JPS6311378B2 - - Google Patents
Info
- Publication number
- JPS6311378B2 JPS6311378B2 JP54066683A JP6668379A JPS6311378B2 JP S6311378 B2 JPS6311378 B2 JP S6311378B2 JP 54066683 A JP54066683 A JP 54066683A JP 6668379 A JP6668379 A JP 6668379A JP S6311378 B2 JPS6311378 B2 JP S6311378B2
- Authority
- JP
- Japan
- Prior art keywords
- ethylene copolymer
- bis
- weight
- polycarbonate resin
- copolymer
- 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
- 229920001038 ethylene copolymer Polymers 0.000 claims description 26
- 125000000816 ethylene group Chemical group [H]C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 26
- 229920005668 polycarbonate resin Polymers 0.000 claims description 21
- 239000004431 polycarbonate resin Substances 0.000 claims description 21
- 239000000203 mixture Substances 0.000 claims description 12
- 229920001577 copolymer Polymers 0.000 claims description 7
- 150000008064 anhydrides Chemical class 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 5
- 239000004711 α-olefin Substances 0.000 claims description 5
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 4
- 239000005977 Ethylene Substances 0.000 claims description 4
- 125000004432 carbon atom Chemical group C* 0.000 claims description 4
- 150000007934 α,β-unsaturated carboxylic acids Chemical class 0.000 claims description 3
- 238000006116 polymerization reaction Methods 0.000 claims description 2
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 8
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 8
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 8
- 229920000515 polycarbonate Polymers 0.000 description 7
- 239000004417 polycarbonate Substances 0.000 description 7
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 6
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 6
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 4
- 230000001419 dependent effect Effects 0.000 description 4
- 229920000578 graft copolymer Polymers 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 239000008188 pellet Substances 0.000 description 4
- 229920005989 resin Polymers 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 3
- 125000003118 aryl group Chemical group 0.000 description 3
- 238000005452 bending Methods 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 238000010559 graft polymerization reaction Methods 0.000 description 3
- 238000001746 injection moulding Methods 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- 239000001294 propane Substances 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- AFFLGGQVNFXPEV-UHFFFAOYSA-N 1-decene Chemical compound CCCCCCCCC=C AFFLGGQVNFXPEV-UHFFFAOYSA-N 0.000 description 2
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 2
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 2
- 238000004566 IR spectroscopy Methods 0.000 description 2
- YGYAWVDWMABLBF-UHFFFAOYSA-N Phosgene Chemical compound ClC(Cl)=O YGYAWVDWMABLBF-UHFFFAOYSA-N 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- PXKLMJQFEQBVLD-UHFFFAOYSA-N bisphenol F Chemical compound C1=CC(O)=CC=C1CC1=CC=C(O)C=C1 PXKLMJQFEQBVLD-UHFFFAOYSA-N 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920006351 engineering plastic Polymers 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 125000005843 halogen group Chemical group 0.000 description 2
- 238000004898 kneading Methods 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 230000000379 polymerizing effect Effects 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 2
- HCNHNBLSNVSJTJ-UHFFFAOYSA-N 1,1-Bis(4-hydroxyphenyl)ethane Chemical compound C=1C=C(O)C=CC=1C(C)C1=CC=C(O)C=C1 HCNHNBLSNVSJTJ-UHFFFAOYSA-N 0.000 description 1
- FDLFMPKQBNPIER-UHFFFAOYSA-N 1-methyl-3-(3-methylphenoxy)benzene Chemical compound CC1=CC=CC(OC=2C=C(C)C=CC=2)=C1 FDLFMPKQBNPIER-UHFFFAOYSA-N 0.000 description 1
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- WROUWQQRXUBECT-UHFFFAOYSA-N 2-ethylacrylic acid Chemical compound CCC(=C)C(O)=O WROUWQQRXUBECT-UHFFFAOYSA-N 0.000 description 1
- KTMNDTPAJZKQPF-UHFFFAOYSA-N 2-tert-butyl-4-[1-(3-tert-butyl-4-hydroxyphenyl)propyl]phenol Chemical compound C=1C=C(O)C(C(C)(C)C)=CC=1C(CC)C1=CC=C(O)C(C(C)(C)C)=C1 KTMNDTPAJZKQPF-UHFFFAOYSA-N 0.000 description 1
- CKNCVRMXCLUOJI-UHFFFAOYSA-N 3,3'-dibromobisphenol A Chemical compound C=1C=C(O)C(Br)=CC=1C(C)(C)C1=CC=C(O)C(Br)=C1 CKNCVRMXCLUOJI-UHFFFAOYSA-N 0.000 description 1
- VPWNQTHUCYMVMZ-UHFFFAOYSA-N 4,4'-sulfonyldiphenol Chemical compound C1=CC(O)=CC=C1S(=O)(=O)C1=CC=C(O)C=C1 VPWNQTHUCYMVMZ-UHFFFAOYSA-N 0.000 description 1
- NZGQHKSLKRFZFL-UHFFFAOYSA-N 4-(4-hydroxyphenoxy)phenol Chemical compound C1=CC(O)=CC=C1OC1=CC=C(O)C=C1 NZGQHKSLKRFZFL-UHFFFAOYSA-N 0.000 description 1
- RQCACQIALULDSK-UHFFFAOYSA-N 4-(4-hydroxyphenyl)sulfinylphenol Chemical compound C1=CC(O)=CC=C1S(=O)C1=CC=C(O)C=C1 RQCACQIALULDSK-UHFFFAOYSA-N 0.000 description 1
- RSSGMIIGVQRGDS-UHFFFAOYSA-N 4-[(4-hydroxyphenyl)-phenylmethyl]phenol Chemical compound C1=CC(O)=CC=C1C(C=1C=CC(O)=CC=1)C1=CC=CC=C1 RSSGMIIGVQRGDS-UHFFFAOYSA-N 0.000 description 1
- OVVCSFQRAXVPGT-UHFFFAOYSA-N 4-[1-(4-hydroxyphenyl)cyclopentyl]phenol Chemical compound C1=CC(O)=CC=C1C1(C=2C=CC(O)=CC=2)CCCC1 OVVCSFQRAXVPGT-UHFFFAOYSA-N 0.000 description 1
- QHJPJZROUNGTRJ-UHFFFAOYSA-N 4-[2-(4-hydroxyphenyl)octan-2-yl]phenol Chemical compound C=1C=C(O)C=CC=1C(C)(CCCCCC)C1=CC=C(O)C=C1 QHJPJZROUNGTRJ-UHFFFAOYSA-N 0.000 description 1
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 description 1
- HTVITOHKHWFJKO-UHFFFAOYSA-N Bisphenol B Chemical compound C=1C=C(O)C=CC=1C(C)(CC)C1=CC=C(O)C=C1 HTVITOHKHWFJKO-UHFFFAOYSA-N 0.000 description 1
- SDDLEVPIDBLVHC-UHFFFAOYSA-N Bisphenol Z Chemical compound C1=CC(O)=CC=C1C1(C=2C=CC(O)=CC=2)CCCCC1 SDDLEVPIDBLVHC-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- KYPYTERUKNKOLP-UHFFFAOYSA-N Tetrachlorobisphenol A Chemical compound C=1C(Cl)=C(O)C(Cl)=CC=1C(C)(C)C1=CC(Cl)=C(O)C(Cl)=C1 KYPYTERUKNKOLP-UHFFFAOYSA-N 0.000 description 1
- 229910021552 Vanadium(IV) chloride Inorganic materials 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- -1 carbonate ester Chemical class 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 150000001924 cycloalkanes Chemical class 0.000 description 1
- ROORDVPLFPIABK-UHFFFAOYSA-N diphenyl carbonate Chemical compound C=1C=CC=CC=1OC(=O)OC1=CC=CC=C1 ROORDVPLFPIABK-UHFFFAOYSA-N 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 238000010097 foam moulding Methods 0.000 description 1
- 239000001530 fumaric acid Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 150000002366 halogen compounds Chemical class 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000000314 lubricant Substances 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
- 238000005259 measurement Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000001451 organic peroxides Chemical class 0.000 description 1
- 150000002899 organoaluminium compounds Chemical class 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 150000008301 phosphite esters Chemical class 0.000 description 1
- 150000003014 phosphoric acid esters Chemical class 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000012744 reinforcing agent Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 150000003462 sulfoxides Chemical class 0.000 description 1
- 238000005809 transesterification reaction Methods 0.000 description 1
- 150000003682 vanadium compounds Chemical class 0.000 description 1
- JBIQAPKSNFTACH-UHFFFAOYSA-K vanadium oxytrichloride Chemical compound Cl[V](Cl)(Cl)=O JBIQAPKSNFTACH-UHFFFAOYSA-K 0.000 description 1
- JTJFQBNJBPPZRI-UHFFFAOYSA-J vanadium tetrachloride Chemical compound Cl[V](Cl)(Cl)Cl JTJFQBNJBPPZRI-UHFFFAOYSA-J 0.000 description 1
Description
本発明はポリカーボネート樹脂組成物に関する
ものである。詳しくは、耐衝撃性の厚み依存性が
少ないポリカーボネート樹脂組成物に関するもの
である。
ポリカーボネート樹脂は、そのすぐれた物性に
より、エンジニアリングプラスチツクとして大き
な需要が期待されているが、機械的性質のうちの
耐衝撃性については、厚み依存性が大きく、厚さ
の薄い成形品の断面積当りの衝撃破壊強度は十分
大きいが、厚さが厚い成形品の断面積当りの衝撃
破壊強度は、厚さが薄い成形品のそれに比べて格
段に小さいという欠点があり、この点が改善され
れば、更に広い用途が期待できる。
本発明者らは、耐衝撃性の厚み依存性がないポ
リカーボネート樹脂を得るべく鋭意研究を重ねた
結果、特定の樹脂を特定量溶融混合するときは、
ポリカーボネートが本来有する耐衝撃性を向上さ
せることができると共に、厚み依存性も解消させ
ることができ、しかもポリカーボネートが有する
すぐれた諸性質を損うことがないことを知得して
本発明を完成した。
すなわち、本発明は、耐衝撃性の厚み依存性の
少ないポリカーボネートを提供することを目的と
するものであり、その要旨とするところは、ポリ
カーボネート樹脂100重量部に対し、エチレンと
炭素数3以上のα―オレフインとの共重合体に
α,β―不飽知カルボン酸またはその無水物を上
記共重合体に対し0.05〜1.5重量%グラフト重合
させて得た変性エチレン共重合体0.5〜40重量部
を溶融混合してなるポリカーボネート樹脂組成物
である。
以下本発明を詳細に説明する。
本発明で使用するポリカーボネート樹脂は、一
般式
(式中、Xは
The present invention relates to polycarbonate resin compositions. Specifically, the present invention relates to a polycarbonate resin composition whose impact resistance is less dependent on thickness. Polycarbonate resin is expected to be in great demand as an engineering plastic due to its excellent physical properties, but impact resistance among mechanical properties is highly dependent on thickness, and the The impact fracture strength of is sufficiently high, but the drawback is that the impact fracture strength per cross-sectional area of thick molded products is much smaller than that of thin molded products.If this point could be improved, , it can be expected to have even wider applications. The present inventors have conducted intensive research to obtain a polycarbonate resin whose impact resistance is not dependent on thickness, and have found that when melt-mixing a specific amount of a specific resin,
The present invention was completed based on the knowledge that polycarbonate's inherent impact resistance can be improved, thickness dependence can also be eliminated, and the excellent properties of polycarbonate are not impaired. . That is, the purpose of the present invention is to provide a polycarbonate whose impact resistance is less dependent on thickness, and its gist is to add ethylene and a carbon number of 3 or more to 100 parts by weight of a polycarbonate resin. 0.5 to 40 parts by weight of a modified ethylene copolymer obtained by graft polymerizing 0.05 to 1.5% by weight of α,β-unsaturated carboxylic acid or its anhydride to a copolymer with α-olefin. This is a polycarbonate resin composition obtained by melt-mixing. The present invention will be explained in detail below. The polycarbonate resin used in the present invention has the general formula (In the formula, X is
【式】―O―、―
S―、―SO―または―SO2―で示される2価の
基を示し、芳香核はアルキル基またはハロゲン原
子を有していてもよい。)
で表わされる繰りかえし単位を有する樹脂であ
り、一般式
(式中、Xは上記一般式〔〕におけると同
じ。芳香核はアルキル基またはハロゲン原子を有
していてもよい。)
で表わされるジヒドロキシジアリール化合物の高
分子炭酸エステルである。
上記一般式〔〕で表わされるジヒドロキシジ
アリール化合物の具体例としては、ビス(4―ヒ
ドロキシフエニル)メタン、
1,1―ビス(4―ヒドロキシフエニル)エタ
ン、
2,2―ビス(4―ヒドロキシフエニル)プロパ
ン、
2,2―ビス(4―ヒドロキシフエニル)プタ
ン、
2,2―ビス(4―ヒドロキシフエニル)オクタ
ン、
ビス(4―ヒドロキシフエニル)フエニルメタ
ン、
2,2―ビス(4―ヒドロキシ―3―メチルフエ
ニル)プロパン、
1,1―ビス(4―ヒドロキシ―3―第3ブチル
フエニル)プロパン、
2,2―ビス(4―ヒドロキシ―3―ブロモフエ
ニル)プロパン、
2,2―ビス(4―ヒドロキシ―3,5―ジブロ
モフエニル)プロパン、
2,2―ビス(4―ヒドロキシ―3,5―ジクロ
ロフエニル)プロパンのようなビス(ヒドロキシ
アリール)アルカン類、
1,1―ビス(4―ヒドロキシフエニル)シクロ
ペンタン、
1,1―ビス(4―ヒドロキシフエニル)シクロ
ヘキサンのようなビス(ヒドロキシアリール)シ
クロアルカン類、
4,4′―ジヒドロキシジフエニルエーテル、
4,4′―ジヒドロキシ―3,3′―ジメチルジフエ
ニルエーテルのようなジヒドロキシアリールエー
テル類、
4,4′―ジヒドロキシフエニルスルフイド、
4,4′―ジヒドロキシ―3,3′―ジメチルジフエ
ニルスルフイドのようなジヒドロキシジアリール
スルフイド類、
4,4′―ジヒドロキシジフエニルスルホキシド、
4,4′―ジヒドロキシ―3,3′―ジメチルジフエ
ニルスルホキシドのようなジヒドロキシジアリー
ルスルホキシド類、
4,4′―ジヒドロキシジフエニルスルホン、4,
4′―ジヒドロキシ―3,3′―ジメチルジフエニル
スルホンのようなジヒドロキシジアリールスルホ
ン類、
等があげられる。
これらのポリカーボネート樹脂の中では、2,
2′―ビス(4―ヒドロキシフエニル)プロパン
(いわゆる、ビスフエノールA)から製造された
ポリカーボネート樹脂が好適である。
ポリカーボネート樹脂の製法としては、例え
ば、ビスフエノールAとホスゲンを反応させるホ
スゲン法、あるいはビスフエノールAとジフエニ
ルカーボネートなどの炭酸エステルを反応させる
エステル交換法などをあげることができる。
本発明で上記ポリカーボネートと溶融混合する
変性エチレン共重合体は、エチレンと炭素数3以
上のα―オレフインとの共重合体(以下このもの
を未変性エチレン共重合体という)に、α,β―
不飽和カルボン酸またはその無水物を未変性エチ
レン共重合体に対し0.05〜1.5重量%グラフト重
合させて得たものである。
上記変性エチレン共重合体の原料となる未変性
エチレン共重合体は、例えば、チーグラーナツタ
系触媒なかでもオキシ三塩化バナジウム、四塩化
バナジウムのようなバナジウム化合物と有機アル
ミニウム化合物を用い、エチレン50モル%以上、
好ましくは80〜95モル%と、50モル%以下、好ま
しくは20〜5モル%の炭素数3以上のα―オレフ
インとを共重合したものがあげられる。
炭素数3以上のα―オレフインとしては、プロ
ピレン、ブテン―1、ヘキセン―1、デセン―
1、4―メチルブテン―1、4―メチルペンテン
―1などがあげられるが、プロピレンまたはブテ
ン―1が好ましい。
このような未変性エチレン共重合体として好適
なものとしては、三井石油化学工業(株)よりタフマ
ーの商標で市販されている一連の樹脂、例えばタ
フマーA4085、A4090、A20090、などのタフマー
Aシリーズ(エチレン―ブテン―1共重合体)、
タフマーP0280、P0480、P0680、P0880などのタ
フマーPシリーズ(エチレン―プロピレン共重合
体)などがあげられる。
上記未変性エチレン共重合体にグラフト重合さ
せるα,β―不飽和カルボン酸またはその無水物
(以下単に不飽和カルボン酸という)としては、
アクリル酸、メタクリル酸、エタクリル酸、マレ
イン酸、フマル酸等あるいはこれらの酸の無水物
をあげることができる。
これらの中では無水マレイン酸が特に好まし
い。
未変性エチレン共重合体にグラフト重合させる
不飽和カルボン酸の量は、未変性エチレン共重合
体に対し0.05〜1.5重量%である。この量があま
り少いとポリカーボネートの耐衝撃性を改善する
効果が小さくなり、引張り伸び率の小さい成形品
しか得られず、また、ポリカーボネートとの相溶
性が悪いために成形品の表面剥離が起るので好ま
しくない。逆にあまりに多いとポリカーボネート
に添加した際に着色の原因となるので好ましくな
い。好ましくは0.1〜1重量%の範囲である。
グラフト重合は、常法に従つて未変性エチレン
共重合体に不飽和カルボン酸を加え、通常150〜
300℃で溶融混練して行う。このグラフト重合に
際しては、重合を効率よく生起させるために、
α,α′―ビス―t―ブチルパーオキシ―p―ジイ
ソプロピルベンゼンのような有機過酸化物を、未
変性エチレン共重合体に対し0.001〜0.05重量%
程度用いてもよい。
本発明で用いる変性エチレン共重合体は、結晶
化度(ジヤーナル・オブ・ポリマーサイエンス、
第巻(1955)第17〜26頁の記載に準じX線法
で測定)が75%以下、好ましくは1〜35%である
ことが好ましく、また、メルトインデツクス
(ASTM D1238 57Tに従い190℃で測定)が、
0.01〜50、好ましくは0.1〜20であることが好ま
しい。
このような結晶化度およびメルトインデツクス
の変性エチレン共重合体を調製するには、未変性
エチレン共重合体として上記範囲の結晶化度およ
びメルトインデツクスを有するものを使用すれば
よい。
本発明においては、ポリカーボネート樹脂と上
記変性エチレン共重合体とを溶融混合してポリカ
ーボネート樹脂組成物とする。
溶融混合は常法に従つて実施することができ、
例えば、単軸もしくは多軸のスクリユー式押出機
またはダブルスクリユーミキサーのような装置を
用い、240〜330℃、好ましくは250〜310℃程度の
温度で、0.5〜15分間、好ましくは1〜10分間程
度行うのがよい。
変性エチレン共重合体の使用量は、ポリカーボ
ネート樹脂100重量部に対し0.5〜40重量部、好ま
しくは1〜30重量部である。変性エチレン共重合
体の量があまり少いと本発明の効果が期待できな
くなる。
逆にあまり多いと成形品の表面剥離が起るよう
になり、また、引張り伸び率が著しく低下するよ
うになるので好ましくない。
本発明のポリカーボネート樹脂組成物は、周知
の種々の成形方法、例えば、射出成形、押出成
形、圧縮成形、発泡成形などによつて各種形状の
成形品に成形することができる。
また、本発明のポリカーボネート樹脂組成物に
は、ガラス繊維、炭素繊維、金属繊維のような繊
維状補強剤、シリカ、アルミナ、シリカアルミ
ナ、粘土類、ガラスビーズ、カーボンブラツクの
ような充填剤、芳香族ハロゲン化合物のような難
燃剤、亜リン酸エステル、リン酸エステルのよう
な安定剤、その他滑剤、紫外線吸収剤、着色剤な
ど、周知の添加剤を添加してもよく、これらは常
法に従つて任意の段階で添加することができる。
本発明のポリカーボネート樹脂組成物は、耐衝
撃性の厚み依存性が小さく、ポリカーボネート樹
脂が本来有するすぐれた物性を保持しているの
で、エンジニアリングプラスチツクとしての価値
が大きい。
以下、実施例によつて本発明を具体的に説明す
るが、本発明はその要旨をこえない限り以下の実
施例に限定されるものではない。
なお、実施例中「部」および「%」はそれぞれ
「重量部」および「重量%」を示し、耐衝撃性
(アイゾツト衝撃強度)はASTM D 256、引張
強度および引張伸び率はASTM D 638、曲げ
強度および曲げ弾性率はASTM D 790に従つ
て測定した値である。
変性エチレン共重合体の製造例
結晶化度20%、メルトインデツクス3.6のブテ
ン―1含量14モル%のエチレン―ブテン―1共重
合体100部、少量のアセトンに溶解させたα,
α′―ビス―t―ブチルパーオキシ―p―ジイソプ
ロピルベンゼン0.025部および無水マレイン酸0.5
部を、ヘンシエルミキサー中でブレンドし、この
ブレンド物を内容40mm、L/D=28の押出機を用
いて230℃で溶融混練、押出し、ペレツト化して
変性エチレン共重合体を得た。
このペレツトの一部を粉砕後、未反応無水マレ
イン酸をアセトンで抽出し、プレス成形後赤外線
スペクトルにより無水マレイン酸を定量したとこ
ろ、0.37%の無水マレイン酸がグラフト重合して
いることが判明した。
実施例1〜2および比較例1〜3
平均分子量22000のポリカーボネート樹脂(三
菱化成工業(株)製、ノバレツクス7022A)100部と、
上記製造例によつて製造した変性エチレン共重合
体を下記表1に示す量混合し、内径40mm、L/D
=28の押出機を用いて280℃で溶融混合して押出
し、ペレツト化してポリカーボネート樹脂組成物
ペレツトを製造した。
このペレツトを3オンス射出成形機とASTM
試験片成形用金型を用いて、樹脂温度300℃、金
型温度90℃で射出成形した。得られた試験片の機
械的性質の測定結果は下記表1に示す通りであつ
た。
なお、比較のため、変性エチレン共重合体を使
用しなかつた場合、変性エチレン共重合体を多量
に使用した場合、および上記製造例における原料
である未変性エチレン共重合体を使用した場合の
結果を併記する。[Formula] represents a divalent group represented by -O-, -S-, -SO- or -SO 2 -, and the aromatic nucleus may have an alkyl group or a halogen atom. ) is a resin having a repeating unit represented by the general formula (In the formula, X is the same as in the above general formula []. The aromatic nucleus may have an alkyl group or a halogen atom.) Specific examples of the dihydroxydiaryl compound represented by the above general formula [] include bis(4-hydroxyphenyl)methane, 1,1-bis(4-hydroxyphenyl)ethane, and 2,2-bis(4-hydroxy). phenyl)propane, 2,2-bis(4-hydroxyphenyl)butane, 2,2-bis(4-hydroxyphenyl)octane, bis(4-hydroxyphenyl)phenylmethane, 2,2-bis(4) -Hydroxy-3-methylphenyl)propane, 1,1-bis(4-hydroxy-3-tert-butylphenyl)propane, 2,2-bis(4-hydroxy-3-bromophenyl)propane, 2,2-bis(4) -hydroxy-3,5-dibromophenyl)propane, bis(hydroxyaryl)alkanes such as 2,2-bis(4-hydroxy-3,5-dichlorophenyl)propane, 1,1-bis(4 -hydroxyphenyl)cyclopentane, bis(hydroxyaryl)cycloalkanes such as 1,1-bis(4-hydroxyphenyl)cyclohexane, 4,4'-dihydroxydiphenyl ether, 4,4'-dihydroxy- Dihydroxyaryl ethers such as 3,3'-dimethyldiphenyl ether, 4,4'-dihydroxyphenyl sulfide, dihydroxy such as 4,4'-dihydroxy-3,3'-dimethyldiphenyl sulfide Diaryl sulfides, 4,4'-dihydroxydiphenyl sulfoxide, dihydroxydiaryl sulfoxides such as 4,4'-dihydroxy-3,3'-dimethyldiphenyl sulfoxide, 4,4'-dihydroxydiphenyl sulfone, 4,
Examples include dihydroxydiarylsulfones such as 4'-dihydroxy-3,3'-dimethyldiphenylsulfone. Among these polycarbonate resins, 2,
Polycarbonate resins made from 2'-bis(4-hydroxyphenyl)propane (so-called bisphenol A) are preferred. Examples of methods for producing polycarbonate resins include a phosgene method in which bisphenol A and phosgene are reacted, and a transesterification method in which bisphenol A is reacted with a carbonate ester such as diphenyl carbonate. The modified ethylene copolymer to be melt-mixed with the polycarbonate in the present invention is a copolymer of ethylene and an α-olefin having 3 or more carbon atoms (hereinafter referred to as unmodified ethylene copolymer).
It is obtained by graft polymerizing 0.05 to 1.5% by weight of unsaturated carboxylic acid or its anhydride to unmodified ethylene copolymer. The unmodified ethylene copolymer that is the raw material for the above-mentioned modified ethylene copolymer is prepared by using, for example, a vanadium compound such as vanadium oxytrichloride or vanadium tetrachloride among Ziegler-Natsuta catalysts and an organoaluminium compound, and 50% by mole of ethylene. that's all,
Preferably, 80 to 95 mol% is copolymerized with α-olefin having 3 or more carbon atoms in an amount of 50 mol% or less, preferably 20 to 5 mol%. Examples of α-olefins having 3 or more carbon atoms include propylene, 1-butene, 1-hexene, and 1-decene.
Examples include 1,4-methylbutene-1,4-methylpentene-1, but propylene or butene-1 is preferred. Suitable unmodified ethylene copolymers include a series of resins commercially available under the Tafmer trademark from Mitsui Petrochemical Industries, Ltd., such as Tafmer A series (Tafmer A series such as Tafmer A4085, A4090, A20090, etc.). ethylene-butene-1 copolymer),
Examples include Tafmer P series (ethylene-propylene copolymers) such as Tafmer P0280, P0480, P0680, and P0880. The α,β-unsaturated carboxylic acid or its anhydride (hereinafter simply referred to as unsaturated carboxylic acid) to be graft-polymerized to the unmodified ethylene copolymer is as follows:
Examples include acrylic acid, methacrylic acid, ethacrylic acid, maleic acid, fumaric acid, and anhydrides of these acids. Among these, maleic anhydride is particularly preferred. The amount of unsaturated carboxylic acid graft-polymerized to the unmodified ethylene copolymer is 0.05 to 1.5% by weight based on the unmodified ethylene copolymer. If this amount is too small, the effect of improving the impact resistance of polycarbonate will be small, and only molded products with low tensile elongation will be obtained, and surface peeling of molded products will occur due to poor compatibility with polycarbonate. So I don't like it. On the other hand, if the amount is too large, it may cause coloring when added to polycarbonate, which is not preferable. Preferably it is in the range of 0.1 to 1% by weight. Graft polymerization is carried out by adding an unsaturated carboxylic acid to an unmodified ethylene copolymer according to a conventional method.
This is done by melting and kneading at 300℃. During this graft polymerization, in order to cause the polymerization to occur efficiently,
Organic peroxide such as α,α′-bis-t-butylperoxy-p-diisopropylbenzene is added in an amount of 0.001 to 0.05% by weight based on the unmodified ethylene copolymer.
It may be used to some extent. The modified ethylene copolymer used in the present invention has a crystallinity (Journal of Polymer Science,
(1955), pages 17 to 26) is 75% or less, preferably 1 to 35%, and the melt index (measured at 190°C according to ASTM D1238 57T) is preferably 75% or less, preferably 1 to 35%. measurement) is
It is preferably from 0.01 to 50, preferably from 0.1 to 20. In order to prepare a modified ethylene copolymer having such a crystallinity and melt index, an unmodified ethylene copolymer having a crystallinity and melt index within the above ranges may be used. In the present invention, a polycarbonate resin composition is prepared by melt-mixing a polycarbonate resin and the above-mentioned modified ethylene copolymer. Melt mixing can be carried out according to conventional methods,
For example, using a device such as a single-screw or multi-screw extruder or a double-screw mixer, the temperature is about 240 to 330°C, preferably 250 to 310°C, for 0.5 to 15 minutes, preferably 1 to 10 minutes. It is best to do this for about a minute. The amount of the modified ethylene copolymer used is 0.5 to 40 parts by weight, preferably 1 to 30 parts by weight, per 100 parts by weight of the polycarbonate resin. If the amount of the modified ethylene copolymer is too small, the effects of the present invention cannot be expected. On the other hand, if the amount is too large, surface peeling of the molded product will occur and the tensile elongation rate will drop significantly, which is not preferable. The polycarbonate resin composition of the present invention can be molded into molded articles of various shapes by various well-known molding methods, such as injection molding, extrusion molding, compression molding, and foam molding. The polycarbonate resin composition of the present invention also contains fibrous reinforcing agents such as glass fibers, carbon fibers, and metal fibers, fillers such as silica, alumina, silica alumina, clays, glass beads, and carbon black, and aromatic Well-known additives such as flame retardants such as Group halogen compounds, stabilizers such as phosphite esters and phosphate esters, other lubricants, ultraviolet absorbers, and colorants may be added, and these can be added using conventional methods. Therefore, it can be added at any stage. The polycarbonate resin composition of the present invention has low thickness dependence of impact resistance and maintains the excellent physical properties originally possessed by polycarbonate resins, so it has great value as an engineering plastic. EXAMPLES The present invention will be specifically explained below with reference to examples, but the present invention is not limited to the following examples unless it exceeds the gist thereof. In the examples, "parts" and "%" indicate "parts by weight" and "% by weight," respectively, and impact resistance (Izot impact strength) is in accordance with ASTM D 256, tensile strength and tensile elongation are in accordance with ASTM D 638, Bending strength and bending modulus are values measured according to ASTM D 790. Production example of modified ethylene copolymer 100 parts of ethylene-butene-1 copolymer with a crystallinity of 20% and a melt index of 3.6 and a butene-1 content of 14 mol%, α dissolved in a small amount of acetone,
α′-bis-t-butylperoxy-p-diisopropylbenzene 0.025 part and maleic anhydride 0.5
This blend was melt-kneaded and extruded at 230° C. using an extruder with a content of 40 mm and L/D=28, and then pelletized to obtain a modified ethylene copolymer. After crushing a portion of this pellet, unreacted maleic anhydride was extracted with acetone, and after press molding, maleic anhydride was quantified by infrared spectroscopy, and it was found that 0.37% of maleic anhydride had undergone graft polymerization. . Examples 1 to 2 and Comparative Examples 1 to 3 100 parts of polycarbonate resin with an average molecular weight of 22,000 (manufactured by Mitsubishi Chemical Industries, Ltd., Novarex 7022A),
The modified ethylene copolymer produced according to the above production example was mixed in the amount shown in Table 1 below, and the inner diameter was 40 mm, L/D
The mixture was melt-mixed and extruded at 280° C. using a No. 28 extruder, and then pelletized to produce polycarbonate resin composition pellets. This pellet is molded using a 3 oz injection molding machine and ASTM
Using a test piece mold, injection molding was performed at a resin temperature of 300°C and a mold temperature of 90°C. The results of measuring the mechanical properties of the obtained test piece were as shown in Table 1 below. For comparison, the results are shown when no modified ethylene copolymer is used, when a large amount of modified ethylene copolymer is used, and when unmodified ethylene copolymer, which is the raw material in the above production example, is used. Also listed.
【表】
グラフト共重合体の製造例
結晶化度20%、メルトインデツクス3.6のブテ
ン―1含量14モル%のエチレン―ブテン―1共重
合体100部、少量のアセトンに溶解させたα,
α′―ビス―t―ブチルパーオキシ―p―ジイソプ
ロピルベンゼン0.025部、メチルメタクリレート
0.15部、およびスチレン0.35部をヘンシエルミキ
サー中でブレンドし、該ブレンド物を内径40mm、
L/D=28の押出機を用いて、230℃で溶融混練、
押出し、ペレツト化してグラフト共重合体を得
た。
このペレツトの一部を粉砕後、未反応物をアセ
トン抽出し、プレス成形後、赤外線スペクトルに
よりメチルメタクリレートおよびスチレン成分を
定量したところ、0.12%のメチルメタクリレート
と0.28%のスチレンがグラフト重合していること
が判明した。
比較例 4
実施例1における変性エチレン共重合体の代り
に、上記グラフト共重合体の製造例によつて製造
したグラフト共重合体10部を用い、他は実施例1
におけると同様に成形を行つた。
得られた試験片の機械的性質は、アイゾツド衝
撃強度1/8″60Kg・cm/cm、同1/2″30Kg・cm/cm、
引張強度490Kg/cm2、引張伸び15%、曲げ強度610
Kg/cm2、曲げ弾性率16800Kg/cm2であり、アイゾ
ツド衝撃強度が小さいとともに厚み依存性が大き
く、引張強度および引張伸びも小さかつた。[Table] Production example of graft copolymer 100 parts of ethylene-butene-1 copolymer with a crystallinity of 20% and a melt index of 3.6 and a butene-1 content of 14 mol%, α dissolved in a small amount of acetone,
α′-bis-t-butylperoxy-p-diisopropylbenzene 0.025 parts, methyl methacrylate
0.15 parts of styrene and 0.35 parts of styrene were blended in a Henschel mixer, and the blend was mixed into a
Melt kneading at 230°C using an extruder with L/D = 28,
A graft copolymer was obtained by extrusion and pelletization. After pulverizing a portion of this pellet, unreacted substances were extracted with acetone, and after press molding, the methyl methacrylate and styrene components were quantified by infrared spectroscopy, and it was found that 0.12% methyl methacrylate and 0.28% styrene were graft polymerized. It has been found. Comparative Example 4 In place of the modified ethylene copolymer in Example 1, 10 parts of the graft copolymer produced according to the above graft copolymer production example was used, and the rest was as in Example 1.
Molding was carried out in the same manner as in . The mechanical properties of the obtained test piece were: Izod impact strength 1/8″60Kg・cm/cm, Izod impact strength 1/2″30Kg・cm/cm,
Tensile strength 490Kg/ cm2 , tensile elongation 15%, bending strength 610
Kg/cm 2 and flexural modulus of 16,800 Kg/cm 2 , the Izod impact strength was low, the thickness dependence was large, and the tensile strength and tensile elongation were also small.
Claims (1)
チレンと炭素数3以上のα―オレフインとの共重
合体にα,β―不飽和カルボン酸またはその無水
物を上記共重合体に対し0.05〜1.5重量%グラフ
ト重合させて得た変性エチレン共重合体0.5〜40
重量部を溶融混合してなるポリカーボネート樹脂
組成物。1 Based on 100 parts by weight of polycarbonate resin, 0.05 to 1.5% by weight of α,β-unsaturated carboxylic acid or its anhydride is grafted to the copolymer of ethylene and α-olefin having 3 or more carbon atoms. Modified ethylene copolymer obtained by polymerization 0.5-40
A polycarbonate resin composition obtained by melt-mixing parts by weight.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6668379A JPS55157648A (en) | 1979-05-29 | 1979-05-29 | Polycarbonate resin composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6668379A JPS55157648A (en) | 1979-05-29 | 1979-05-29 | Polycarbonate resin composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS55157648A JPS55157648A (en) | 1980-12-08 |
JPS6311378B2 true JPS6311378B2 (en) | 1988-03-14 |
Family
ID=13322964
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6668379A Granted JPS55157648A (en) | 1979-05-29 | 1979-05-29 | Polycarbonate resin composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS55157648A (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS588759A (en) * | 1981-07-09 | 1983-01-18 | Idemitsu Petrochem Co Ltd | Flame retardant polycarbonate resin composition |
US4472554A (en) * | 1982-07-26 | 1984-09-18 | Mobay Chemical Corporation | Polycarbonate ABS blends of improved impact strength |
JPS5927947A (en) * | 1982-08-07 | 1984-02-14 | Idemitsu Petrochem Co Ltd | Polycarbonate resin composition |
JPS5941617U (en) * | 1982-09-13 | 1984-03-17 | トヨタ自動車株式会社 | Swirl chamber structure of diesel engine |
JPS59223749A (en) * | 1983-06-02 | 1984-12-15 | Ube Ind Ltd | Polycarbonate resin composition |
US4487881A (en) * | 1983-10-03 | 1984-12-11 | Mobay Chemical Corporation | Impact improvement of reinforced polycarbonate/ABS blends |
EP0743343B9 (en) * | 1995-05-17 | 2007-05-23 | Mitsubishi Engineering-Plastics Corporation | Polycarbonate composition for profile extrusion |
JP2000063639A (en) * | 1998-08-13 | 2000-02-29 | Mitsui Chemicals Inc | alpha-OLEFIN/CONJUGATED DIENE COPOLYMER COMPOSITION |
WO2013079631A1 (en) | 2011-11-30 | 2013-06-06 | Bayer Intellectual Property Gmbh | Glass-fiber reinforced, flame-retardant polycarbonate compositions |
TW201840705A (en) * | 2016-12-19 | 2018-11-16 | 德商科思創德意志股份有限公司 | Thermoplastic compositions with good mechanical properties |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS50109247A (en) * | 1974-02-04 | 1975-08-28 | Sumitomo Chemical Co | NETSUKASOSEIJUSHISOSEIBUTSU |
JPS5169558A (en) * | 1974-12-13 | 1976-06-16 | Sumitomo Chemical Co | TAINENSEI JUGOTAISOSEIBUTSU |
-
1979
- 1979-05-29 JP JP6668379A patent/JPS55157648A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS50109247A (en) * | 1974-02-04 | 1975-08-28 | Sumitomo Chemical Co | NETSUKASOSEIJUSHISOSEIBUTSU |
JPS5169558A (en) * | 1974-12-13 | 1976-06-16 | Sumitomo Chemical Co | TAINENSEI JUGOTAISOSEIBUTSU |
Also Published As
Publication number | Publication date |
---|---|
JPS55157648A (en) | 1980-12-08 |
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