JPH0221420B2 - - Google Patents
Info
- Publication number
- JPH0221420B2 JPH0221420B2 JP2278782A JP2278782A JPH0221420B2 JP H0221420 B2 JPH0221420 B2 JP H0221420B2 JP 2278782 A JP2278782 A JP 2278782A JP 2278782 A JP2278782 A JP 2278782A JP H0221420 B2 JPH0221420 B2 JP H0221420B2
- Authority
- JP
- Japan
- Prior art keywords
- melting point
- high melting
- polyester elastomer
- pbt
- glycol
- 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
- 238000002844 melting Methods 0.000 claims description 28
- 230000008018 melting Effects 0.000 claims description 28
- 229920001971 elastomer Polymers 0.000 claims description 26
- 239000000806 elastomer Substances 0.000 claims description 25
- 229920000728 polyester Polymers 0.000 claims description 24
- 229920001707 polybutylene terephthalate Polymers 0.000 claims description 23
- -1 polybutylene terephthalate Polymers 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 9
- 239000004721 Polyphenylene oxide Substances 0.000 claims description 5
- 125000003118 aryl group Chemical group 0.000 claims description 5
- 229920000570 polyether Polymers 0.000 claims description 5
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 15
- 238000002425 crystallisation Methods 0.000 description 7
- 230000008025 crystallization Effects 0.000 description 7
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 6
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 6
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 238000000465 moulding Methods 0.000 description 5
- 230000001737 promoting effect Effects 0.000 description 5
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 4
- 239000008188 pellet Substances 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 125000001931 aliphatic group Chemical group 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- WOZVHXUHUFLZGK-UHFFFAOYSA-N dimethyl terephthalate Chemical compound COC(=O)C1=CC=C(C(=O)OC)C=C1 WOZVHXUHUFLZGK-UHFFFAOYSA-N 0.000 description 2
- USIUVYZYUHIAEV-UHFFFAOYSA-N diphenyl ether Chemical compound C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 description 2
- KZTYYGOKRVBIMI-UHFFFAOYSA-N diphenyl sulfone Chemical compound C=1C=CC=CC=1S(=O)(=O)C1=CC=CC=C1 KZTYYGOKRVBIMI-UHFFFAOYSA-N 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 238000010438 heat treatment Methods 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
- 239000012299 nitrogen atmosphere Substances 0.000 description 2
- YPFDHNVEDLHUCE-UHFFFAOYSA-N propane-1,3-diol Chemical compound OCCCO YPFDHNVEDLHUCE-UHFFFAOYSA-N 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- ISPYQTSUDJAMAB-UHFFFAOYSA-N 2-chlorophenol Chemical compound OC1=CC=CC=C1Cl ISPYQTSUDJAMAB-UHFFFAOYSA-N 0.000 description 1
- XCSGHNKDXGYELG-UHFFFAOYSA-N 2-phenoxyethoxybenzene Chemical compound C=1C=CC=CC=1OCCOC1=CC=CC=C1 XCSGHNKDXGYELG-UHFFFAOYSA-N 0.000 description 1
- ALQSHHUCVQOPAS-UHFFFAOYSA-N Pentane-1,5-diol Chemical compound OCCCCCO ALQSHHUCVQOPAS-UHFFFAOYSA-N 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 229920005601 base polymer Polymers 0.000 description 1
- RWCCWEUUXYIKHB-UHFFFAOYSA-N benzophenone Chemical compound C=1C=CC=CC=1C(=O)C1=CC=CC=C1 RWCCWEUUXYIKHB-UHFFFAOYSA-N 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- YHWCPXVTRSHPNY-UHFFFAOYSA-N butan-1-olate;titanium(4+) Chemical compound [Ti+4].CCCC[O-].CCCC[O-].CCCC[O-].CCCC[O-] YHWCPXVTRSHPNY-UHFFFAOYSA-N 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- XXMIOPMDWAUFGU-UHFFFAOYSA-N hexane-1,6-diol Chemical compound OCCCCCCO XXMIOPMDWAUFGU-UHFFFAOYSA-N 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- KYTZHLUVELPASH-UHFFFAOYSA-N naphthalene-1,2-dicarboxylic acid Chemical compound C1=CC=CC2=C(C(O)=O)C(C(=O)O)=CC=C21 KYTZHLUVELPASH-UHFFFAOYSA-N 0.000 description 1
- 239000002667 nucleating agent Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N phenylbenzene Natural products C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920001451 polypropylene glycol Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Description
本発明はポリエステルエラストマー組成物に関
する。その目的とするところは、ハードセグメン
トの結晶性を向上させた、弾性特性のすぐれたエ
ラストマー組成物を提供するにある。
従来より、芳香族ポリエステルをハードセグメ
ントとし、ポリエーテルをソフトセグメントとす
るポリエステルエラストマーは、溶融成形可能な
エラストマーとして注目されていたが、その組成
的限界から、物性的にはゴムとプラスチツクスの
間に位置し、それなりの使い方が開発され、最近
になつて一部成形品、コーテイング剤等に使用さ
れ出してきた。
このエラストマーは、ハードセグメントの結晶
凝集力によつてソフトセグメントの分子の流動性
を抑制して、弾性をもたせているために、ソフト
セグメントの2次転位点を低くすると共にハード
セグメントの結晶性を向上させることが弾性特性
を改良するうえで重要な因子になつている。本発
明者らは、該ポリエステルエラストマーは、エン
トロピー弾性であるため、単なる結晶核剤ではな
く、比熱の大きな充填剤の添加効果の大きいこと
を認め、既に提案したが、核剤でも、そのマトリ
ツクスと親和性の大きいものであるならば、同等
な効果を有することを見い出し、本発明に到達し
た。
即ち本発明は、芳香族ポリエステルをハードセ
グメントとし、ポリエーテルをソフトセグメント
とするポリエステルエラストマーに、融点231℃
以上の高融点ポリブチレンテレフタレートを0.01
〜10重量%配合したことを特徴とするポリエステ
ルエラストマー組成物である。
本発明において、ハードセグメントを構成する
「芳香族ポリエステル」とは、芳香族ジカルボン
酸を主たる酸成分とし、脂肪族ジヒドロキシ化合
物を主たるグリコール成分とするポリエステルで
ある。ここに「主たる」とは、通常繰り返し単位
の80モル%以上を意味し、20モル%以下の他成分
が共重合されていてもよい。
本発明において言う芳香族ジカルボン酸として
はテレフタル酸、イソフタル酸、ナフタレンジカ
ルボン酸、ジフエニルジカルボン酸、ジフエノキ
シエタンジカルボン酸、ジフエニルエーテルジカ
ルボン酸、ジフエニルケトンジカルボン酸、ジフ
エニルスルホンジカルボン酸等が例示され、全酸
成分の50モル%以上が同一の酸からなることが好
ましい。
脂肪族ジヒドロキシ化合物としてはエチレング
リコール、トリメチレングリコール、テトラメチ
レングリコール、ペンタメチレングリコール、ヘ
キサメチレングリコール等が例示され、全グリコ
ール成分の50モル%以上は同一のジヒドロキシ化
合物からなることが好ましい。
これらのうち、テレフタル酸―テトラメチレン
グリコールの組み合せが特に好ましい。
本発明の弾性体のソフトセグメントを構成する
ポリエーテルとは、前記例示した脂肪族グリコー
ルの重合体を意味し、具体的にはポリエチレング
リコール、ポリプロピレングリコール、ポリテト
ラメチレングリコール又はこれらの共重合体が例
示される。かかるポリエーテルの分子量は500〜
6000が好ましく、800〜3000が特に好ましい。こ
れらのなかでとくにポリテトラメチレングリコー
ルが好ましい。
本発明の組成物には、高融点ポリブチレンテレ
フタレートを0.01〜10重量%配合する必要があ
る。
ここに「高融点ポリブチレンテレフタレート」
(以下「高融点PBT」と略す)とは、差動熱量計
により20℃/分で昇温した時の吸熱ピーク温度、
即ち融点(Tm℃)が231℃以上のポリブチレン
テレフタレートを言う。従来より、一般に製造、
市販されているポリブチレンテレフタレートは、
融点が220〜230℃であり通常は225〜228℃程度
で、これにα型、β型の二種の結晶構造のあるこ
とも知られている。しかし本発明で用いる高融点
PBTは、融点が231℃以上、好ましくは235℃以
上、更に240℃以上のポリマーであつて、その結
晶構造も従来のものと同じかどうかも明らかにさ
れていない。該高融点PBTは、通常のPBTポリ
マーを融点近傍、例えば200℃前後で数十時間に
わたる長時間、熱処理することによつて得られ
る。
高融点PBTは、配合するマトリツクスとなる
ベースポリマーのポリエステルエラストマーと分
子構造が類似しており、親和性を有するためであ
ろうか、少量でも結晶化促進効果が大きい。
ここに、「結晶化促進効果」は差動熱量計にて
窒素雰囲気中20℃/分の速度で250℃まで昇温し、
そこで3分間保持後、7℃/分で降温した時に出
る発熱ピーク温度(Tcd℃)と吸熱ピーク(Tm
℃)との差△T(=Tm−Tcd)によつて示され、
△Tが小さいということは「結晶化促進効果」が
大きいことを意味する。
本発明において、該高融点PBTの配合量は
0.01〜10重量%であることが必要である。0.01重
量%未満であると結晶化促進効果は小さく、逆に
10重量%を超えると促進効果はあつても、もろく
なつたり、異物感を与える等外観が悪くなる。又
繊維やフイルム等に成形する際、パツク圧、フイ
ルター過圧等が高くなり易い。好ましくは0.05
〜8重量%、更に好ましくは0.1〜5重量%であ
る。
該高融点PBTをポリエステルエラストマーへ
配合する方法は任意であるが、例えば以下の方法
がある。まず高融点PBTを平均粒子径50μ以下、
好ましくは20μ以下、更に好ましくは5μ以下に粉
砕する。
次いで、以下のような方法でポリエステルエラ
ストマーに配合する。
1 ポリエステルエラストマーの重合末期に該高
融点PBT粉末を添加し、撹拌混合後吐出する。
2 ポリエステルエラストマーペレツトを高融点
PBTとを、タンブラーやブレンダーなどの混
合機を用いて機械的に混合し、そのまま溶融成
形に供する。
3 2で得られた高融点PBTを配合したポリエ
ステルエラストマーを一度溶融押し出し、ペレ
タイザーでペレツト化した後、溶融成形に供す
る。
4 ポリエステルエラストマーの成形時、その供
給部又はベント部に高融点PBTを定量供給し
つつポリエステルエラストマーに混入してその
まま成形する。
5 高融点PBTを、押出機の供給部又はベント
部から定量供給しつつポリエステルエラストマ
ーに混入し、次いで該ポリエステルエラストマ
ーを押し出し、ペレタイザーでペレツト化した
後、溶融成形に供する。
本発明のポリエステルエラストマー組成物は、
結晶性にすぐれ、弾性特性の良好な成形品を与え
る。
成形品としては、通常の射出成形品、押出成形
品の他、フイルム、繊維等も含む。
以下実施例を挙げて本発明を具体的に説明す
る。実施例中、部は全て重量部を表わし、固有粘
度はポリマーの35℃におけるオルソクロロフエノ
ール溶液の溶液粘度から算出したものである。
又、Tmは、差動熱量計により20℃/分で昇温し
て測定した吸熱ピーク温度(℃)、即ち融点を意
味し、Tcdは差動熱量計にて、窒素雰囲気中20
℃/分の速度で250℃まで昇温し、そこで3分間
保持後、7℃/分で降温した時の吸熱ピーク温度
(℃)である。更に50%伸長弾性率は、JISL1073
(1977)合成繊維糸試験法の伸長弾性率B法によ
り、50%伸長時の伸長弾性率を測定したものであ
る。
実施例1〜5、比較例1〜2
ジメチルテレフタレート147部、テトラメチレ
ングリコール100部、数平均分子量2000のポリテ
トラメチレングリコール244部、テトラブチルチ
タネート0.31部を反応機に仕込み内温170℃でエ
ステル交換反応を行なつた。理論量の80%のメタ
ノールが溜出した時点で系を昇温し、減圧に引き
始め約30分かけて30mmHgとし、更に30分かけて
3mmHgとして以後1mmHgの真空下で内温245℃
で240分反応を行なつた。得られたポリヤーの固
有粘度は1.40であつた。
このポリエステルエラストマーに次表に掲げる
各種高融点PBTを所定量配合し、タンブラーで
混合後、押出し機で溶融押出ししてペレツト化し
た。この配合エラストマーペレツトの結晶化挙動
は同表中央欄に示した通りであつた。このペレツ
トを260℃で溶融紡糸して、135デニールの弾性糸
を得た。この弾性糸の50%伸長弾性率は同表右欄
に示す通りであつた。
The present invention relates to polyester elastomer compositions. The purpose is to provide an elastomer composition with improved crystallinity of the hard segment and excellent elastic properties. Polyester elastomers, which have aromatic polyester as a hard segment and polyether as a soft segment, have traditionally attracted attention as melt-moldable elastomers, but due to their compositional limitations, they are between rubber and plastics in terms of physical properties. Its uses have been developed, and recently it has been used in some molded products, coating agents, etc. This elastomer suppresses the fluidity of molecules in the soft segment by the crystal cohesive force of the hard segment, giving it elasticity, which lowers the secondary dislocation point of the soft segment and improves the crystallinity of the hard segment. improvement has become an important factor in improving elastic properties. The present inventors recognized that since the polyester elastomer has entropic elasticity, addition of a filler with a large specific heat is more effective than just a nucleating agent. The inventors have discovered that the same effect can be achieved if the affinity is high, and the present invention has been achieved. That is, the present invention uses a polyester elastomer with aromatic polyester as a hard segment and polyether as a soft segment, with a melting point of 231°C.
High melting point polybutylene terephthalate of more than 0.01
This is a polyester elastomer composition characterized by containing ~10% by weight. In the present invention, the "aromatic polyester" constituting the hard segment is a polyester containing an aromatic dicarboxylic acid as the main acid component and an aliphatic dihydroxy compound as the main glycol component. Here, "main" usually means 80 mol% or more of repeating units, and 20 mol% or less of other components may be copolymerized. Aromatic dicarboxylic acids referred to in the present invention include terephthalic acid, isophthalic acid, naphthalene dicarboxylic acid, diphenyl dicarboxylic acid, diphenoxyethane dicarboxylic acid, diphenyl ether dicarboxylic acid, diphenyl ketone dicarboxylic acid, diphenyl sulfone dicarboxylic acid, etc. is exemplified, and it is preferable that 50 mol% or more of the total acid components consist of the same acid. Examples of the aliphatic dihydroxy compound include ethylene glycol, trimethylene glycol, tetramethylene glycol, pentamethylene glycol, hexamethylene glycol, etc., and it is preferable that 50 mol% or more of the total glycol component is composed of the same dihydroxy compound. Among these, the combination of terephthalic acid and tetramethylene glycol is particularly preferred. The polyether constituting the soft segment of the elastomer of the present invention means a polymer of the aliphatic glycol listed above, specifically polyethylene glycol, polypropylene glycol, polytetramethylene glycol, or a copolymer thereof. Illustrated. The molecular weight of such polyether is 500~
6000 is preferred, and 800-3000 is particularly preferred. Among these, polytetramethylene glycol is particularly preferred. The composition of the present invention needs to contain 0.01 to 10% by weight of high melting point polybutylene terephthalate. Here is "high melting point polybutylene terephthalate"
(hereinafter abbreviated as "high melting point PBT") is the endothermic peak temperature when the temperature is raised at 20℃/min using a differential calorimeter.
That is, it refers to polybutylene terephthalate with a melting point (Tm°C) of 231°C or higher. Traditionally, generally manufactured,
Commercially available polybutylene terephthalate is
It has a melting point of 220-230°C, usually around 225-228°C, and is known to have two types of crystal structures: α-type and β-type. However, the high melting point used in the present invention
PBT is a polymer with a melting point of 231°C or higher, preferably 235°C or higher, and even 240°C or higher, and it is not clear whether its crystal structure is the same as conventional ones. The high melting point PBT can be obtained by heat treating a normal PBT polymer at a temperature close to its melting point, for example around 200° C., for a long period of several tens of hours. High melting point PBT has a similar molecular structure to the polyester elastomer, which is the base polymer used as the matrix to be blended, and has a strong crystallization promoting effect, perhaps because it has affinity. Here, the "crystallization promotion effect" is determined by heating up to 250°C at a rate of 20°C/min in a nitrogen atmosphere using a differential calorimeter.
Therefore, after holding for 3 minutes, the exothermic peak temperature (Tcd℃) and endothermic peak (Tm
℃) and the difference △T (= Tm - Tcd),
A small ΔT means a large "crystallization promoting effect". In the present invention, the blending amount of the high melting point PBT is
It is necessary that the content is 0.01 to 10% by weight. If it is less than 0.01% by weight, the effect of promoting crystallization is small;
If it exceeds 10% by weight, although there is a promoting effect, the appearance deteriorates, such as becoming brittle or giving a foreign body feel. Furthermore, when molding into fibers, films, etc., pack pressure, filter overpressure, etc. tend to increase. preferably 0.05
~8% by weight, more preferably 0.1~5% by weight. Although the high melting point PBT can be blended into the polyester elastomer by any method, for example, the following method can be used. First, use high melting point PBT with an average particle size of 50μ or less.
It is preferably ground to 20μ or less, more preferably 5μ or less. Next, it is blended into a polyester elastomer in the following manner. 1. Add the high melting point PBT powder to the polyester elastomer at the final stage of polymerization, stir and mix, and then discharge. 2 Polyester elastomer pellets with high melting point
PBT is mechanically mixed using a mixer such as a tumbler or blender, and the mixture is directly subjected to melt molding. 3. The polyester elastomer blended with the high melting point PBT obtained in step 2 is once melt-extruded, pelletized using a pelletizer, and then subjected to melt molding. 4. When molding polyester elastomer, high melting point PBT is supplied in a fixed amount to the supply section or vent section, mixed into the polyester elastomer, and molded as it is. 5. High melting point PBT is mixed into the polyester elastomer while being fed in a constant quantity from the feed section or vent section of the extruder, and then the polyester elastomer is extruded and pelletized using a pelletizer, followed by melt molding. The polyester elastomer composition of the present invention is
Provides molded products with excellent crystallinity and good elastic properties. Molded products include ordinary injection molded products and extrusion molded products, as well as films, fibers, etc. The present invention will be specifically explained below with reference to Examples. In the examples, all parts represent parts by weight, and the intrinsic viscosity is calculated from the solution viscosity of an orthochlorophenol solution of the polymer at 35°C.
In addition, Tm means the endothermic peak temperature (°C), that is, the melting point, measured by heating at 20 °C/min with a differential calorimeter, and Tcd means the endothermic peak temperature (°C) measured with a differential calorimeter at 20 °C/min in a nitrogen atmosphere.
This is the endothermic peak temperature (°C) when the temperature is raised to 250°C at a rate of °C/min, held there for 3 minutes, and then lowered at a rate of 7°C/min. Furthermore, the 50% elongation modulus is JISL1073
(1977) The elongation elastic modulus at 50% elongation was measured using the elongation elastic modulus B method of the synthetic fiber yarn test method. Examples 1 to 5, Comparative Examples 1 to 2 147 parts of dimethyl terephthalate, 100 parts of tetramethylene glycol, 244 parts of polytetramethylene glycol with a number average molecular weight of 2000, and 0.31 part of tetrabutyl titanate were charged into a reactor and esterified at an internal temperature of 170°C. An exchange reaction was carried out. When 80% of the theoretical amount of methanol had been distilled, the temperature of the system was raised, and the pressure began to be reduced to 30 mmHg over about 30 minutes, and then to 3 mmHg over another 30 minutes, after which the internal temperature was reduced to 245°C under a vacuum of 1 mmHg.
The reaction was carried out for 240 minutes. The intrinsic viscosity of the resulting polyar was 1.40. This polyester elastomer was blended with predetermined amounts of various high melting point PBT listed in the following table, mixed in a tumbler, and then melted and extruded in an extruder to form pellets. The crystallization behavior of this blended elastomer pellet was as shown in the center column of the same table. This pellet was melt-spun at 260°C to obtain an elastic yarn of 135 denier. The elastic modulus of this elastic yarn at 50% elongation was as shown in the right column of the same table.
【表】
この結果からも明らかなように、融点(Tm)
231℃以上の高融点PBTを添加したエラストマー
組成物(実施例1〜5)は結晶化促進効果が顕著
に認められ、弾性特性も大きく改良される。これ
に対して高融点PBTを添加しないもの(比較例
1)、融点が231℃未満のPBTを添加したもの
(比較例2)は、結晶化促進効果がなく、弾性特
性も劣つたものであつた。[Table] As is clear from this result, melting point (Tm)
In the elastomer compositions (Examples 1 to 5) to which PBT with a high melting point of 231° C. or higher is added, the effect of promoting crystallization is remarkable, and the elastic properties are also greatly improved. On the other hand, those without the addition of high melting point PBT (Comparative Example 1) and those with the addition of PBT with a melting point of less than 231°C (Comparative Example 2) had no crystallization promotion effect and had poor elastic properties. Ta.
Claims (1)
し、ポリエーテルをソフトセグメントとするポリ
エステルエラストマーに、融点231℃以上の高融
点ポリブチレンテレフタレートを0.01〜10重量%
配合したことを特徴とするポリエステルエラスト
マー組成物。1 0.01 to 10% by weight of high melting point polybutylene terephthalate with a melting point of 231°C or higher is added to a polyester elastomer with aromatic polyester as a hard segment and polyether as a soft segment.
A polyester elastomer composition comprising:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2278782A JPS58141236A (en) | 1982-02-17 | 1982-02-17 | Polyester elastomer composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2278782A JPS58141236A (en) | 1982-02-17 | 1982-02-17 | Polyester elastomer composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58141236A JPS58141236A (en) | 1983-08-22 |
JPH0221420B2 true JPH0221420B2 (en) | 1990-05-14 |
Family
ID=12092384
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2278782A Granted JPS58141236A (en) | 1982-02-17 | 1982-02-17 | Polyester elastomer composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58141236A (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007089747A1 (en) | 2006-01-27 | 2007-08-09 | General Electric Company | Articles derived from compositions containing modified polybutylene terephthalate (pbt) random copolymers derived from polyethylene terephthalate (pet) |
JP2009525358A (en) | 2006-01-27 | 2009-07-09 | ゼネラル・エレクトリック・カンパニイ | Molding composition comprising polyalkylene terephthalate and modified polybutylene terephthalate (PBT) derived from PET |
US7902263B2 (en) | 2006-01-27 | 2011-03-08 | Sabic Innovative Plastics Ip B.V. | Process for making polybutylene terephthalate (PBT) from polyethylene terephthalate (PET) |
US8309656B2 (en) | 2006-07-26 | 2012-11-13 | Sabic Innovative Plastics Ip B.V. | Elastomer blends containing polycarbonates and copolyetheresters derived from polyethylene terephthalate, method of manufacture, and articles therefrom |
US7799838B2 (en) | 2006-07-26 | 2010-09-21 | Sabic Innovative Plastics Ip B.V. | Elastomer blends of polyesters and copolyetheresters derived from polyethylene terephthalate, method of manufacture, and articles therefrom |
US8158710B2 (en) | 2006-11-27 | 2012-04-17 | Sabic Innovative Plastics Ip B.V. | Polyester blends, methods of making, and articles formed therefrom |
JP2018203833A (en) * | 2017-05-31 | 2018-12-27 | 三菱ケミカル株式会社 | Resin composition, film, multilayer film, and packaging material |
-
1982
- 1982-02-17 JP JP2278782A patent/JPS58141236A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS58141236A (en) | 1983-08-22 |
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