852A (en) * | 1983-02-22 | 1984-08-31 | 株式会社クラレ | Laminate and manufacture thereof |
DE3321797A1 (en) * | 1983-06-16 | 1984-12-20 | Röhm GmbH, 6100 Darmstadt | HOT SEALABLE COATINGS |
US4813947A (en) * | 1985-12-30 | 1989-03-21 | Personal Products Company | Closure system for resealably attaching a tape tab to a fabric surface |
-
1979
- 1979-10-05 JP JP12786279A patent/JPS5653165A/en active Granted
Also Published As
Publication number | Publication date |
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JPS5653165A (en) | 1981-05-12 |
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