JPS6328127B2 - - Google Patents
Info
- Publication number
- JPS6328127B2 JPS6328127B2 JP54120007A JP12000779A JPS6328127B2 JP S6328127 B2 JPS6328127 B2 JP S6328127B2 JP 54120007 A JP54120007 A JP 54120007A JP 12000779 A JP12000779 A JP 12000779A JP S6328127 B2 JPS6328127 B2 JP S6328127B2
- Authority
- JP
- Japan
- Prior art keywords
- polyester
- fiber
- dicarboxylic acid
- acid component
- polymerization
- 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
- 229920000728 polyester Polymers 0.000 claims description 29
- 239000000835 fiber Substances 0.000 claims description 23
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 13
- 239000000203 mixture Substances 0.000 claims description 11
- 238000006116 polymerization reaction Methods 0.000 claims description 11
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 claims description 8
- 150000002148 esters Chemical class 0.000 claims description 8
- 239000000178 monomer Substances 0.000 claims description 7
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims description 6
- 230000003014 reinforcing effect Effects 0.000 claims description 5
- LLLVZDVNHNWSDS-UHFFFAOYSA-N 4-methylidene-3,5-dioxabicyclo[5.2.2]undeca-1(9),7,10-triene-2,6-dione Chemical compound C1(C2=CC=C(C(=O)OC(=C)O1)C=C2)=O LLLVZDVNHNWSDS-UHFFFAOYSA-N 0.000 claims description 4
- -1 polyethylene terephthalate Polymers 0.000 description 11
- 229920000139 polyethylene terephthalate Polymers 0.000 description 7
- 239000005020 polyethylene terephthalate Substances 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 125000003367 polycyclic group Chemical group 0.000 description 5
- 239000002253 acid Substances 0.000 description 3
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 230000006866 deterioration Effects 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- NEQFBGHQPUXOFH-UHFFFAOYSA-N 4-(4-carboxyphenyl)benzoic acid Chemical compound C1=CC(C(=O)O)=CC=C1C1=CC=C(C(O)=O)C=C1 NEQFBGHQPUXOFH-UHFFFAOYSA-N 0.000 description 2
- 238000007259 addition reaction Methods 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 239000012779 reinforcing material Substances 0.000 description 2
- 238000009987 spinning Methods 0.000 description 2
- 238000004804 winding Methods 0.000 description 2
- ISPYQTSUDJAMAB-UHFFFAOYSA-N 2-chlorophenol Chemical compound OC1=CC=CC=C1Cl ISPYQTSUDJAMAB-UHFFFAOYSA-N 0.000 description 1
- 229920001634 Copolyester Polymers 0.000 description 1
- GHKOFFNLGXMVNJ-UHFFFAOYSA-N Didodecyl thiobispropanoate Chemical compound CCCCCCCCCCCCOC(=O)CCSCCC(=O)OCCCCCCCCCCCC GHKOFFNLGXMVNJ-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
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000004760 aramid Substances 0.000 description 1
- 150000004982 aromatic amines Chemical class 0.000 description 1
- 229920003235 aromatic polyamide Polymers 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
- 239000013078 crystal Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002074 melt spinning Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000008247 solid mixture Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
Description
本発明はポリエステル繊維に関するものであ
り、更に詳しくはゴム製品を補強するためのコー
ド用に適した、耐熱安定性の改善されたポリエス
テル繊維に関するものである。
近年自動車の走行速度の増大及び飛行機の離着
陸速度の高速化によつて空気入りタイヤは次第に
苛酷な取扱いをうけるようになつた。このため、
高速度又は重荷重下の取扱いによる苛烈な衝撃と
高温度に抗するように企画された改良ゴム補強コ
ードを提供するために種々の試みがなされてき
た。たとえばガラス繊維、スチール繊維などの無
機質素材や分子鎖の剛直な全芳香族ポリアミド繊
維などは、それらの例である。他方、より汎用的
合成繊維として高い強度と低い平衡水分率を有す
るポリエチレンテレフタレートからなるゴム補強
コードは優れた寸法安定性、熱的劣化に対して高
度の抵抗を有することが知られているが高温度を
発する重荷重、高速度の条件のものでは引張強度
が著しく低下する。
ポリエチレンテレフタレート繊維のこのように
な欠点は、分子鎖の遊離カルボキシル基が多く加
水分解による解重合が一因であつたり繊維構造に
おいて非晶部分の構造がルーズでゴム中に含まれ
るアミン化合物類によつて化学的に劣化させられ
るためと考えられている。特に前者に対しては遊
離カルボキシル基を低下させる幾つかの改良がな
されているが、これらによつては同時に後者の要
因を除去することができないのが現状である。
本発明者の目的は上記2つの要因によるタイヤ
コードの欠点を排除して高温度を発する重荷重、
高速度の条件下でも、充分な強度を有し特にゴム
補強材用として有用なポリエステル繊維を提供す
ることにある。更に本発明の他の目的は比較的容
易に低コストで所望のポリエステル繊維を提供す
ることにある。
本発明によれば
エチレンテレフタレートを主たる繰返し単位と
して含有するポリエステルに該ポリエステルの重
量を基準として縮合多環又は少なくとも2個のベ
ンゼン環を有するジカルボン酸成分とエチレング
リコール成分とからなるエステルのモノマー又は
重合度が10以下のプレポリマーを0.5〜7重量%
添加反応させてなる組成物からなる繊維であつ
て、破断伸度が20%以下であるゴム補強コード用
ポリエステル繊維
が提供される。
本発明において、“ポリエステル”とは、エチ
レンテレフタレート繰返し単位を主たる構成成分
とするものでポリエチレンテレフタレートを主た
る対象とするがその性質を本質的に変化させない
範囲(例えば15モル%以下)で第3成分を共重合
させたコポリエステルでもよい。更には斯界でよ
く知られている添加剤特に耐熱安定剤、たとえば
立体障害フエノール(Irganox)、芳香族アミ
ン(スミライザーPB)、含リン化合物、含硫黄
化合物(スミライザーTPL)を上記ポリエス
テルに添加含有させることも本発明では有用であ
る。
更に上記ポリエステルの重合度はポリエステル
の種類やその用途に応じて適宜選定すべきである
が、一般にポリエチレンテレフタレートの場合35
℃のo−クロロフエノール溶液で測定した固有粘
度が0.5以上のものが適当である。しかし固有粘
度が0.90を越えると後述する如く、エステル乃至
プレポリマーの添加反応後の組成物の溶融粘度が
増大し繊維状に溶融成型するのに多くの困難を伴
うので0.5〜0.9とするのが望ましい。
本発明において上記ポリエステルに縮合多環又
は少くとも2個のベンゼン環を有するジカルボン
酸成分からなるエステルのモノマー又は重合度が
10以下のプレポリマーを0.5〜7.0重量%添加反応
させてポリエステル組成物をうる。
ここで縮合多環又は少くとも2個のベンゼン環
を有するジカルボン酸成分としては、たとえば下
記構造式で示されるものが挙げられる。
これらのジカルボン酸成分はエチレングリコー
ル成分とエステルを形成させ、モノマーのまま或
はオリゴマーを含む重合度10以下のプレポリマー
の状態でポリエステルに添加反応させる。
本発明では上記ジカルボン酸成分より得られた
エステルのモノマー又は重合度10以下のプレポリ
マーをポリエステルの重合完結前又はポリエステ
ルの重合完結後に添加する。一般に、ポリエステ
ルの重合完結前にモノマー又はプレポリマーを添
加する場合は、添加混合後、その系を少くとも
280℃以上に保持することにより、ポリエチレン
テレフタレートと反応させることが好適である。
また、ポリエステルの重合完結後添加混合する場
合には、該ポリエステルをペレツト又は粉末状に
し、他方の上記ジカルボン酸成分より得られるエ
ステルのモノマー又はプレポリマーを粉末状と
し、ドラムタンブラー、リボンブレンダー等を用
いて充分混合後両者を280℃以上の温度で加熱反
応させるか、又は固体状で混合されたものをその
まま280℃以上で溶融紡糸し、その溶融紡糸中に
反応させてもよい。いずれにしても線状ポリエチ
レンテレフタレート分子末端に少くとも上記酸成
分が有効的に反応するようにポリエステルに対し
て0.5〜0.7重量%の範囲で添加し280℃以上に加
熱混合することが必要である。この場合、該添加
量が0.5%未満では所望の耐熱安定性の効果がな
く、また7%を越えると線状ポリエチレンフタレ
ートの分子鎖中にランダムに酸成分が組み込まれ
るため、得られるポリエステル組成物の融点降下
が大きく所望の耐熱安定性の効果が得られなくな
る。
本発明における耐熱安定性良好なポリエステル
繊維は一般に、上記の如くして得られたポリエス
テル組成物を溶融成型可能な程度の溶融粘度に調
整後、紡糸口金より吐出せしめ常法により繊維状
に成型することによつて得ることができる。
この場合、吐出後冷却し一旦未延伸糸状に巻取
つた後別工程で加熱延伸熱処理する方法、吐出後
冷却し一旦未延伸糸状に巻取らずに直ちに加熱延
伸熱処理する方法など随時採用することができ
る。特に後者の直延伸法においては溶融吐出後未
だ固化していない糸条に直ちに2段延伸熱処理す
ることが得られる繊維の性能の点で有用である。
上記延伸により、得られる繊維の破断伸度は、ゴ
ム補強コード用ポリエステル繊維に従来より普通
に採用されている20%以下に調整される。
本発明のポリエステル繊維においては、添加反
応する縮合多環又は少くとも2個のベンゼン環を
有するジカルボン酸成分からなるエステルが分子
末端に結合し、結果的に遊離カルボキシル濃度の
比較的低いポリエステル繊維になつているのみな
らず繊維状に成型し配向結晶化を行わしめて繊維
構造を組織化した場合たとえば結晶相−非晶相の
如き2層構造モデルにあつては非晶相が縮合多環
又は少くとも2個のベンゼン環の存在により比較
的緻密になつているために耐薬品性(特にアミ
ン)に優れているという特徴を有する。又溶融成
型法の組み合せによつては繊維構造が比較的均質
構造で結晶相−必晶相が明瞭でないのでアミン分
解に対しても比較的安定である。従つて本発明で
得られるポリエステル繊維を常法によりコードに
しゴム補強に使用すれば、高温度を発する重荷重
と高速度の条件のもとでも強力低下が少く極めて
有用な補強材となる。
以下本発明の実施例を詳述するが本発明はこれ
に限定されるものではない。
実施例 1
固有粘度が0.71のポリエチレンテレフタレート
ペレツトに4,4′−ジフエニルジカルボン酸のエ
チレングリコールのジエステルの粉末を1.5重量
%混合し、160℃で6時間乾燥後エクストルーダ
ーを備えた溶融紡糸機に供給し、最高300℃の温
度に加熱溶融し孔径0.4mm、孔数192個の紡糸口金
より吐出し、冷却後オイリングして400m/min
で巻取つた。然る後80m/minで回転している
100℃の加熱ロール、140℃に加熱されている第2
ロール、195℃に加熱されている第3ロールを用
いて、全延伸倍率6.0に延伸し、熱処理した。
得られた糸条を250℃の恒温槽で60分定長及び
弛緩熱劣化させた場合の強度、伸度維持率を第1
表に示す。
なお、実験No.2は4,4′−ジフエニルジカルボ
ン酸のエチレングリコールジエステルを添加混合
しない比較例である。
The present invention relates to polyester fibers, and more particularly to polyester fibers with improved heat resistance stability suitable for cords for reinforcing rubber products. In recent years, pneumatic tires have come to be increasingly subjected to harsh handling due to the increase in the traveling speed of automobiles and the faster takeoff and landing speeds of airplanes. For this reason,
Various attempts have been made to provide improved rubber reinforced cords designed to withstand the severe impacts and high temperatures of handling at high speeds or under heavy loads. Examples include inorganic materials such as glass fibers and steel fibers, and wholly aromatic polyamide fibers with rigid molecular chains. On the other hand, as a more general-purpose synthetic fiber, rubber reinforced cord made of polyethylene terephthalate, which has high strength and low equilibrium moisture content, is known to have excellent dimensional stability and high resistance to thermal deterioration. Tensile strength decreases significantly under heavy load and high speed conditions that generate heat. These disadvantages of polyethylene terephthalate fibers may be due to the large number of free carboxyl groups in the molecular chain and depolymerization due to hydrolysis, or the loose structure of the amorphous portion of the fiber structure, which may cause the amine compounds contained in the rubber to This is thought to be due to chemical deterioration. In particular, some improvements have been made to reduce the number of free carboxyl groups for the former, but the current situation is that these cannot simultaneously eliminate the latter factor. The purpose of the present inventor is to eliminate the drawbacks of tire cords due to the above two factors, and to eliminate heavy loads that generate high temperatures.
The object of the present invention is to provide a polyester fiber that has sufficient strength even under high speed conditions and is particularly useful as a rubber reinforcing material. Yet another object of the present invention is to provide desired polyester fibers relatively easily and at low cost. According to the present invention, a monomer or polymerization of an ester consisting of a dicarboxylic acid component having a polycyclic condensation or at least two benzene rings and an ethylene glycol component based on the weight of the polyester containing ethylene terephthalate as a main repeating unit. 0.5 to 7% by weight of prepolymer with a degree of less than 10
Provided is a polyester fiber for a rubber reinforcing cord, which is a fiber made of a composition obtained by an additive reaction and has a breaking elongation of 20% or less. In the present invention, "polyester" refers to a substance whose main constituent is ethylene terephthalate repeating units, and which contains polyethylene terephthalate as its main component, but contains a third component within a range that does not essentially change its properties (for example, 15 mol% or less). A copolyester obtained by copolymerizing may also be used. Furthermore, additives well known in the field, particularly heat stabilizers, such as sterically hindered phenols (Irganox), aromatic amines (Sumilizer PB), phosphorus-containing compounds, and sulfur-containing compounds (Sumilizer TPL) are added to the above polyester. This is also useful in the present invention. Furthermore, the degree of polymerization of the above-mentioned polyester should be selected appropriately depending on the type of polyester and its use, but generally in the case of polyethylene terephthalate, the degree of polymerization is 35%.
A suitable material has an intrinsic viscosity of 0.5 or more as measured with an o-chlorophenol solution at °C. However, as will be described later, if the intrinsic viscosity exceeds 0.90, the melt viscosity of the composition increases after the addition reaction of the ester or prepolymer, making it difficult to melt and mold it into a fiber shape. desirable. In the present invention, the monomer or degree of polymerization of the ester consisting of a dicarboxylic acid component having a condensed polycyclic ring or at least two benzene rings is added to the polyester.
A polyester composition is obtained by adding and reacting 0.5 to 7.0% by weight of a prepolymer of 10 or less. Examples of the dicarboxylic acid component having a condensed polycyclic ring or at least two benzene rings include those represented by the following structural formula. These dicarboxylic acid components form esters with the ethylene glycol component, and are added to the polyester as monomers or in the form of prepolymers containing oligomers with a degree of polymerization of 10 or less. In the present invention, an ester monomer obtained from the dicarboxylic acid component or a prepolymer having a degree of polymerization of 10 or less is added before or after the completion of polyester polymerization. Generally, when monomers or prepolymers are added before the completion of polymerization of polyester, the system is at least
It is preferable to react with polyethylene terephthalate by maintaining the temperature at 280°C or higher.
In addition, when the polyester is added and mixed after completion of polymerization, the polyester is made into pellets or powder, and the ester monomer or prepolymer obtained from the other dicarboxylic acid component is made into powder, and a drum tumbler, ribbon blender, etc. After sufficiently mixing the two, the mixture may be reacted by heating at a temperature of 280° C. or higher, or the solid mixture may be melt-spun as it is at a temperature of 280° C. or higher, and the reaction may be caused during the melt-spinning. In any case, it is necessary to add at least the above acid component to the end of the linear polyethylene terephthalate molecule in a range of 0.5 to 0.7% by weight based on the polyester and heat and mix at 280°C or higher so that at least the above acid component reacts effectively. . In this case, if the amount added is less than 0.5%, the desired heat-resistant stability effect will not be achieved, and if it exceeds 7%, the acid component will be randomly incorporated into the molecular chain of the linear polyethylene phthalate, so that the resulting polyester composition The melting point decreases significantly, making it impossible to obtain the desired heat-resistant stability effect. The polyester fiber with good heat resistance stability in the present invention is generally produced by adjusting the polyester composition obtained as described above to a melt viscosity that allows melt molding, and then extruding it from a spinneret and molding it into a fiber by a conventional method. It can be obtained by In this case, a method may be adopted as needed, such as a method of cooling after discharge, winding it into an undrawn filament and then heating and stretching heat treatment in a separate process, or a method of cooling after discharge and immediately heating and stretching heat treatment without winding it into an undrawn filament. can. In particular, in the latter direct drawing method, it is useful in terms of the performance of the resulting fibers that the unsolidified yarn is immediately subjected to a two-step drawing heat treatment after being melted and discharged.
By the above-mentioned stretching, the elongation at break of the resulting fiber is adjusted to 20% or less, which has conventionally been commonly used for polyester fibers for rubber reinforcing cords. In the polyester fiber of the present invention, the ester consisting of a dicarboxylic acid component having a condensed polycyclic ring or at least two benzene rings that undergoes an addition reaction is bonded to the molecular terminal, resulting in a polyester fiber with a relatively low free carboxyl concentration. For example, in the case of a two-layer structure model such as a crystalline phase and an amorphous phase, when the fiber structure is organized by forming it into a fibrous shape and performing oriented crystallization, the amorphous phase is a condensed polycyclic or amorphous phase. Both have excellent chemical resistance (especially to amines) because they are relatively dense due to the presence of two benzene rings. Also, depending on the combination of melt molding methods, the fiber structure is relatively homogeneous and the crystal phase-obligatory phase is not clear, so it is relatively stable against amine decomposition. Therefore, if the polyester fiber obtained by the present invention is made into a cord by a conventional method and used for reinforcing rubber, it will become an extremely useful reinforcing material with little loss of strength even under conditions of heavy loads and high speeds that generate high temperatures. Examples of the present invention will be described in detail below, but the present invention is not limited thereto. Example 1 Polyethylene terephthalate pellets with an intrinsic viscosity of 0.71 were mixed with 1.5% by weight of powder of ethylene glycol diester of 4,4'-diphenyldicarboxylic acid, dried at 160°C for 6 hours, and then melt-spun using an extruder. It is fed to a spinning machine, heated and melted to a maximum temperature of 300℃, discharged from a spinneret with a hole diameter of 0.4 mm and 192 holes, cooled, and oiled at a speed of 400 m/min.
I rolled it up. After that, it rotates at 80m/min.
Heated roll at 100℃, second heated at 140℃
Using a roll and a third roll heated to 195° C., the film was stretched to a total stretching ratio of 6.0 and heat-treated. The strength and elongation retention rate when the obtained yarn was subjected to constant length and relaxation heat deterioration for 60 minutes in a constant temperature bath at 250°C were
Shown in the table. Note that Experiment No. 2 is a comparative example in which ethylene glycol diester of 4,4'-diphenyl dicarboxylic acid was not added or mixed.
【表】
実施例 2
エチレンテレフタレートを常法により重合し、
重合完結10分前に別途作成していたエチレン−
2,6−ナフタレートの5量体を添加し、320℃
で10分間反応させ、固有粘度0.67のポリエステル
組成物を得た。この組成物をエクストルーダーを
備えた紡糸機に供給し、330℃で溶融し[実施例
1]と同様にして、紡糸し延伸して延伸糸を得
た。次いでこの延伸糸を250℃の乾熱恒温槽で60
分定長で熱劣化させた場合の強度、伸度維持率を
第3表に示す。[Table] Example 2 Ethylene terephthalate was polymerized by a conventional method,
Ethylene was prepared separately 10 minutes before polymerization was completed.
Add 2,6-naphthalate pentamer and heat at 320℃
The mixture was reacted for 10 minutes to obtain a polyester composition with an intrinsic viscosity of 0.67. This composition was supplied to a spinning machine equipped with an extruder, melted at 330°C, and spun and drawn in the same manner as in Example 1 to obtain a drawn yarn. Next, this drawn yarn was heated in a dry heat constant temperature bath at 250℃ for 60 minutes.
Table 3 shows the strength and elongation retention rate when thermally degraded over a certain length.
Claims (1)
として含有するポリエステルに、該ポリエステル
の重量を基準として縮合多環又は少なくとも2個
のベンゼン環を有するジカルボン酸成分とエチレ
ングリコール成分とからなるエステルのモノマー
又は重合度が10以下のプレポリマーを0.5〜7重
量%添加反応させてなる組成物からなる繊維であ
つて、破断伸度が20%以下であるゴム補強コード
用ポリエステル繊維。1 A polyester containing ethylene terephthalate as a main repeating unit is added with a monomer of an ester consisting of a dicarboxylic acid component having a condensed polycycle or at least two benzene rings and an ethylene glycol component, or a polymerization degree of 10 based on the weight of the polyester. A polyester fiber for rubber reinforcing cord, which is a fiber made of a composition obtained by adding and reacting 0.5 to 7% by weight of the following prepolymers, and having a breaking elongation of 20% or less.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12000779A JPS5649014A (en) | 1979-09-20 | 1979-09-20 | Polyester fiber with improved heat stability |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12000779A JPS5649014A (en) | 1979-09-20 | 1979-09-20 | Polyester fiber with improved heat stability |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5649014A JPS5649014A (en) | 1981-05-02 |
JPS6328127B2 true JPS6328127B2 (en) | 1988-06-07 |
Family
ID=14775589
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12000779A Granted JPS5649014A (en) | 1979-09-20 | 1979-09-20 | Polyester fiber with improved heat stability |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5649014A (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61266613A (en) * | 1985-05-22 | 1986-11-26 | Teijin Ltd | Production of polyester fiber |
US5397527A (en) * | 1991-12-30 | 1995-03-14 | Alliedsignal Inc. | High modulus polyester yarn for tire cords and composites |
US5688874A (en) * | 1995-12-22 | 1997-11-18 | Eastman Chemical Company | Process for preparing blends of poly(ethylene terephthalate) and poly(ethylene 2,6-naphthalenedicarboxylate) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS495231A (en) * | 1972-04-28 | 1974-01-17 | ||
JPS5637329A (en) * | 1979-08-31 | 1981-04-11 | Teijin Ltd | Raw yarn for weft yarn of tire cord fabric |
-
1979
- 1979-09-20 JP JP12000779A patent/JPS5649014A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS495231A (en) * | 1972-04-28 | 1974-01-17 | ||
JPS5637329A (en) * | 1979-08-31 | 1981-04-11 | Teijin Ltd | Raw yarn for weft yarn of tire cord fabric |
Also Published As
Publication number | Publication date |
---|---|
JPS5649014A (en) | 1981-05-02 |
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