JPH02245056A - Polyester composition - Google Patents
Polyester compositionInfo
- Publication number
- JPH02245056A JPH02245056A JP6514489A JP6514489A JPH02245056A JP H02245056 A JPH02245056 A JP H02245056A JP 6514489 A JP6514489 A JP 6514489A JP 6514489 A JP6514489 A JP 6514489A JP H02245056 A JPH02245056 A JP H02245056A
- Authority
- JP
- Japan
- Prior art keywords
- particles
- polyester
- film
- crosslinked polymer
- polyester composition
- 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.)
- Granted
Links
- 229920000728 polyester Polymers 0.000 title claims abstract description 44
- 239000000203 mixture Substances 0.000 title claims description 26
- 239000002245 particle Substances 0.000 claims abstract description 70
- 229920006037 cross link polymer Polymers 0.000 claims abstract description 23
- 229920001577 copolymer Polymers 0.000 claims abstract description 15
- -1 polyethylene terephthalate Polymers 0.000 claims abstract description 11
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims abstract description 6
- 229920002554 vinyl polymer Polymers 0.000 claims abstract description 5
- 150000001252 acrylic acid derivatives Chemical group 0.000 claims description 4
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 abstract description 14
- 238000005299 abrasion Methods 0.000 abstract description 14
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 abstract description 11
- 229920000642 polymer Polymers 0.000 abstract description 8
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 abstract description 5
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 abstract description 4
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 abstract description 3
- 229920000139 polyethylene terephthalate Polymers 0.000 abstract description 3
- 239000005020 polyethylene terephthalate Substances 0.000 abstract description 3
- 239000011248 coating agent Substances 0.000 abstract description 2
- 238000000576 coating method Methods 0.000 abstract description 2
- 239000000178 monomer Substances 0.000 abstract description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 abstract 1
- 238000013329 compounding Methods 0.000 abstract 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 abstract 1
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 17
- 150000001875 compounds Chemical class 0.000 description 14
- 238000000034 method Methods 0.000 description 12
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- 238000005809 transesterification reaction Methods 0.000 description 8
- 238000001816 cooling Methods 0.000 description 7
- 239000002002 slurry Substances 0.000 description 6
- 238000004381 surface treatment Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000012756 surface treatment agent Substances 0.000 description 5
- 239000000654 additive Substances 0.000 description 4
- 230000000996 additive effect Effects 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 230000003746 surface roughness Effects 0.000 description 4
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005886 esterification reaction Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 229910052698 phosphorus Inorganic materials 0.000 description 3
- 239000011574 phosphorus Substances 0.000 description 3
- 238000006068 polycondensation reaction Methods 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- 238000011282 treatment Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 2
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- 229910019142 PO4 Inorganic materials 0.000 description 2
- 239000004793 Polystyrene Substances 0.000 description 2
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 2
- 241001422033 Thestylus Species 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 125000001931 aliphatic group Chemical group 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 150000003863 ammonium salts Chemical class 0.000 description 2
- ADCOVFLJGNWWNZ-UHFFFAOYSA-N antimony trioxide Chemical compound O=[Sb]O[Sb]=O ADCOVFLJGNWWNZ-UHFFFAOYSA-N 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 2
- 239000003990 capacitor Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N hexan-1-ol Chemical compound CCCCCCO ZSIAUFGUXNUGDI-UHFFFAOYSA-N 0.000 description 2
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 2
- 150000002681 magnesium compounds Chemical class 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Chemical class 0.000 description 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 2
- 239000012299 nitrogen atmosphere Substances 0.000 description 2
- 239000011146 organic particle Substances 0.000 description 2
- 239000005022 packaging material Substances 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 2
- 239000010452 phosphate Substances 0.000 description 2
- 238000000206 photolithography Methods 0.000 description 2
- 229920006267 polyester film Polymers 0.000 description 2
- 229920002223 polystyrene Polymers 0.000 description 2
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- UQADULIGBPMSNJ-UHFFFAOYSA-N 2-(ethenoxymethyl)oxirane ethenyl acetate Chemical compound C(C)(=O)OC=C.C(C1CO1)OC=C UQADULIGBPMSNJ-UHFFFAOYSA-N 0.000 description 1
- MMINFSMURORWKH-UHFFFAOYSA-N 3,6-dioxabicyclo[6.2.2]dodeca-1(10),8,11-triene-2,7-dione Chemical compound O=C1OCCOC(=O)C2=CC=C1C=C2 MMINFSMURORWKH-UHFFFAOYSA-N 0.000 description 1
- FRIBMENBGGCKPD-UHFFFAOYSA-N 3-(2,3-dimethoxyphenyl)prop-2-enal Chemical compound COC1=CC=CC(C=CC=O)=C1OC FRIBMENBGGCKPD-UHFFFAOYSA-N 0.000 description 1
- DBCAQXHNJOFNGC-UHFFFAOYSA-N 4-bromo-1,1,1-trifluorobutane Chemical compound FC(F)(F)CCCBr DBCAQXHNJOFNGC-UHFFFAOYSA-N 0.000 description 1
- 239000005995 Aluminium silicate Substances 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 239000004342 Benzoyl peroxide Substances 0.000 description 1
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- PJANXHGTPQOBST-VAWYXSNFSA-N Stilbene Natural products C=1C=CC=CC=1/C=C/C1=CC=CC=C1 PJANXHGTPQOBST-VAWYXSNFSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- 125000003236 benzoyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C(*)=O 0.000 description 1
- 235000019400 benzoyl peroxide Nutrition 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- MPMBRWOOISTHJV-UHFFFAOYSA-N but-1-enylbenzene Chemical compound CCC=CC1=CC=CC=C1 MPMBRWOOISTHJV-UHFFFAOYSA-N 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000007809 chemical reaction catalyst Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000006866 deterioration 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
- 238000010586 diagram Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- AFOSIXZFDONLBT-UHFFFAOYSA-N divinyl sulfone Chemical compound C=CS(=O)(=O)C=C AFOSIXZFDONLBT-UHFFFAOYSA-N 0.000 description 1
- 125000004185 ester group Chemical group 0.000 description 1
- STVZJERGLQHEKB-UHFFFAOYSA-N ethylene glycol dimethacrylate Substances CC(=C)C(=O)OCCOC(=O)C(C)=C STVZJERGLQHEKB-UHFFFAOYSA-N 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 125000003055 glycidyl group Chemical group C(C1CO1)* 0.000 description 1
- 125000005843 halogen group Chemical group 0.000 description 1
- 239000012456 homogeneous solution Substances 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 239000010954 inorganic particle Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 229940057995 liquid paraffin Drugs 0.000 description 1
- 150000002642 lithium compounds Chemical class 0.000 description 1
- 229940097364 magnesium acetate tetrahydrate Drugs 0.000 description 1
- XKPKPGCRSHFTKM-UHFFFAOYSA-L magnesium;diacetate;tetrahydrate Chemical compound O.O.O.O.[Mg+2].CC([O-])=O.CC([O-])=O XKPKPGCRSHFTKM-UHFFFAOYSA-L 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
- 150000002736 metal compounds Chemical class 0.000 description 1
- 125000005395 methacrylic acid group Chemical group 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- RXOHFPCZGPKIRD-UHFFFAOYSA-N naphthalene-2,6-dicarboxylic acid Chemical compound C1=C(C(O)=O)C=CC2=CC(C(=O)O)=CC=C21 RXOHFPCZGPKIRD-UHFFFAOYSA-N 0.000 description 1
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 125000004433 nitrogen atom Chemical group N* 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920000233 poly(alkylene oxides) Polymers 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 229920001225 polyester resin Polymers 0.000 description 1
- 239000004645 polyester resin Substances 0.000 description 1
- 239000003505 polymerization initiator Substances 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 230000003381 solubilizing effect Effects 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- PJANXHGTPQOBST-UHFFFAOYSA-N stilbene Chemical compound C=1C=CC=CC=1C=CC1=CC=CC=C1 PJANXHGTPQOBST-UHFFFAOYSA-N 0.000 description 1
- 235000021286 stilbenes Nutrition 0.000 description 1
- 150000003440 styrenes Chemical class 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 238000010333 wet classification Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、ポリエステル組成物に関し、詳しくは、フィ
ルム化した際、耐摩耗性、易滑性、表面性及び透明性に
優れたフィルムを与えるポリエステル組成物に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a polyester composition, and more particularly, to a polyester composition that, when formed into a film, provides a film with excellent abrasion resistance, easy sliding properties, surface properties, and transparency. The present invention relates to polyester compositions.
〔従来の技術及び発明が解決しようとする課題〕二軸延
伸ポリエステルフィルムは、その優れた特性から磁気テ
ープ、コンデンサー、包装材、写真製版などの広い分野
で基材フィルムとして使用されている。[Prior Art and Problems to be Solved by the Invention] Due to its excellent properties, biaxially oriented polyester film is used as a base film in a wide range of fields such as magnetic tapes, capacitors, packaging materials, and photolithography.
かかるポリエステルフィルムの特性として、−船釣に耐
摩耗性が良いこと、易滑性に優れていること、さらに表
面粗大突起が少ないことが要求される。これらの耐摩耗
性および易滑性を良好なものとするため、従来からフィ
ルム表面に微細な凹凸を与えるという手法が使用されて
いる。この微細な凹凸を与える方法として、ポリエステ
ル製造工程や押出工程中でポリエステルに対して不活性
な微粒子(無機系又は有機系粒子)を添加することによ
り、フィルム表面に突起を形成させる方法(以下、「添
加粒子法」と称す。)が良く知られている。Such polyester films are required to have - good abrasion resistance for boat fishing, excellent slipperiness, and a small number of rough protrusions on the surface. In order to improve these abrasion resistance and slipperiness, a method of providing fine irregularities on the film surface has been used. As a method for providing these fine irregularities, a method (hereinafter referred to as (referred to as the "added particle method") is well known.
添加粒子法を採用する場合、重要なことは、粒子の選定
であり、粒子の種類により、フィルムの易滑性、耐摩耗
性、表面粗大突起数、および透明性などが著しく異なっ
てくる。特に、ポリエステルとの親和性が悪い粒子を添
加したポリエステル組成物を二軸延伸してフィルム化す
る場合、延伸応力の作用で、粒子表面付近では粒子表面
とポリエステルの剥離により空間部(以降「内部ボイド
」と称す。)が生じ、わずかの外力により容易に粒子が
脱落してしまう。この現象は、フィルムの耐摩耗性の悪
化に直接結びつくものである。また、内部ボイド部分は
ポリエステル自体と屈折率が大きく異なるため、内部ボ
イドの容積や数が増加すると、フィルム全体の透明性が
著しく減少する。When employing the additive particle method, the important thing is the selection of particles, and the slipperiness, abrasion resistance, number of coarse protrusions on the surface, transparency, etc. of the film vary significantly depending on the type of particles. In particular, when a polyester composition containing particles that have poor affinity with polyester is biaxially stretched to form a film, due to the effect of stretching stress, the particle surface and the polyester peel off near the particle surface, resulting in spaces (hereinafter referred to as "internal"). (referred to as "voids"), and particles easily fall off due to a slight external force. This phenomenon is directly linked to deterioration of the abrasion resistance of the film. Furthermore, since the refractive index of the internal voids is significantly different from that of the polyester itself, as the volume and number of internal voids increases, the transparency of the entire film decreases significantly.
本発明者らの検討では、添加する粒子としては、有機系
粒子の方が無機系粒子と比較して、ポリエステルとの親
和性が優れていることが明らかとなり、有機系粒子につ
いて詳細な検討を行なった結果、フィルム化した際の易
滑性、耐摩耗性および透明性の優れる架橋高分子の粒子
の製造法を確立した。The inventors' study revealed that organic particles have a better affinity with polyester than inorganic particles, and a detailed study on organic particles was conducted. As a result, we established a method for producing crosslinked polymer particles that have excellent slipperiness, abrasion resistance, and transparency when formed into a film.
しかしながら、架橋高分子粒子は、その表面の官能基の
相互作用のため凝集性を示し、特に粒子径が小さい場合
に凝集性が顕著である。凝集した粒子をポリエステル中
に添加すると、フィルム化した際に表面粗大突起の原因
となり、フィルムとしての品質を著しく損なうこととな
り好ましくない。However, crosslinked polymer particles exhibit aggregation properties due to interactions between functional groups on their surfaces, and the aggregation properties are particularly noticeable when the particle size is small. Adding aggregated particles to polyester is not preferable because it causes rough protrusions on the surface when formed into a film, significantly impairing the quality of the film.
また、架橋高分子粒子を含有する組成物は、フィルム化
に際しての生産性、すなわち、製膜速度の増大が従来は
必ずしも十分達成されておらず、より高い生産性が望ま
れていた。Furthermore, compositions containing crosslinked polymer particles have not always been able to sufficiently increase the productivity when forming into a film, that is, the film forming speed, and higher productivity has been desired.
本発明者らは、上記課題に鑑み鋭意検討した結果、ある
特定の表面処理を行なった架橋高分子粒子を含有してな
り、且つ溶融時の比抵抗が、ある特定範囲にあるポリエ
ステル組成物が、フィルム化に際し、粒子のポリエステ
ルに対する親和性に優れ、表面粗大突起も少なく、高生
産性を有することを見出し、本発明を完成するに至った
。As a result of intensive studies in view of the above-mentioned problems, the present inventors have found that a polyester composition containing crosslinked polymer particles subjected to a certain surface treatment and having a specific resistance when melted is within a certain range. They found that the particles have excellent affinity for polyester, have few rough surface protrusions, and have high productivity when formed into a film, and have completed the present invention.
すなわち、本発明の要旨は、側鎖にベンゼン環を有する
ビニル化合物単位およびアクリル酸誘導体単位を含有す
る共重合体で架橋高分子からなる粒子を表面処理して得
られる、平均粒径0.01〜5μmの粒子を0.001
〜10重量%含有し、且つ溶融時の比抵抗値カ月、0X
106〜1.0×109Ω・印であることを特徴とする
ポリエステル組成物に存する。That is, the gist of the present invention is to obtain particles with an average particle size of 0.01 that are obtained by surface treating particles made of a crosslinked polymer with a copolymer containing a vinyl compound unit having a benzene ring in the side chain and an acrylic acid derivative unit. 0.001 ~5μm particles
Contains ~10% by weight, and the specific resistance value when melted is 0X
A polyester composition characterized by having a resistance of 10 6 to 1.0×10 9 Ω·.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
本発明においてポリエステルとは、テレフタル酸、ナフ
タレン−2,6−ジカルボン酸のような芳香族ジカルボ
ン酸又はそのエステルとエチレングリコールとを主たる
出発原料として得られるポリエステルを指すが、これに
他の第三成分を含有していてもよい。第三成分としては
、芳香族ジカルボン酸としてイソフタル酸、一方、グリ
コール成分としてプロピレングリコール、テトラメチレ
ングリコール、ネオペンチルグリコール等から適宜選択
される。In the present invention, polyester refers to a polyester obtained using an aromatic dicarboxylic acid such as terephthalic acid or naphthalene-2,6-dicarboxylic acid or an ester thereof and ethylene glycol as main starting materials; It may contain ingredients. The third component is appropriately selected from isophthalic acid as an aromatic dicarboxylic acid, and propylene glycol, tetramethylene glycol, neopentyl glycol, etc. as a glycol component.
本発明で用いる架橋高分子粒子としては、例えば分子中
に唯一個の脂肪族の不飽和結合を有するモノビニル化合
物(A)と、架橋剤として分子中に2個以上の脂肪族の
不飽和結合を有する化合物(’B)との共重合体を挙げ
ることができる。この場合かかる共重合体はポリエステ
ルと反応し得る基を持っていてもよい。The crosslinked polymer particles used in the present invention include, for example, a monovinyl compound (A) having only one aliphatic unsaturated bond in the molecule, and a monovinyl compound (A) having two or more aliphatic unsaturated bonds in the molecule as a crosslinking agent. Examples include copolymers with compound ('B) having In this case, such copolymers may have groups capable of reacting with the polyester.
共重合体の一成分である化合物(A)としては、アクリ
ル酸、メタクリル酸及びこれらのメチルまたはグリシジ
ルエステル、無水マレイン酸及びそのアルキル誘導体、
ビニルグリシジルエーテル酢酸ビニル、スチレン、アル
キル置換スチレン等を挙げることができる。また、化合
物(B)としては、ジビニルベンゼン、ジビニルスルホ
ン、エチレングリコールジメタクリレート等を挙げるこ
とができる。化合物(A)及び(B)は各一種類以上用
いるが、エチレンや窒素原子を有する化合物を共重合さ
せてもよい。これらの共重合体の典型的な例としては、
メタクリル酸メチルとジビニルベンゼン、アクリル酸メ
チルとジビニルベンゼンの共重合体を挙げることができ
る。As the compound (A) which is one component of the copolymer, acrylic acid, methacrylic acid and their methyl or glycidyl esters, maleic anhydride and its alkyl derivatives,
Examples include vinyl glycidyl ether vinyl acetate, styrene, and alkyl-substituted styrene. Further, examples of the compound (B) include divinylbenzene, divinyl sulfone, ethylene glycol dimethacrylate, and the like. One or more types of each of compounds (A) and (B) are used, but a compound having ethylene or a nitrogen atom may be copolymerized. Typical examples of these copolymers include:
Examples include copolymers of methyl methacrylate and divinylbenzene, and copolymers of methyl acrylate and divinylbenzene.
また、これらアルキルエステル基を有する架橋高分子を
ケン化するか、メタクリル酸エステルの代わりにメタク
リル酸、アクリル酸エステルの代わりにアクリル酸を用
いて共重合を行なえば容易にカルボキシル基を有する架
橋高分子を得ることができる。In addition, if these crosslinked polymers having alkyl ester groups are saponified or copolymerized using methacrylic acid instead of methacrylic esters and acrylic acid instead of acrylic esters, crosslinked polymers having carboxyl groups can be easily obtained. molecules can be obtained.
さらに、スチレンとジビニルベンゼンとの共重合体も好
ましく用いることができる。Furthermore, a copolymer of styrene and divinylbenzene can also be preferably used.
これらの粒子は多孔質であってもよく、そのためには化
合物(A)と化合物(B)とを共重合させるに際し、化
合物(C)の存在下、重合し、次いで化合物(C)を有
機溶媒で除去する方法が一般に採用される。化合物(C
)としては、例えばn−ヘキサン、n−へブタン、シク
ロヘキサンケロシン、トルエン、キシレン等の炭化水素
化合物、n−ブタノール、n〜ヘキサノール プロピル
アルコール等のアルコール化合物、及びポリスチレン、
ポリビニルアルコール、ポリアルキレンオキサイド等を
挙げることができる。These particles may be porous, and for that purpose, when copolymerizing compound (A) and compound (B), the polymerization is carried out in the presence of compound (C), and then compound (C) is dissolved in an organic solvent. Generally, the method of removing Compound (C
), for example, hydrocarbon compounds such as n-hexane, n-hebutane, cyclohexane kerosene, toluene, xylene, alcohol compounds such as n-butanol, n-hexanol propyl alcohol, and polystyrene,
Examples include polyvinyl alcohol and polyalkylene oxide.
なお、化合物(A)と化合物(B)とを共重合させるた
めの重合開始剤としては周知の化学的ラジカル開始剤、
例えばアゾイソブチロニトリル過酸化ベンゾイル、t−
ブチルパーオキサイド。In addition, as a polymerization initiator for copolymerizing compound (A) and compound (B), well-known chemical radical initiators,
For example, azoisobutyronitrile benzoyl peroxide, t-
Butyl peroxide.
クメンハイドロパーオキサイド等を用いるか、紫外線照
射法が簡便であるが、単に加熱によって重合を開始させ
てもよい。Although cumene hydroperoxide or the like or ultraviolet irradiation is convenient, polymerization may also be initiated simply by heating.
いずれにしても、これらの共重合体は架橋構造を有し、
ポリエステルの製造あるいは成型時の高温においても実
質的に不溶、不融で耐熱性を有するものが好ましい。In any case, these copolymers have a crosslinked structure,
It is preferable to use a material that is substantially insoluble, infusible, and heat resistant even at high temperatures during production or molding of polyester.
次に本発明における粒子の表面処理方法について説明す
る。表面処理剤としては、側鎖にベンゼン環を有するビ
ニル化合物単位とアクリル酸誘導体単位とを含有する共
重合体を用いる必要がある。Next, the method for surface treatment of particles in the present invention will be explained. As the surface treatment agent, it is necessary to use a copolymer containing a vinyl compound unit having a benzene ring in the side chain and an acrylic acid derivative unit.
側鎖にベンゼン環を有するビニル化合物としては、スチ
レン、ジビニルベンゼン、スチルベン等が挙げられるが
、これらに限定されるものではない。Examples of the vinyl compound having a benzene ring in a side chain include, but are not limited to, styrene, divinylbenzene, and stilbene.
なお、ベンゼン環は、ハロゲン原子、アルキル基。Note that the benzene ring is a halogen atom or an alkyl group.
水酸基等で置換されていてもよい。本発明において特に
好ましく用いられるものはスチレンである。It may be substituted with a hydroxyl group or the like. Styrene is particularly preferably used in the present invention.
また、アクリル酸誘導体としては、アクリル酸。Also, as an acrylic acid derivative, acrylic acid.
メタクリル酸、これらの酸の金属塩ならびにアンモニウ
ム塩7エステル等が挙げられる。これらの中でも、本発
明において特に好ましく用いられるものは、金属塩、ア
ンモニウム塩である。Examples include methacrylic acid, metal salts of these acids, and ammonium salt 7 esters. Among these, metal salts and ammonium salts are particularly preferably used in the present invention.
これらの単位を含有する共重合体を、水またはエチレン
グリコール等の架橋高分子粒子スラリーに添加し、攪拌
分散袋W(ホモミキサー、ホモジナイザー等)で十分に
分散混合するか、共重合体を添加後、湿式粉砕処理を行
なうことにより、架橋高分子粒子の表面処理を行なうこ
とができる。Add the copolymer containing these units to a slurry of crosslinked polymer particles such as water or ethylene glycol, and thoroughly disperse and mix with a stirring dispersion bag W (homomixer, homogenizer, etc.), or add the copolymer. Thereafter, the crosslinked polymer particles can be surface-treated by performing a wet pulverization treatment.
表面処理剤の添加量としては特に制限はないが、粒子の
総量に対して0,1〜5重量%が好ましい。There is no particular restriction on the amount of the surface treatment agent added, but it is preferably 0.1 to 5% by weight based on the total amount of particles.
0.1重量%未満では、表面処理効果が不十分な場合が
多く、また5重量%を超えると処理剤自体の凝集が生じ
て好ましくない。If it is less than 0.1% by weight, the surface treatment effect is often insufficient, and if it exceeds 5% by weight, the treatment agent itself will aggregate, which is not preferable.
得られる粒子の平均粒径は0.01〜5μmの範囲とな
るよう架橋高分子粒子の調製条件を制御するか、粉砕9
分級5濾過等の処理が行なわれる。The preparation conditions of the crosslinked polymer particles are controlled so that the average particle size of the obtained particles is in the range of 0.01 to 5 μm, or the pulverization
Treatments such as classification 5 filtration are performed.
平均粒径が0.01μm未満では、フィルム化した際の
滑り性、耐摩耗性が不充分であり、5μmを超えるとフ
ィルムの表面粗度が過大となり好ましくない。If the average particle diameter is less than 0.01 μm, the slipperiness and abrasion resistance when formed into a film are insufficient, and if it exceeds 5 μm, the surface roughness of the film becomes excessive, which is not preferable.
以上のようにして得られた表面処理を施された架橋高分
子のポリエステル組成物中の添加量は0゜001〜10
重量%の範囲でなければならない。The amount of the surface-treated crosslinked polymer obtained as described above added in the polyester composition is 0°001 to 10
Must be within the range of % by weight.
添加量が0.001重量%未満では、フィルム化した際
、滑り性や耐摩耗性が不十分である。また、添加量が1
0重量%を超えると、フィルムの表面粗度が過大となり
好ましくない。If the amount added is less than 0.001% by weight, the slipperiness and abrasion resistance will be insufficient when formed into a film. Also, the amount added is 1
If it exceeds 0% by weight, the surface roughness of the film will become excessive, which is not preferable.
本発明のポリエステル組成物の製造にあたって、添加粒
子は、ポリエステルの合成反応中に添加するのが好まし
い。特に、エステル交換反応前またはエステル化反応前
、エステル交換反応中またはエステル化反応中、あるい
はエステル交換反応終了後またはエステル化反応終了後
、重縮合反応開始前までに添加するのが好適である。In producing the polyester composition of the present invention, the additive particles are preferably added during the polyester synthesis reaction. In particular, it is suitable to add it before the transesterification reaction or the esterification reaction, during the transesterification reaction or the esterification reaction, after the completion of the transesterification reaction or after the completion of the esterification reaction, or before the start of the polycondensation reaction.
本発明のポリエステル組成物には、表面処理した架橋高
分子粒子の他、二酸化チタン、シリカ。The polyester composition of the present invention contains titanium dioxide and silica in addition to surface-treated crosslinked polymer particles.
カオリン、炭酸カルシウム等の微粒子を併用してもよい
。Fine particles of kaolin, calcium carbonate, etc. may be used in combination.
また、このような微粒子以外にも、ポリエステルの重縮
合反応系で触媒残渣とリン化合物との反応により析出し
た内部粒子を併用することもできる。In addition to such fine particles, internal particles precipitated by a reaction between a catalyst residue and a phosphorus compound in a polyester polycondensation reaction system can also be used.
本発明のポリエステル組成物は、さらに、溶融時の比抵
抗力月×106〜1×109Ω・ctnであることが必
要であり、特に、3X106〜5×10″Ω・0の範囲
が望ましい。比抵抗力月×106Ω・Cl11未満では
ポリマーの熱安定性が悪化し、フィルム化が困難となる
。The polyester composition of the present invention further needs to have a specific resistance during melting of 1×10 6 to 1×10 9 Ω・ctn, and in particular, a range of 3×10 6 to 5×10″ Ω・0 is desirable. Ratio If the resistance is less than 10 6 Ω·Cl 11 , the thermal stability of the polymer deteriorates, making it difficult to form a film.
一方、比抵抗がlXl0’Ω・印を超えると、静電印加
冷却法(特公昭37−6142号公報等に記載されてい
る未延伸シートの優れた製造方法。)を用いても製膜速
度を上げることが困難となり、フィルムの生産性が極め
て悪化する。この溶融度の比抵抗はポリエステルに金属
化合物を可溶化させることにより調整され、通常はエス
テル交換反応終了後、該エステル交換反応触媒、例えば
マグネシウム化合物、リチウム化合物等に対し、0.3
〜1.0倍当量、好ましくは0゜4〜0.8倍当量のリ
ン化合物を添加することにより実施される。On the other hand, if the specific resistance exceeds lXl0'Ω·, the film forming rate will increase even if the electrostatic cooling method (an excellent manufacturing method for unstretched sheets described in Japanese Patent Publication No. 37-6142, etc.) is used. It becomes difficult to raise the temperature, and the productivity of the film becomes extremely poor. The specific resistance of this melting degree is adjusted by solubilizing a metal compound in polyester, and usually after the completion of the transesterification reaction, the specific resistance of the transesterification reaction catalyst, such as a magnesium compound, a lithium compound, etc., is 0.3%.
This is carried out by adding 1.0 to 1.0 times the equivalent, preferably 0.4 to 0.8 times the equivalent of the phosphorus compound.
本発明のポリエステル組成物を、溶融押出し、回転冷却
ドラム上で未延伸シートとしく好ましくは前述の静電印
加冷却法を併用)、80〜130℃で縦方向に2〜10
倍、80〜140°Cで横方向に2〜10倍で逐時また
は同時に延伸し、必要に応じ再度延伸した後、160〜
240°Cで熱処理することによりフィルム化すること
ができるが、この方法に限定されるものではなく、フィ
ルムの使用される用途に応じ、その製膜条件は適宜、選
択される。The polyester composition of the present invention is melt-extruded, turned into an unstretched sheet on a rotating cooling drum (preferably in combination with the above-mentioned electrostatic application cooling method), and heated for 2 to 10 minutes in the machine direction at 80 to 130°C.
Stretched 2 to 10 times in the transverse direction at 80 to 140°C, one after another or simultaneously, stretched again if necessary, and then stretched to 160 to 140°C.
Although it can be formed into a film by heat treatment at 240°C, the method is not limited to this, and the film forming conditions are appropriately selected depending on the use of the film.
以下、本発明を実施例にてさらに詳細に説明するが、本
発明はこれら実施例によって限定されるものではない。EXAMPLES Hereinafter, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited by these Examples.
本発明における物性及び特性の評価方法を以下に示す。A method for evaluating physical properties and characteristics in the present invention is shown below.
(1)架橋高分子粒子の平均粒子径
粒子径は島原製作所製5A−CP3を用いて遠心沈降法
にて測定した。(1) Average particle size of crosslinked polymer particles The particle size was measured by centrifugal sedimentation using Shimabara Seisakusho 5A-CP3.
(2) フィルムの滑り性
滑り性はASTM D1891−63の方法に従い摩
擦係数を測定することにより評価した。(2) Sliding property of the film Sliding property was evaluated by measuring the coefficient of friction according to the method of ASTM D1891-63.
(3)フィルムの耐摩耗性
耐摩耗性の評価は、第1図に示す走行系でフィルムを1
000m長にわたって走行させ、1で示した6mmφの
ピン(SUS420J2の表面仕上げ0.23 )上に
摩耗により付着した量を目視評価し、下記のランクで表
わした。(3) Abrasion resistance of the film The abrasion resistance was evaluated using the running system shown in Figure 1.
The test piece was run over a length of 1,000 m, and the amount of adhesion due to abrasion on the 6 mmφ pin (SUS420J2 surface finish 0.23) indicated by 1 was visually evaluated and expressed in the following ranking.
なお、フィルムの走行速度は10m/mjnとして、張
力は約500g、ピンとの巻き付は角(θ)は135°
とした。The running speed of the film is 10 m/mjn, the tension is approximately 500 g, and the angle (θ) of the wrapping around the pin is 135°.
And so.
O・・・ 付着が殆どない。O... There is almost no adhesion.
△ ・・・ 若干付着する。△... Slight adhesion.
× ・・・ 付着量が多い。×...The amount of adhesion is large.
(4)粗大突起数
フィルム表面にアルミニウムを蒸着し、三光束干渉顕微
鏡を用いて測定した。測定波長0.54μnでn次の干
渉縞を示す個数を25c+fl当りに換算して示した。(4) Number of coarse protrusions Aluminum was deposited on the film surface and measured using a three-beam interference microscope. The number of n-th order interference fringes at a measurement wavelength of 0.54 μn is shown in terms of number per 25c+fl.
4次以上の突起数をF4.3次以上の突起数をF、とし
て示した。The number of protrusions of 4th or higher order is indicated as F4. The number of protrusions of 3rd or higher order is indicated as F.
(5)表面粗度(Ra)
JIS BO601−1976記載の方法により測定
した。(5) Surface roughness (Ra) Measured by the method described in JIS BO601-1976.
測定には小板研究所製、表面粗さ測定機モデル5E−3
Fを用い、触針径2μ、触針荷重30mg、カットオフ
値0.08mn+とじた。For measurement, a surface roughness measuring machine model 5E-3 manufactured by Koita Research Institute was used.
F was used, the stylus diameter was 2 μ, the stylus load was 30 mg, and the cutoff value was 0.08 mn+.
(6)添加粒子とポリエステルとの親和性添加粒子とポ
リエステルとの親和性の評価として、フィルム内部の粒
子のまわりのボイドの大きさを偏光顕微鏡にて観察し、
下記のランクで表わした。(6) Affinity between additive particles and polyester To evaluate the affinity between additive particles and polyester, the size of voids around the particles inside the film was observed using a polarizing microscope.
The ranking is shown below.
O・・・ 大多数の粒子にボイドがみられない。O... No voids are observed in the majority of particles.
Δ ・・・ ボイドのみられる粒子数がやや多い。Δ...The number of particles with voids is slightly higher.
× ・・・ 大多数の粒子に極めて大きいボイドがみら
れる。×...Extremely large voids are seen in the majority of particles.
(7) フィルム内部ヘーズ
ASTM D1003−61の方法に従い、日本重色
■製濁度計NDH−2Aを用い、フィルム両面に流動パ
ラフィンを塗り測定した。(7) Film internal haze It was measured by coating both sides of the film with liquid paraffin using a turbidimeter NDH-2A manufactured by Nippon Heavy Industries Ltd. according to the method of ASTM D1003-61.
(8)ポリエステルの溶融時の比抵抗
プリティンシュ・ジャーナル・オブ・アプライド・フィ
ジンクス(Brit、 J、 Appl、 Phys)
第17巻、第1149〜1154頁(1966年)に記
載しである方法に従った。但し、この場合ポリマー組成
物の溶融時の温度は290°Cとし、直流3000Vを
印加した直後の値を熔融時の比抵抗とした。(8) Resistivity of polyester when melted Prtinsch Journal of Applied Physics (Brit, J., Appl, Phys.)
17, pp. 1149-1154 (1966). However, in this case, the temperature at the time of melting of the polymer composition was 290°C, and the value immediately after applying a direct current of 3000 V was taken as the specific resistance at the time of melting.
なお、実施例で1部」またはc%」は特記しない限り「
重量部」または「重量%」を意味する。In addition, in the examples, "1 part" or "c%" means "unless otherwise specified".
"parts by weight" or "% by weight".
実施例1
[架橋高分子粒子の合成]
メタクリル酸メチル100部、ジビニルベンゼン25部
、エチルビニルベンゼン22 部、 a酸化ベンゾイル
1部、トルエン100部の均一溶液ヲ水700部に分散
させた。Example 1 [Synthesis of crosslinked polymer particles] A homogeneous solution of 100 parts of methyl methacrylate, 25 parts of divinylbenzene, 22 parts of ethylvinylbenzene, 1 part of benzoyl a oxide, and 100 parts of toluene was dispersed in 700 parts of water.
次に窒素雰囲気下で80°Cで4時間攪拌しながら重合
を行なった。得られたエステル基を有する架橋高分子粒
状体の平均粒径は、約10μmであった。生成ポリマー
を脱塩水で水洗し500部のトルエンで2回抽出し少量
の未反応モノマー線状ポリマーを除去した。Next, polymerization was carried out under a nitrogen atmosphere at 80°C with stirring for 4 hours. The average particle size of the obtained crosslinked polymer particles having ester groups was about 10 μm. The resulting polymer was washed with demineralized water and extracted twice with 500 parts of toluene to remove a small amount of unreacted monomer linear polymer.
[表面処理工程]
上記の架橋高分子のエチレングリコールスラリー中に、
表面処理剤として、ポリスチレンとポリアクリル酸アン
モニウムの共重合体を粒子に対して1.0%となるよう
に添加した後、サンドグラインダーを用いて粉砕処理し
、平均粒径1.2μmの粒子スラリーを得た。このスラ
リーを湿式分級および濾過をして平均粒径1.0μmの
20部濃度のスラリーを得た。[Surface treatment step] In the ethylene glycol slurry of the above crosslinked polymer,
As a surface treatment agent, a copolymer of polystyrene and ammonium polyacrylate was added to the particles at a concentration of 1.0%, and then ground using a sand grinder to form a particle slurry with an average particle size of 1.2 μm. I got it. This slurry was subjected to wet classification and filtration to obtain a slurry having a concentration of 20 parts and an average particle size of 1.0 μm.
[ポリエステル組成物の製造]
ジメチレンテレフタレート100部とエチレングリコー
ル60部及び酢酸マグネシウム・四水塩0.09部を反
応器にとり、加熱昇温するとともに、メタノールを留去
してエステル交換反応を行ない、反応開始から4時間を
要して、230°Cに昇温し、実質的にエステル交換反
応を終了した。次いで、エチルアシッドフォスフェート
0.04部を添加(この際、マグネシウム化合物に対し
0.7倍当量のリン化合物が添加されることになる)し
た後、上記平均粒径1.0μmの粒子エチレングリコー
ルスラリー1.5部を添加しく得られるポリエステル樹
脂に対し粒子が0.3%含有することになる)さらに三
酸化アンチモン0.04部を加えて、4時間重縮合を行
ないポリエチレンテレフタレートのポリマーを得た。得
られたポリマーの溶融時の比抵抗は5X10bΩ・印で
あった。[Manufacture of polyester composition] 100 parts of dimethylene terephthalate, 60 parts of ethylene glycol, and 0.09 parts of magnesium acetate tetrahydrate were placed in a reactor, heated to raise the temperature, and methanol was distilled off to perform a transesterification reaction. It took 4 hours from the start of the reaction to raise the temperature to 230°C, and the transesterification reaction was substantially completed. Next, after adding 0.04 part of ethyl acid phosphate (at this time, 0.7 times equivalent amount of phosphorus compound to the magnesium compound is added), the above particle ethylene glycol having an average particle size of 1.0 μm is added. (If 1.5 parts of slurry is added, the particles will be contained in an amount of 0.3% based on the resulting polyester resin) Furthermore, 0.04 parts of antimony trioxide is added and polycondensation is carried out for 4 hours to obtain a polyethylene terephthalate polymer. Ta. The specific resistance of the resulting polymer when melted was 5×10 bΩ·.
[フィルムの製造]
得られたポリマーを180°Cで窒素雰囲気下6時間加
熱乾燥後、押出機により溶融押出しし、静電印加冷却法
により220μmのシート状物を作成し、次いで縦方向
に85°Cで3.7倍、さらに横方向に90°Cで4倍
に延伸した後、220°Cで5秒間熱処理を行なって厚
さ15μmの二軸延伸ポリエチレンテレフタレートフィ
ルムを得た。[Manufacture of film] The obtained polymer was heated and dried at 180°C for 6 hours in a nitrogen atmosphere, then melt-extruded using an extruder, and a 220 μm sheet was created using an electrostatic cooling method. After stretching 3.7 times at 90°C and 4 times in the transverse direction at 90°C, heat treatment was performed at 220°C for 5 seconds to obtain a biaxially stretched polyethylene terephthalate film with a thickness of 15 μm.
なお、この際静電印加冷却法により束縛気泡が入らずに
製膜できる速度すなわち冷却ドラムの最大回転速度は6
0m/分と高速にすることが可能であり、フィルムの生
産性は良好であった。In addition, at this time, the speed at which a film can be formed without trapped air bubbles using the electrostatic application cooling method, that is, the maximum rotational speed of the cooling drum is 6.
It was possible to achieve a high speed of 0 m/min, and the productivity of the film was good.
実施例2
表面処理剤量を粒子に対して2%用いることおよび添加
する粒子の平均粒径が0.3μmであること以外はすべ
て実施例1と同様に行ないポリエステル組成物を得、実
施例1と同様に製膜し厚さ15μmのフィルムを得た。Example 2 A polyester composition was obtained in the same manner as in Example 1 except that the amount of surface treatment agent was 2% based on the particles and the average particle size of the particles added was 0.3 μm. A film with a thickness of 15 μm was obtained in the same manner as above.
比較例1
添加する架橋高分子粒子の平均粒径が1.0μm、表面
処理剤を添加せず表面処理を行なわない以外はすべて実
施例1と同様に行ないポリエステル組成物を得、実施例
1と同様に製膜し厚さ15μmのフィルムを得た。Comparative Example 1 A polyester composition was obtained in the same manner as in Example 1 except that the average particle size of the crosslinked polymer particles to be added was 1.0 μm, no surface treatment agent was added, and no surface treatment was performed. A film with a thickness of 15 μm was obtained in the same manner.
比較例2
添加する架橋高分子粒径の粒子添加量を0.0005重
景%重量ること以外はすべて実施例1と同様に行ないポ
リエステル組成物を得、実施例1と同様に製膜し、厚さ
15μmのフィルムを得た。Comparative Example 2 A polyester composition was obtained in the same manner as in Example 1, except that the amount of crosslinked polymer particles added was 0.0005% by weight, and a film was formed in the same manner as in Example 1. A film with a thickness of 15 μm was obtained.
比較例3
添加する架橋高分子粒子の粒子添加量を15重量%とす
ること以外はすべて実施例1と同様に行ないポリエステ
ル組成物を得、実施例1と同様に製膜し、厚さ15μm
のフィルムを得た。Comparative Example 3 A polyester composition was obtained in the same manner as in Example 1, except that the amount of crosslinked polymer particles added was 15% by weight, and a film was formed in the same manner as in Example 1 to a thickness of 15 μm.
obtained the film.
比較例4
エステル交換反応終了後に添加するエチルアシッドフォ
スフェート量を0.2部とすること以外はすべて実施例
1と同様に行ないポリエステル組成物を得た。Comparative Example 4 A polyester composition was obtained in the same manner as in Example 1 except that the amount of ethyl acid phosphate added after completion of the transesterification reaction was 0.2 parts.
得られた組成物の溶融時の比抵抗は5X109Ω・印と
高く、次いで実施例1と同様にして二軸延伸フィルムを
製造したが、その際に束縛気泡が入らずに製膜できる速
度すなわち冷却ドラムの最大回転数は20m/分と遅く
、フィルムの生産性は悪かった。The specific resistance of the obtained composition when melted was as high as 5×10 9 Ω·mark. Next, a biaxially stretched film was produced in the same manner as in Example 1, but the speed at which the film could be formed without trapped air bubbles, that is, cooling The maximum rotation speed of the drum was slow at 20 m/min, and the productivity of the film was poor.
以上、得られた結果をまとめて表−1に示す。The results obtained above are summarized in Table 1.
本発明の特殊な表面処理を行なった架橋高分子粒子を含
有するポリエステル組成物は、ポリエステルと粒子の高
い親和性を有し、かつ、粒子の分散性が極めて向上して
いる。かかるポリエステル組成物を用いてなるフィルム
は、粒子の脱落が極めて少なく、優れた耐摩耗性を有し
、内部ボイドも少ないため透明性が高く、表面粗大突起
も極めて少ない。The polyester composition containing the crosslinked polymer particles subjected to the special surface treatment of the present invention has a high affinity between the polyester and the particles, and extremely improved dispersibility of the particles. A film made using such a polyester composition has extremely few particles falling off, excellent abrasion resistance, high transparency due to few internal voids, and extremely few rough protrusions on the surface.
従って本発明のポリエステル組成物は、磁気テープ、コ
ンデンサー、包装材、写真製版等、広い用途のフィルム
に適用でき、その工業的価値は高い。Therefore, the polyester composition of the present invention can be applied to films for a wide range of applications, such as magnetic tapes, capacitors, packaging materials, and photolithography, and has high industrial value.
第1図はフィルムの耐摩耗性を評価する走行系の概略図
であり、図中(1)は6mmφの5US420−J20
,2S表面仕上げの固定ピン、(IT)はテンションビ
・ンクアップである。また、固定ビンのフィルムの巻き
付は角θは135°である。Figure 1 is a schematic diagram of the running system for evaluating the abrasion resistance of the film.
, 2S surface finish fixing pin, (IT) is tension link up. Further, the angle θ of the winding of the film around the fixed bottle is 135°.
Claims (1)
びアクリル酸誘導体単位を含有する共重合体で架橋高分
子からなる粒子を表面処理して得られる、平均粒径0.
01〜5μmの粒子を0.001〜10重量%含有し、
且つ溶融時の比抵抗値が1.0×10^6〜1.0×1
0^9Ω・cmであることを特徴とするポリエステル組
成物。(1) A particle with an average particle size of 0.5 mm obtained by surface treating particles made of a crosslinked polymer with a copolymer containing a vinyl compound unit having a benzene ring in the side chain and an acrylic acid derivative unit.
Contains 0.001 to 10% by weight of particles of 01 to 5 μm,
And the specific resistance value when melted is 1.0 x 10^6 ~ 1.0 x 1
A polyester composition characterized by having a resistance of 0^9Ω·cm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1065144A JPH068384B2 (en) | 1989-03-17 | 1989-03-17 | Polyester composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1065144A JPH068384B2 (en) | 1989-03-17 | 1989-03-17 | Polyester composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02245056A true JPH02245056A (en) | 1990-09-28 |
JPH068384B2 JPH068384B2 (en) | 1994-02-02 |
Family
ID=13278396
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1065144A Expired - Fee Related JPH068384B2 (en) | 1989-03-17 | 1989-03-17 | Polyester composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH068384B2 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04117429A (en) * | 1990-09-06 | 1992-04-17 | Toray Ind Inc | Polyester film |
JPH0532872A (en) * | 1991-07-29 | 1993-02-09 | Toray Ind Inc | Thermoplastic polyester resin composition |
JPH0657107A (en) * | 1991-07-19 | 1994-03-01 | Toray Ind Inc | Thermoplastic polyester composition |
US5376711A (en) * | 1992-03-24 | 1994-12-27 | Diafoil Hoechst Company, Limited | Poly(ethylene 2,6-naphthalate) film |
EP0667360A1 (en) * | 1994-02-15 | 1995-08-16 | Japan Synthetic Rubber Co., Ltd. | Process for producing modified cross-linked polymer particles |
US8993112B2 (en) | 2004-06-15 | 2015-03-31 | Basf Se | Polymeric particles |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55152719A (en) * | 1979-05-18 | 1980-11-28 | Diafoil Co Ltd | Preparation of polyester |
JPS5794038A (en) * | 1980-10-16 | 1982-06-11 | Bayer Ag | Tenacity-improved thermoplastic polyester molding composition |
JPS57190040A (en) * | 1981-05-16 | 1982-11-22 | Diafoil Co Ltd | Polyester composition |
JPS595216A (en) * | 1982-06-30 | 1984-01-12 | Fujitsu Ltd | Optical fiber connector |
JPS61181837A (en) * | 1985-02-06 | 1986-08-14 | Japan Synthetic Rubber Co Ltd | Thermoplastic resin film |
-
1989
- 1989-03-17 JP JP1065144A patent/JPH068384B2/en not_active Expired - Fee Related
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55152719A (en) * | 1979-05-18 | 1980-11-28 | Diafoil Co Ltd | Preparation of polyester |
JPS5794038A (en) * | 1980-10-16 | 1982-06-11 | Bayer Ag | Tenacity-improved thermoplastic polyester molding composition |
JPS57190040A (en) * | 1981-05-16 | 1982-11-22 | Diafoil Co Ltd | Polyester composition |
JPS595216A (en) * | 1982-06-30 | 1984-01-12 | Fujitsu Ltd | Optical fiber connector |
JPS61181837A (en) * | 1985-02-06 | 1986-08-14 | Japan Synthetic Rubber Co Ltd | Thermoplastic resin film |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04117429A (en) * | 1990-09-06 | 1992-04-17 | Toray Ind Inc | Polyester film |
JPH0657107A (en) * | 1991-07-19 | 1994-03-01 | Toray Ind Inc | Thermoplastic polyester composition |
JPH0532872A (en) * | 1991-07-29 | 1993-02-09 | Toray Ind Inc | Thermoplastic polyester resin composition |
US5376711A (en) * | 1992-03-24 | 1994-12-27 | Diafoil Hoechst Company, Limited | Poly(ethylene 2,6-naphthalate) film |
EP0667360A1 (en) * | 1994-02-15 | 1995-08-16 | Japan Synthetic Rubber Co., Ltd. | Process for producing modified cross-linked polymer particles |
US5773519A (en) * | 1994-02-15 | 1998-06-30 | Japan Synthetic Rubber Co., Ltd. | Process for producing modified cross-linked polymer particles |
US8993112B2 (en) | 2004-06-15 | 2015-03-31 | Basf Se | Polymeric particles |
Also Published As
Publication number | Publication date |
---|---|
JPH068384B2 (en) | 1994-02-02 |
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