JPS6357466B2 - - Google Patents
Info
- Publication number
- JPS6357466B2 JPS6357466B2 JP18028985A JP18028985A JPS6357466B2 JP S6357466 B2 JPS6357466 B2 JP S6357466B2 JP 18028985 A JP18028985 A JP 18028985A JP 18028985 A JP18028985 A JP 18028985A JP S6357466 B2 JPS6357466 B2 JP S6357466B2
- Authority
- JP
- Japan
- Prior art keywords
- polyethylene terephthalate
- glass
- physical properties
- weight
- temperature
- 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
- 239000011521 glass Substances 0.000 claims description 37
- -1 polyethylene terephthalate Polymers 0.000 claims description 30
- 239000011888 foil Substances 0.000 claims description 29
- 229920000139 polyethylene terephthalate Polymers 0.000 claims description 28
- 239000005020 polyethylene terephthalate Substances 0.000 claims description 28
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 claims description 21
- 150000001875 compounds Chemical class 0.000 claims description 19
- 239000004593 Epoxy Substances 0.000 claims description 18
- 239000000203 mixture Substances 0.000 claims description 12
- JYEUMXHLPRZUAT-UHFFFAOYSA-N 1,2,3-triazine Chemical group C1=CN=NN=C1 JYEUMXHLPRZUAT-UHFFFAOYSA-N 0.000 claims description 9
- 239000012763 reinforcing filler Substances 0.000 claims description 7
- 150000008065 acid anhydrides Chemical class 0.000 claims description 6
- 239000007795 chemical reaction product Substances 0.000 claims description 4
- 230000000704 physical effect Effects 0.000 description 22
- 239000000047 product Substances 0.000 description 17
- 239000000376 reactant Substances 0.000 description 17
- 230000000694 effects Effects 0.000 description 12
- 239000002667 nucleating agent Substances 0.000 description 10
- OUPZKGBUJRBPGC-UHFFFAOYSA-N 1,3,5-tris(oxiran-2-ylmethyl)-1,3,5-triazinane-2,4,6-trione Chemical compound O=C1N(CC2OC2)C(=O)N(CC2OC2)C(=O)N1CC1CO1 OUPZKGBUJRBPGC-UHFFFAOYSA-N 0.000 description 7
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 6
- 239000005711 Benzoic acid Substances 0.000 description 6
- 235000010233 benzoic acid Nutrition 0.000 description 6
- 238000002425 crystallisation Methods 0.000 description 6
- 230000008025 crystallization Effects 0.000 description 6
- 238000000465 moulding Methods 0.000 description 6
- 230000007423 decrease Effects 0.000 description 5
- 238000001746 injection moulding Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 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 4
- 239000000945 filler Substances 0.000 description 4
- 239000003365 glass fiber Substances 0.000 description 4
- 238000004898 kneading Methods 0.000 description 4
- HQKMJHAJHXVSDF-UHFFFAOYSA-L magnesium stearate Chemical compound [Mg+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O HQKMJHAJHXVSDF-UHFFFAOYSA-L 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 230000003014 reinforcing effect Effects 0.000 description 4
- 238000004040 coloring Methods 0.000 description 3
- 239000003822 epoxy resin Substances 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 229920000647 polyepoxide Polymers 0.000 description 3
- QPFMBZIOSGYJDE-UHFFFAOYSA-N 1,1,2,2-tetrachloroethane Chemical compound ClC(Cl)C(Cl)Cl QPFMBZIOSGYJDE-UHFFFAOYSA-N 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 2
- 229930185605 Bisphenol Natural products 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- 150000001558 benzoic acid derivatives Chemical class 0.000 description 2
- 235000010237 calcium benzoate Nutrition 0.000 description 2
- 239000004301 calcium benzoate Substances 0.000 description 2
- HZQXCUSDXIKLGS-UHFFFAOYSA-L calcium;dibenzoate;trihydrate Chemical compound O.O.O.[Ca+2].[O-]C(=O)C1=CC=CC=C1.[O-]C(=O)C1=CC=CC=C1 HZQXCUSDXIKLGS-UHFFFAOYSA-L 0.000 description 2
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 2
- ZFSLODLOARCGLH-UHFFFAOYSA-N isocyanuric acid Chemical compound OC1=NC(O)=NC(O)=N1 ZFSLODLOARCGLH-UHFFFAOYSA-N 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 235000019359 magnesium stearate Nutrition 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- RIZUCYSQUWMQLX-UHFFFAOYSA-N 2,3-dimethylbenzoic acid Chemical compound CC1=CC=CC(C(O)=O)=C1C RIZUCYSQUWMQLX-UHFFFAOYSA-N 0.000 description 1
- BLPURQSRCDKZNX-UHFFFAOYSA-N 2,4,6-tris(oxiran-2-ylmethoxy)-1,3,5-triazine Chemical compound C1OC1COC(N=C(OCC1OC1)N=1)=NC=1OCC1CO1 BLPURQSRCDKZNX-UHFFFAOYSA-N 0.000 description 1
- VZSRBBMJRBPUNF-UHFFFAOYSA-N 2-(2,3-dihydro-1H-inden-2-ylamino)-N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]pyrimidine-5-carboxamide Chemical group C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C(=O)NCCC(N1CC2=C(CC1)NN=N2)=O VZSRBBMJRBPUNF-UHFFFAOYSA-N 0.000 description 1
- CGMMPMYKMDITEA-UHFFFAOYSA-N 2-ethylbenzoic acid Chemical compound CCC1=CC=CC=C1C(O)=O CGMMPMYKMDITEA-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 group O=C1OCCOC(=O)C2=CC=C1C=C2 MMINFSMURORWKH-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
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 150000001733 carboxylic acid esters Chemical class 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000003484 crystal nucleating agent Substances 0.000 description 1
- GYZLOYUZLJXAJU-UHFFFAOYSA-N diglycidyl ether Chemical compound C1OC1COCC1CO1 GYZLOYUZLJXAJU-UHFFFAOYSA-N 0.000 description 1
- 125000003700 epoxy group Chemical group 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000012442 inert solvent Substances 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- ZWLPBLYKEWSWPD-UHFFFAOYSA-N o-toluic acid Chemical compound CC1=CC=CC=C1C(O)=O ZWLPBLYKEWSWPD-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 150000003077 polyols Chemical class 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- KKEYFWRCBNTPAC-UHFFFAOYSA-L terephthalate(2-) Chemical compound [O-]C(=O)C1=CC=C(C([O-])=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-L 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Description
本発明は成形性、物性および成形品外観の優れ
た強化ポリエチレンテレフタレート組成物に関す
る。
ポリエチレンテレフタレートは低温での結晶化
速度が遅いため、通常の成形方法による場合到達
結晶化度に限界があり、成形性、物性の劣つたも
のしか得られないという欠点を持つている。これ
に対してガラス繊維などの無機充填剤を添加し剛
性を上げることによつて成形性、物性が改善され
ることは公知であるが、それだけでは充分満足す
べき物性は得られない。特に耐熱性の結晶化度依
存性は大きく、ポリエチレンテレフタレートの無
定形状態の二次転移点約80℃以下の金型で成形し
たものは、熱変形温度が80〜90℃であるのに対し
て、結晶化開始温度約120℃以上の金型で成形し
たものは熱変形温度が200℃近くなりガラス繊維
充填の効果が顕著に発現する。ために強化ポリエ
チレンテレフタレートでは耐熱性が要求される場
合、140〜150℃という高温の金型で成形する必要
があり、このことが成形加工上の大きな欠点とな
つている。この点に関しては結晶核剤の添加が有
効であり、結晶化速度と結晶化度が大きくなつて
低温の金型でもかなり高い熱変形温度を示すもの
が得られるため、種々の核剤効果を有する化合物
が報告されている。たとえば特公昭44―7542号公
報によれば炭素粉、中性粘土類、2価金属の酸化
物あるいは安息香酸塩などが有効とされており、
又特公昭45―9470号公報によればCaCO3、Sb2O3
およびガラス粉末などが挙げられている。これら
を添加したものは確かに耐熱性が向上するものの
金型温度依存性を完全に無くす迄には到らず充分
満足すべきものではない。本発明者らは更に有効
な核剤について鋭意研究した結果、ガラス箔が顕
著な結晶化促進作用を有することを見出したが、
この際トリアジン環を有するエポキシ化合物と芳
香族カルボン酸又はその酸無水物を特定割合で反
応させた反応物を添加することによつて物性が一
段と向上することを見出し本発明を完成した。
即ち本発明は、ポリエチレンテレフタレート及
びトリアジン環を有するエポキシ化合物1モルに
対し芳香族カルボン酸又はその酸無水物0.5〜2
モルを反応させて得た反応物をポリエチレンテレ
フタレートに対し0.05〜5重量%及び全組成物中
10〜50重量%の繊維状補強充填剤と1〜40重量%
のガラス箔からなることを特徴とする強化ポリエ
チレンテレフタレート組成物に関するものであ
る。
強化ポリエチレンテレフタレートにエポキシ樹
脂を添加すると物性や成形性が向上することは公
知であるが、従来使用されているエポキシ樹脂は
必ずしも満足すべき効果を示さず充分なものとは
言えない。
通常用いられるエポキシ樹脂としては、ビスフ
エノールAのジグリシジルエーテルの様なビスフ
エノール型やポリオールエーテル型、多価カルボ
ン酸エステル型のものが挙げられるが、これらを
強化ポリエチレンテレフタレートに添加した場合
一様に物性が向上するものではなく中にはかえつ
て強度低下をきたすものも認められる。ビスフエ
ノール型のエポキシ化合物は比較的物性の向上効
果を示すが、必ずしも高い効果とは言えず全般的
に低水準にとどまつている。それに対してトリア
ジン環を有するエポキシ化合物は極めて顕著な機
械的性質の向上をもたらし特異的に大きな効果を
示す。しかし強化ポリエチレンテレフタレートに
対してトリアジン環を有するエポキシ化合物を単
独で添加すると、流動性が悪くなつて成形性が低
下すると共に成形時に着色がおこり外観が損なわ
れ商品価値が低下する欠点がある。この欠点は、
トリアジン環を有するエポキシ化合物と芳香族カ
ルボン酸又はその酸無水物を特定割合で反応させ
た反応物を用いることによつて解決し、物性水準
が高くしかも流動性の低下や成形品の着色の無い
良好な外観の成形品が得られる。しかるにこの場
合でも、物性の中でもとりわけ耐熱性の金型温度
依存性を改良する迄には到らず、100℃以下の低
温金型で成形する場合には低い熱変形温度のもの
しか得られない。これに対して更にガラス箔を配
合したものは、100℃以下の低温金型で成形して
も200℃以上の高い熱変形温度を示し、高温金型
で成形した場合とほとんど遜色のないものにな
る。また成形品は均質不透明で、特に表面のシル
バーストリークが改良され平滑性、光沢の優れた
ものが得られる。またガラス箔はそれ自身で補強
効果を有するため使用する繊維状補強充填剤の一
部をガラス箔でおきかえても全般的に物性水準は
維持される。これらの点はガラス箔の極めて有利
な点であり、他の核剤では認められない特性であ
る。ガラス箔以外の核剤たとえば2価金属の酸化
物や安息香酸塩では成形品の平滑性、光沢は特に
改良されずそれ自身の補強効果もない。又比較的
成分組成の類似したガラス粉末でも補強効果はガ
ラス箔より低く、特に結晶化促進作用はガラス箔
に比較して著しく劣る。その他CaCO3、Al2O3の
如く通常増量剤として用いられるものを強化ポリ
エチレンテレフタレートに配合すると強度低下が
著しく脆弱になる上、核剤効果もガラス箔に比較
してはるかに小さい。
本発明において用いられるポリエチレンテレフ
タレートとは、エチレンテレフタレート単位を主
構成単位とする線状ポリエステル又は該ポリエス
テルを主成分とする熱可塑性組成物であつて、そ
の縮合度については特に限定されない。
本発明において用いられる繊維状補強充填剤と
しては通常用いられるガラス繊維以外に、炭素繊
維、アスベスト繊維、チタン酸繊維など繊維状無
機物はいずれも適用できる。添加量としては10〜
50重量%の範囲が好適で、10重量%より少ないと
物性が低く、又50重量%を越えると成形時の流動
性が低下するので不適当である。
本発明において用いられるガラス箔とは、32メ
ツシユ以下で厚さ0.5〜10μの鱗片状フレークであ
つて、粒度の細かい方が本発明の効果は顕著にな
るが、粒度がいかに細かくても繊維状のガラスを
粉砕した粉末やミルドフアイバーでは本発明の効
果は得られない。添加量としては1〜40重量%が
好ましく、1重量%より少ないと核剤効果が低く
高い耐熱性が得られず、又40重量%を越えると脆
弱化して物性が低下するので不適当である。
又本発明において用いられるトリアジン環を有
するエポキシ化合物とはエポキシ基を2個以上有
するものであつて、具体的にはトリグリシジルイ
ソシアヌレート(TGIC)、トリグリシジルシア
ヌレート、N―メチル―N′,N″―ジグリシジル
イソシアヌレート(DGIC)などが挙げられる。
反応させる芳香族カルボン酸としては安息香酸、
トルイル酸、ジメチル安息香酸、エチル安息香
酸、フタル酸等およびこれらの酸無水物が挙げら
れるが中でも安息香酸が好ましい。
エポキシ化合物と芳香族カルボン酸の反応条件
としては100〜200℃で5〜30分間溶融撹拌するの
が望ましい。反応温度が100℃より低いと反応が
不均一となる上に長時間の反応を必要とする。又
200℃より高い場合には反応物が着色するので不
適当である。反応物が粘稠で添加混合しにくい時
にはテトラクロルエタン、クロロホルム、アセト
ンなどの適当な不活性溶剤で希釈して添加しても
よい。反応物の添加量はポリエチレンテレフタレ
ートに対して0.05〜5重量%の範囲であり、エポ
キシ化合物と芳香族カルボン酸の仕込みモル比が
0.5〜2で反応させたものであることが重要であ
る。反応物の添加量が0.05重量%未満では物性向
上の効果が低く、又5重量%を越えると機械的強
度は向上せずかえつて流動性の低下をきたすので
不適当である。又エポキシ化合物に対して芳香族
カルボン酸のモル比が0.5未満の反応物では流動
性の低下と成形品の着色がおこり、2を越えると
物性特に機械的強度の向上効果が低下するので好
ましくない。
また、一般にトリアジン環を有するエポキシ化
合物や芳香族カルボン酸は粉末状であるが、これ
らを反応させることによつて粘着性を持つた液状
となるので、これを繊維状充填剤及びガラス箔と
共にポリエチレンテレフタレートに添加して混合
すると、充填剤が反応物を介してポリエチレンテ
レフタレートに粘着し、混合分散性があがると共
に混合および混練作業時に充填剤の飛散が無く有
利である。またエポキシ化合物と芳香族カルボン
酸を反応物として添加した系は繊維状補強充填剤
およびガラス箔の分散性が良好で、物性も高くな
り外観も良好で、平滑性、光沢が良くなる。
本発明の強化ポリエチレンテレフタレート組成
物を構成するポリエチレンテレフタレート、エポ
キシ化合物と芳香族カルボン酸又はその酸無水物
との反応物、繊維状補強充填剤及びガラス箔の混
合方法は一括溶融混練又は、ポリエチレンテレフ
タレートと上記反応物の混合物を予め溶融混練し
て得られる変性ポリエチレンテレフタレートに更
に繊維状補強充填剤とガラス箔を添加して混練す
る方法のいずれでも良いが、後者の方が物性の高
いものが得られる。
本発明を実施するに際して用いる溶融混練装置
としては通常用いられるものはいずれも使用でき
るが、工程簡便性の点から特に押出機が好まし
い。押出条件としては265〜300℃で平均滞在時間
2〜10分間が適当である。
以下実施例により本発明の更に詳細な説明を行
なう。
実施例 1
4ツ口のセパラプルフラスコ中にTGIC50部と
安息香酸20部を仕込み、窒素雰囲気下に120℃で
30分間溶融撹拌して反応を行ない粘稠な液状物を
得た。この反応物14部をアセトン30部で希釈しポ
リエチレンテレフタレート(〔η〕=0.72)2000部
に添加し、タンブラーで混合した後80℃の蒸気乾
燥機中で1時間乾燥してアセトンを除去した。得
られたポリエチレンテレフタレートのチツプは表
面に反応物が均一にコーテイングされ多少粘着性
であつた。これに712部の3mmガラスチヨツプド
ストランドと145部のガラス箔(200メツシユ以
下、厚さ3μ)を加え、タンブラーで混合したと
ころガラス繊維とガラス箔がチツプに均一に粘着
し飛散の少ない混合物が得られた。これをL/D
=25の30mmφ押出機により280℃で押出してペレ
ツトを得た。5オンスの36mmφスクリユーインラ
イン型射出成形機によりシリンダー温度280℃、
金型温度80℃で射出成形して3.2mm厚1号ダンベ
ル、3.2mm厚熱変形試片および6.4mm厚熱変形試片
をつくり物性を評価した。引張強度は1号ダンベ
ルからASTM D638により、又熱変形温度
(HDT)は6.4mm厚熱変形試片からASTM D790
により測定した。
また、比較として各種エポキシ化合物を上記反
応物の代わりにタンブラーで混合したものも同様
に成形評価した。
結果を表―1に示すが、エポキシ化合物の中で
はTGICやDGICの様にトリアジン環を有するエ
ポキシ化合物が顕著に高い引張強度を示してい
る。しかしシヨートシヨツトのゲージ圧が高くて
成形性が劣り成形品が着色するという欠点があ
る。
これに対し、本発明の反応物を用いた組成物で
は強度物性が高い上にシヨートシヨツトのゲージ
圧も低く成形性が良好で着色のない外観の優れた
成形品となる。なおHDTは金型温度が80℃であ
るにもかかわらずエポキシ化合物の種類によらず
ガラス箔を添加する事によつて、一様に200℃以
上の高い値を示している。
The present invention relates to a reinforced polyethylene terephthalate composition with excellent moldability, physical properties, and appearance of molded products. Since polyethylene terephthalate has a slow crystallization rate at low temperatures, there is a limit to the degree of crystallinity that can be achieved using conventional molding methods, and it has the disadvantage that only products with poor moldability and physical properties can be obtained. On the other hand, it is known that moldability and physical properties can be improved by adding an inorganic filler such as glass fiber to increase rigidity, but this alone does not provide sufficiently satisfactory physical properties. In particular, the dependence of heat resistance on the degree of crystallinity is large, and the heat distortion temperature of polyethylene terephthalate molded in a mold with a secondary transition point of about 80°C or lower in the amorphous state is 80 to 90°C. When molded in a mold with a crystallization initiation temperature of about 120°C or higher, the heat distortion temperature approaches 200°C, and the effect of glass fiber filling becomes noticeable. Therefore, if heat resistance is required for reinforced polyethylene terephthalate, it is necessary to mold it in a mold at a high temperature of 140 to 150°C, which is a major drawback in molding processing. In this regard, the addition of a crystal nucleating agent is effective, as it increases the crystallization rate and degree of crystallization, resulting in a mold that exhibits a fairly high heat distortion temperature even at low temperatures, and has various nucleating effects. compounds have been reported. For example, according to Japanese Patent Publication No. 44-7542, carbon powder, neutral clays, divalent metal oxides, or benzoates are effective.
According to Special Publication No. 45-9470, CaCO 3 , Sb 2 O 3
and glass powder. Although it is true that the heat resistance is improved by adding these, it does not completely eliminate mold temperature dependence and is not fully satisfactory. As a result of intensive research into more effective nucleating agents, the present inventors discovered that glass foil has a remarkable effect of promoting crystallization.
At this time, it was discovered that the physical properties could be further improved by adding a reactant in which an epoxy compound having a triazine ring and an aromatic carboxylic acid or its acid anhydride were reacted in a specific ratio, and the present invention was completed. That is, in the present invention, 0.5 to 2 of the aromatic carboxylic acid or its acid anhydride is added to 1 mole of the epoxy compound having polyethylene terephthalate and a triazine ring.
0.05 to 5% by weight of the reactant obtained by reacting the mole with respect to polyethylene terephthalate and in the total composition.
10-50% by weight fibrous reinforcing filler and 1-40% by weight
The present invention relates to a reinforced polyethylene terephthalate composition characterized by comprising a glass foil. Although it is known that adding an epoxy resin to reinforced polyethylene terephthalate improves its physical properties and moldability, the epoxy resins that have been used so far do not necessarily show satisfactory effects and cannot be said to be sufficient. Commonly used epoxy resins include bisphenol type such as diglycidyl ether of bisphenol A, polyol ether type, and polyhydric carboxylic acid ester type, but when these are added to reinforced polyethylene terephthalate, uniform In some cases, the physical properties do not improve, and some actually cause a decrease in strength. Although bisphenol type epoxy compounds show a comparative effect of improving physical properties, the effects are not necessarily high and remain at a low level overall. On the other hand, epoxy compounds having a triazine ring bring about extremely significant improvement in mechanical properties and exhibit a particularly large effect. However, when an epoxy compound having a triazine ring is added alone to reinforced polyethylene terephthalate, there are disadvantages in that the fluidity becomes poor and moldability decreases, and coloration occurs during molding, impairing the appearance and lowering the commercial value. This drawback is
This problem can be solved by using a reactant made by reacting an epoxy compound with a triazine ring with an aromatic carboxylic acid or its acid anhydride in a specific ratio, which has high physical properties and does not cause a decrease in fluidity or coloring of molded products. A molded product with a good appearance can be obtained. However, even in this case, it has not been possible to improve the mold temperature dependence of heat resistance, among other physical properties, and only a low heat distortion temperature can be obtained when molding with a low temperature mold of 100°C or less. . On the other hand, products containing glass foil exhibit a high heat distortion temperature of over 200°C even when molded in a low-temperature mold of 100°C or less, and are almost comparable to those molded in a high-temperature mold. Become. In addition, the molded product is homogeneous and opaque, and in particular, silver streaks on the surface are improved, and the product has excellent smoothness and gloss. Furthermore, since glass foil itself has a reinforcing effect, the physical properties are generally maintained even if a portion of the fibrous reinforcing filler used is replaced with glass foil. These points are extremely advantageous points of glass foil, and are characteristics not found in other nucleating agents. Nucleating agents other than glass foil, such as divalent metal oxides and benzoates, do not particularly improve the smoothness and gloss of the molded product and do not have any reinforcing effect on their own. Further, even glass powder having a relatively similar composition has a lower reinforcing effect than glass foil, and in particular, its crystallization promoting effect is significantly inferior to that of glass foil. If other fillers such as CaCO 3 and Al 2 O 3 that are commonly used as fillers are added to reinforced polyethylene terephthalate, the strength will be significantly lowered and the nucleating agent effect will be much smaller than that of glass foil. The polyethylene terephthalate used in the present invention is a linear polyester having ethylene terephthalate units as a main constituent unit or a thermoplastic composition having the polyester as a main component, and the degree of condensation thereof is not particularly limited. As the fibrous reinforcing filler used in the present invention, in addition to commonly used glass fibers, any fibrous inorganic material such as carbon fiber, asbestos fiber, titanate fiber, etc. can be used. The amount added is 10~
A range of 50% by weight is preferable; if it is less than 10% by weight, the physical properties will be poor, and if it exceeds 50% by weight, the fluidity during molding will be reduced, which is unsuitable. The glass foil used in the present invention is a scale-like flake with a thickness of 0.5 to 10 μm and 32 meshes or less. The effects of the present invention cannot be obtained with powder or milled fiber obtained by pulverizing glass. The amount added is preferably 1 to 40% by weight; if it is less than 1% by weight, the nucleating agent effect is low and high heat resistance cannot be obtained, and if it exceeds 40% by weight, it becomes brittle and the physical properties deteriorate, so it is inappropriate. . Further, the epoxy compound having a triazine ring used in the present invention has two or more epoxy groups, and specifically includes triglycidyl isocyanurate (TGIC), triglycidyl cyanurate, N-methyl-N', Examples include N″-diglycidyl isocyanurate (DGIC).
The aromatic carboxylic acids to be reacted include benzoic acid,
Examples include toluic acid, dimethylbenzoic acid, ethylbenzoic acid, phthalic acid, and acid anhydrides thereof, and among these, benzoic acid is preferred. The reaction conditions for the epoxy compound and aromatic carboxylic acid are preferably melting and stirring at 100 to 200°C for 5 to 30 minutes. When the reaction temperature is lower than 100°C, the reaction becomes non-uniform and requires a long reaction time. or
If the temperature is higher than 200°C, the reaction product will be colored, which is inappropriate. When the reactant is viscous and difficult to add and mix, it may be diluted with an appropriate inert solvent such as tetrachloroethane, chloroform, acetone, etc. before addition. The amount of the reactant added is in the range of 0.05 to 5% by weight based on polyethylene terephthalate, and the molar ratio of the epoxy compound and aromatic carboxylic acid is
It is important that the reaction is carried out at a concentration of 0.5 to 2. If the amount of the reactant added is less than 0.05% by weight, the effect of improving the physical properties will be low, and if it exceeds 5% by weight, the mechanical strength will not be improved and fluidity will deteriorate, which is unsuitable. In addition, if the molar ratio of the aromatic carboxylic acid to the epoxy compound is less than 0.5, fluidity will decrease and the molded product will be colored, while if it exceeds 2, the effect of improving physical properties, especially mechanical strength, will decrease, which is undesirable. . Epoxy compounds and aromatic carboxylic acids that have a triazine ring are generally in powder form, but by reacting them, they become a sticky liquid. When added to terephthalate and mixed, the filler adheres to polyethylene terephthalate via the reactant, improving mixing and dispersibility, and advantageously, there is no scattering of the filler during mixing and kneading operations. In addition, a system in which an epoxy compound and an aromatic carboxylic acid are added as reactants has good dispersibility of the fibrous reinforcing filler and glass foil, has high physical properties, and has a good appearance, smoothness, and gloss. The method for mixing the polyethylene terephthalate, the reaction product of an epoxy compound and an aromatic carboxylic acid or its acid anhydride, the fibrous reinforcing filler, and the glass foil constituting the reinforced polyethylene terephthalate composition of the present invention is by batch melt-kneading or polyethylene terephthalate. Either method may be used, in which a fibrous reinforcing filler and glass foil are further added to the modified polyethylene terephthalate obtained by melt-kneading a mixture of the above-mentioned reactants, but the latter method yields a product with higher physical properties. It will be done. Although any commonly used melt-kneading apparatus can be used in carrying out the present invention, an extruder is particularly preferred from the viewpoint of process simplicity. Appropriate extrusion conditions are 265-300°C and an average residence time of 2-10 minutes. The present invention will be explained in more detail with reference to Examples below. Example 1 50 parts of TGIC and 20 parts of benzoic acid were placed in a 4-necked separate flask and heated at 120°C under a nitrogen atmosphere.
The reaction was carried out by melting and stirring for 30 minutes to obtain a viscous liquid. 14 parts of this reaction product was diluted with 30 parts of acetone, added to 2000 parts of polyethylene terephthalate ([η]=0.72), mixed in a tumbler, and then dried for 1 hour in a steam dryer at 80°C to remove acetone. The resulting polyethylene terephthalate chips had a uniform coating of the reactant on the surface and were somewhat sticky. To this, 712 parts of 3mm glass chopped strands and 145 parts of glass foil (200 mesh or less, thickness 3μ) were added and mixed in a tumbler. The glass fibers and glass foil adhered uniformly to the chips, resulting in less scattering. A mixture was obtained. This is L/D
Pellets were obtained by extrusion at 280° C. using a 30 mmφ extruder of 25 mm. The cylinder temperature is 280℃ using a 5oz 36mmφ screw in-line injection molding machine.
A 3.2 mm thick No. 1 dumbbell, a 3.2 mm thick thermally deformed specimen, and a 6.4 mm thick thermally deformed specimen were made by injection molding at a mold temperature of 80°C, and their physical properties were evaluated. Tensile strength is determined by ASTM D638 from a No. 1 dumbbell, and heat distortion temperature (HDT) is determined by ASTM D790 from a 6.4 mm thick heat deformed specimen.
It was measured by For comparison, various epoxy compounds were mixed in a tumbler instead of the above reactants, and the molding was evaluated in the same manner. The results are shown in Table 1. Among epoxy compounds, epoxy compounds with triazine rings, such as TGIC and DGIC, exhibit significantly high tensile strength. However, the disadvantage is that the gauge pressure of the shot is high, resulting in poor moldability and coloring of the molded product. On the other hand, compositions using the reactants of the present invention have high physical strength, low shot shot gauge pressure, good moldability, and produce molded products with excellent appearance and no coloration. Furthermore, despite the mold temperature being 80°C, HDT uniformly shows a high value of 200°C or more by adding glass foil, regardless of the type of epoxy compound.
【表】【table】
【表】
実施例 2
実施例1で用いたのと同じポリエチレンテレフ
タレート70部にTGICと安息香酸の反応物(モル
比1)を0.7部加え、更に3mmのガラスチヨツプ
ドストランドと表−2に示した各種の核剤を添加
混合し、L/D=25の30mmφノンベント押出機に
より280℃で押出しペレツトを得た。これを5オ
ンス、36mmφのスクリユーインライン射出成形機
で、シリンダー温度280℃で金型温度をかえて成
形し、実施例1に準じて物性を評価した。結果を
表−2に示す。
80℃の低温金型で成形した場合、ガラス箔以外
の核剤では安息香酸カルシウムとステアリン酸マ
グネシウムが200℃以上の熱変形温度を示すが、
他は85〜107℃と低く核剤未添加の87℃と比較し
て小さな効果しか示さない。又安息香酸カルシウ
ムとステアリン酸マグネシウムの場合でもガラス
箔に比較して金型温度依存性は大きく、80℃金型
と150℃金型で15〜20℃近い熱変形温度の差が認
められるのに対し、ガラス箔では0〜10℃と小さ
い。
CaCO3、Al2O3、ガラス粉末などは、低温金型
での熱変形温度が低く引張強度が低下しており、
有効な核剤とは言えない。なおガラス箔以外の核
剤では、全般的に成形品の光沢が劣り、金型を高
温にするとかなり改良はされるもののガラス箔を
添加した程の効果は無い。
ガラス箔の中では粒度の小さいもの程、引張強
度、熱変形温度共に向上するが、一様に高い水準
の値を示している。又チヨツプドストランドの一
部をガラス箔でおきかえても、物性にはほとんど
有意差が認められず、ガラス箔自身が補強効果を
持つていることがわかる。但し、ガラス箔が1重
量%より少なくなると熱変形温度が大巾に低下す
るので不適当である。なおポリエチレンテレフタ
レート70部とガラスチヨツプドストランド30部だ
けから得られる成形品は、引張強度が1620Kg/
cm2、熱変形温度が87℃と低い値しか示さない。[Table] Example 2 0.7 parts of a reactant of TGIC and benzoic acid (molar ratio 1) was added to 70 parts of the same polyethylene terephthalate used in Example 1, and a glass chopped strand of 3 mm was added. The various nucleating agents shown above were added and mixed, and pellets were extruded at 280°C using a 30 mmφ non-vent extruder with L/D=25. This was molded using a 5 ounce, 36 mmφ screw in-line injection molding machine with a cylinder temperature of 280°C and varying mold temperatures, and the physical properties were evaluated according to Example 1. The results are shown in Table-2. When molded in a low-temperature mold at 80°C, calcium benzoate and magnesium stearate exhibit heat distortion temperatures of 200°C or higher when using nucleating agents other than glass foil.
Others are as low as 85-107°C, showing only a small effect compared to 87°C with no nucleating agent added. Also, in the case of calcium benzoate and magnesium stearate, the dependence on mold temperature is greater than that of glass foil, and a difference in heat distortion temperature of nearly 15 to 20 degrees Celsius is observed between an 80 degrees Celsius mold and a 150 degrees Celsius mold. On the other hand, glass foil has a low temperature of 0 to 10°C. CaCO 3 , Al 2 O 3 , glass powder, etc. have low thermal deformation temperatures in low-temperature molds and have reduced tensile strength.
It cannot be said to be an effective nucleating agent. Note that with nucleating agents other than glass foil, the gloss of the molded product is generally inferior, and although it is considerably improved by raising the temperature of the mold, it is not as effective as adding glass foil. Among glass foils, the smaller the particle size, the better both the tensile strength and heat distortion temperature, but the values are uniformly high. Furthermore, even when a portion of the chopped strands was replaced with glass foil, almost no significant difference was observed in the physical properties, indicating that the glass foil itself has a reinforcing effect. However, if the amount of glass foil is less than 1% by weight, the heat deformation temperature will drop significantly, which is unsuitable. The molded product obtained from only 70 parts of polyethylene terephthalate and 30 parts of glass chopped strand has a tensile strength of 1620 kg/
cm 2 and heat distortion temperature of 87°C.
【表】
注)光沢は肉眼による判定:◎特に良好 ○良好 △
やや悪い ×不良
実施例 3
反応物の種類及び量比を変える以外は、実施例
1と同様に反応物を作り、ポリエチレンテレフタ
レートにコーテイングし、実施例1で用いたガラ
スチヨツプドストランド及びガラス箔を実施例1
と同量加えて押出し、射出成形を行ない成形品の
物性を調べた結果を表―3に示す。
TGICと安息香酸のモル比は0.5〜2の範囲が適
当であり、また反応物の添加量も0.05〜5重量%
が良く、これらの範囲からはずれると外観、流動
性、強度などが劣るので好ましくない。
(N―メチル―N′,N″―ジグリシジルイソシ
アヌレート)
成形品の着色
◎ 全くなし ○ わずかにある
△ かなりある × 著しくある[Table] Note) Gloss is judged by the naked eye: ◎ Particularly good ○ Good △
Somewhat poor × Bad Example 3 The reactants were prepared in the same manner as in Example 1 except for changing the type and quantitative ratio of the reactants, and the glass chopped strands and glass used in Example 1 were coated on polyethylene terephthalate. Foil Example 1
Table 3 shows the results of extrusion and injection molding by adding the same amount of the same amount as the above and examining the physical properties of the molded product. The appropriate molar ratio of TGIC and benzoic acid is in the range of 0.5 to 2, and the amount of reactants added is 0.05 to 5% by weight.
If it deviates from these ranges, the appearance, fluidity, strength, etc. will deteriorate, which is not preferable. (N-Methyl-N′,N″-diglycidyl isocyanurate) Coloring of molded products ◎ Not at all ○ Slightly △ Quite × Significantly
【表】
実施例 4
実施例1で用いたTGICと安息香酸の反応物14
部を〔η〕=0.72のポリエチレンテレフタレート
チツプ2000部に添加し、タンブラー中で混合した
後L/D=25の30mmφ押出機により280℃で押出
した。得られた変性ポリエチレンテレフタレート
のペレツト1050部に375部の3mmチヨツプドスト
ランドと75部のガラス箔(200メツシユ以下、厚
さ3μ)を添加混合し、同じ押出機で押出した後
実施例1と同様に射出成形を行ない物性を評価し
た。成形品は着色の無い光沢の良好なもので、引
張強度は1820Kg/cm2、熱変形温度は235℃と高い
値を示し、シヨートシヨツトのゲージ圧も18Kg/
cm2で成形性も良好であつた。[Table] Example 4 Reactant 14 of TGIC and benzoic acid used in Example 1
1 part was added to 2000 parts of polyethylene terephthalate chips with [η] = 0.72, mixed in a tumbler, and then extruded at 280°C using a 30 mmφ extruder with L/D = 25. Example 1 After adding and mixing 375 parts of 3 mm chopped strands and 75 parts of glass foil (200 mesh or less, thickness 3 μm) to 1050 parts of the obtained modified polyethylene terephthalate pellets and extruding them using the same extruder. Injection molding was performed in the same manner as above, and the physical properties were evaluated. The molded product has good gloss with no coloration, has a tensile strength of 1820Kg/cm 2 , a high heat distortion temperature of 235℃, and a shot shot gauge pressure of 18Kg/cm 2 .
The moldability was also good at cm2 .
Claims (1)
環を有するエポキシ化合物1モルに対し芳香族カ
ルボン酸又はその酸無水物0.5〜2モルを反応さ
せて得た反応物をポリエチレンテレフタレートに
対し0.05〜5重量%及び全組成物中10〜50重量%
の繊維状補強充填剤と1〜40重量%のガラス箔か
らなることを特徴とする強化ポリエチレンテレフ
タレート組成物。1 A reaction product obtained by reacting 0.5 to 2 moles of an aromatic carboxylic acid or its acid anhydride to 1 mole of polyethylene terephthalate and an epoxy compound having a triazine ring is added to the polyethylene terephthalate in an amount of 0.05 to 5% by weight and based on the total composition. 10-50% by weight
A reinforced polyethylene terephthalate composition comprising a fibrous reinforcing filler and 1 to 40% by weight of glass foil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18028985A JPS6195059A (en) | 1985-08-16 | 1985-08-16 | Reinforced polyethylene terephthalate composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18028985A JPS6195059A (en) | 1985-08-16 | 1985-08-16 | Reinforced polyethylene terephthalate composition |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6017077A Division JPS53144955A (en) | 1977-05-23 | 1977-05-23 | Reinforced polyethylene terephthalate composition and its production |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6195059A JPS6195059A (en) | 1986-05-13 |
| JPS6357466B2 true JPS6357466B2 (en) | 1988-11-11 |
Family
ID=16080605
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18028985A Granted JPS6195059A (en) | 1985-08-16 | 1985-08-16 | Reinforced polyethylene terephthalate composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6195059A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4948823A (en) * | 1988-12-01 | 1990-08-14 | Polysar Financial Services S.A. | Nucleating systems |
| JP2012092309A (en) * | 2010-09-29 | 2012-05-17 | Shikoku Chem Corp | Epoxy resin composition |
-
1985
- 1985-08-16 JP JP18028985A patent/JPS6195059A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6195059A (en) | 1986-05-13 |
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