JPH0742616B2 - High strength polyester fiber - Google Patents
High strength polyester fiberInfo
- Publication number
- JPH0742616B2 JPH0742616B2 JP63285898A JP28589888A JPH0742616B2 JP H0742616 B2 JPH0742616 B2 JP H0742616B2 JP 63285898 A JP63285898 A JP 63285898A JP 28589888 A JP28589888 A JP 28589888A JP H0742616 B2 JPH0742616 B2 JP H0742616B2
- Authority
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- Japan
- Prior art keywords
- strength
- weight
- less
- polyester fiber
- component
- 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 - Lifetime
Links
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- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
- Artificial Filaments (AREA)
- Chemical Treatment Of Fibers During Manufacturing Processes (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は、高強力ポリエステル繊維に関する。更に詳し
くは、撚糸後レゾルシン・ホルマリン・ラテックス液
(RFL液と称す)で処理する際の発煙が少なく、また得
られる処理コードの強力が高いゴム補強用高強力ポリエ
ステル繊維に関するものである。TECHNICAL FIELD The present invention relates to high-strength polyester fibers. More specifically, the present invention relates to a high-strength polyester fiber for rubber reinforcement, which emits less smoke when treated with a resorcin / formalin / latex liquid (referred to as RFL liquid) after twisting and has a high strength in the obtained treated cord.
(従来技術) 近年、タイヤの品質の向上および生産性向上の必要性が
以前よりまして叫ばれるようになり、ポリエステル繊維
に対し高強力化,耐熱性の向上がより強く要求されつつ
ある。このため、ポリエステル繊維は、高い強度を得る
目的で、より高温でより高い倍率で延伸されることか
ら、高温高接圧時の油膜強度がすぐれ、発煙性も優れて
いる処理剤が要求されている。(Prior Art) In recent years, the need to improve tire quality and productivity has become more pronounced than ever, and there is a strong demand for higher strength and higher heat resistance of polyester fibers. Therefore, the polyester fiber is stretched at a higher temperature and a higher draw ratio for the purpose of obtaining high strength, so that a treatment agent having excellent oil film strength at high temperature and high contact pressure and excellent smoke emission is required. There is.
また、撚糸後RFL液で処理し、乾燥,熱処理を行なって
処理コードを得るが、これの強度が高く、熱処理時の発
煙が少ないことも要求されている。Further, the twisted yarn is treated with RFL liquid, dried and heat-treated to obtain a treated cord, which is required to have high strength and to emit less smoke during heat treatment.
これらの要求を満足させるために、従来より、硫黄元素
を導入した平滑剤、例えば、チオジプロピオン酸と一価
アルコールのジエステル(特開昭52-103590号公報)
や、チオジプロピオン酸と一価アルコールのEO付加物の
モノ及びジエステル(特開昭55-148216号公報)など
が、提案されている。In order to satisfy these requirements, conventionally, a leveling agent introduced with elemental sulfur, for example, a diester of thiodipropionic acid and a monohydric alcohol (JP-A-52-103590).
In addition, mono- and diesters of EO adducts of thiodipropionic acid and monohydric alcohols (JP-A-55-148216) have been proposed.
また、特に高接圧時の繊維間の摩擦を下げる目的で、高
分子量の活性剤、例えば、多価アルコールとヒドロキシ
モノカルボン酸とのエステルのアルキレンオキシド付加
物と、マレイン酸を必須成分とするカルボン酸成分との
エステル(特開昭59-223368号公報)なども提案されて
いる。Further, particularly for the purpose of reducing the friction between fibers at the time of high contact pressure, a high molecular weight activator, for example, an alkylene oxide adduct of an ester of a polyhydric alcohol and hydroxymonocarboxylic acid, and maleic acid are essential components. Esters with carboxylic acid components (JP-A-59-223368) and the like have also been proposed.
しかしながら、フィラメントの強度が8.5g/dをこえるも
のを得るためには、紡糸延伸時の糸張力を著しく増加さ
せたり、加熱温度を著しく高くする必要が有り、油膜強
度,発煙性への要求もより厳しくなって、今までの平滑
剤及び高分子量の活性剤だけの組み合わせでは、所定の
効果が得られなくなる。即ち、フィラメントの強度を増
加させても、最終的に得られる処理コード強力の増加が
見られなくなり、発煙も増加する。However, in order to obtain filaments having a strength of more than 8.5 g / d, it is necessary to remarkably increase the yarn tension during spinning and drawing, and to raise the heating temperature remarkably, and the requirements for oil film strength and smoke emission are also required. It becomes more severe, and the predetermined effect cannot be obtained with the conventional combination of only the leveling agent and the high molecular weight active agent. That is, even if the strength of the filament is increased, the strength of the finally obtained treatment cord is not increased, and the smoking is also increased.
かかる問題を解決する手段としては、平滑剤の比率を大
きくしたり、高分子活性剤を用いたり、または非含水油
剤の給油(特開昭60-9919号公報)などの方法が提案さ
れているが、これらはいずれも再乳化性(繊維上の油剤
がRFL液中へ入った時の溶解性)に劣るという問題があ
った。この再乳化性が低下すると、RFL液の粘性が変化
したり、RFL液の乳化バランスがくずれてラテックス部
分が分離したりするため好ましくないのである。そし
て、このような処理剤の再乳化性を向上させようとする
には、平滑剤の比率の低下,分子量の低下が考えられる
が、これらは、発煙性の増加,平滑性の低下の方向にあ
るため好ましくない。As means for solving such a problem, methods such as increasing the ratio of the leveling agent, using a polymer activator, or refueling a non-hydrating oil agent (JP-A-60-9919) have been proposed. However, all of them have a problem that they are inferior in re-emulsification property (solubility when the oil on the fiber enters the RFL liquid). If the re-emulsification property is lowered, the viscosity of the RFL solution is changed, or the emulsification balance of the RFL solution is disturbed and the latex portion is separated, which is not preferable. Then, in order to improve the re-emulsification property of such a treatment agent, it is considered that the ratio of the smoothing agent and the molecular weight are decreased, but these tend to increase smoke emission and decrease smoothness. It is not preferable because it exists.
(発明の目的) 本発明の目的は、フィラメントの強度が8.5g/d以上にお
いても、フィラメント強度の上昇につれて処理コード強
力の増加が見られ、かつ発煙性も低い高強力ポリエステ
ル繊維を提供することにある。(Object of the Invention) An object of the present invention is to provide a high-strength polyester fiber in which the treated cord strength is increased as the filament strength is increased even when the filament strength is 8.5 g / d or more, and the smoke emission is low. It is in.
(発明の構成) 本発明者らは、前記目的を達成するめ鋭意検討した結
果、特定分子量の硫黄含有エステル系(以下S含有エス
テル系と称すことがある)の平滑剤,エーテル系高分子
活性剤および非イオン活性剤を組み合わせて用いると、
発煙性とRFL浸透性を同時に満足するポリエステル繊維
が安定して得られることを知り本発明に到達した。すな
わち本発明は、 (a) 分子量が600以上の硫黄含有エステル化合物を
主成分とする平滑剤(A成分)を62重量%以上、 (b) 分子量が7000以上でかつ15℃で液状のエーテル
系高分子活性剤(B成分)を8重量%以上、 (c) 分子量が800以上、270C以下の非イオン活性剤
(C成分)を20重量%以下含有し、かつA+Bが90重量
%以下である 処理剤が付与されたポリエステル繊維であって、該ポリ
エステル繊維は下記(i)〜(iii)を同時に満足する
ことを特徴とする高強力ポリエステル繊維である。(Structure of the Invention) As a result of intensive studies aimed at achieving the above object, the present inventors have found that a sulfur-containing ester-based leveling agent (hereinafter sometimes referred to as S-containing ester-based) having a specific molecular weight and an ether-based polymer activator. And a combination of nonionic activators,
The inventors have reached the present invention by knowing that a polyester fiber satisfying both smoke emission and RFL permeability can be stably obtained. That is, the present invention includes (a) 62% by weight or more of a leveling agent (component A) containing a sulfur-containing ester compound having a molecular weight of 600 or more as a main component, and (b) an ether type liquid having a molecular weight of 7000 or more and a liquid at 15 ° C. 8% by weight or more of polymer activator (component B), (c) 20% by weight or less of nonionic activator (component C) having a molecular weight of 800 or more and 270C or less, and A + B of 90% by weight or less A polyester fiber having a treating agent applied thereto, which is a high-strength polyester fiber characterized by simultaneously satisfying the following (i) to (iii).
(i) フィラメント強度≧8.5g/d (ii) 発煙性≦1500 (iii) RFL浸透性≦5cm 本発明は、製糸後の最終的に得られる繊維のフィラメン
ト強度が8.5g/d以上のポリエステル繊維を対象とする。
8.5g/d未満の場合にあっては、本発明に用いる処理剤を
付与したものであっても、また従来公知の処理剤を付与
したものであっても、処理コード強力の差はほとんど発
現しない。ところが、8.5g/d以上特に9.0g/d以上の場合
には、後述するように本発明のポリエステル繊維から得
られる処理コードの強力は増大するという事実が判明し
た。(I) Filament strength ≧ 8.5 g / d (ii) Smoke generation ≦ 1500 (iii) RFL permeability ≦ 5 cm The present invention is a polyester fiber having a filament strength of 8.5 g / d or more in the final fiber after spinning. Target.
In the case of less than 8.5 g / d, even if the treatment agent used in the present invention is added, or even if the conventionally known treatment agent is added, the difference in the treatment code strength is almost expressed. do not do. However, it has been found that the strength of the treated cord obtained from the polyester fiber of the present invention increases at 8.5 g / d or more, particularly 9.0 g / d or more, as described later.
本発明で付与される処理剤を構成する平滑剤(A成分)
は、分子量が600以上の硫黄含有エステル系の平滑剤を
主成分とする必要がある(ここで主成分とはA成分中の
50重量%以上であることをいう)。硫黄含有エステルの
分子量が600未満もしくはA成分中の割合が50重量%未
満の場合には、処理剤の平滑性が劣り延伸熱処理時の糸
切れ発生,処理コードの強力低下が起り、さらには処理
コード製造時の発煙が大きいため好ましくない。また、
A成分は処理剤に対して62重量%以上である必要があ
る。62重量%未満の場合にも、処理剤の平滑性が低下す
るため好ましくない。Smoothing agent (component A) constituting the treatment agent applied in the present invention
Needs to have a sulfur-containing ester-based smoothing agent with a molecular weight of 600 or more as the main component (here, the main component is the A component).
It means 50% by weight or more). When the molecular weight of the sulfur-containing ester is less than 600 or the ratio of the component A in the component A is less than 50% by weight, the smoothness of the treating agent is poor, yarn breakage occurs during drawing heat treatment, and the strength of the treated cord decreases. It is not preferable because the smoke generated during the production of the cord is large. Also,
The component A needs to be 62% by weight or more based on the treating agent. Even if it is less than 62% by weight, the smoothness of the treating agent is deteriorated, which is not preferable.
ここで硫黄含有エステル系の平滑剤としては、分子内に
硫黄原子を有する化合物で、例えばチオジプロピオン酸
と高級アルコールのジエステル類をあげることができ
る。高級アルコールとしては、天然または合成アルコー
ルの直鎖または側鎖を有する飽和または不飽和アルコー
ル、および芳香核を含有するアルコールをあげることが
でき、これらのうち特に好ましいのは直鎖の不飽和脂肪
族アルコールである。具体的には、ジオレイルチオジプ
ロピオネートが好適に用いられる。Here, the sulfur-containing ester-based leveling agent is a compound having a sulfur atom in the molecule, and examples thereof include diesters of thiodipropionic acid and higher alcohols. Examples of higher alcohols include saturated or unsaturated alcohols having a straight chain or side chain of natural or synthetic alcohols, and alcohols containing an aromatic nucleus, and among these, particularly preferred is a straight chain unsaturated aliphatic It is alcohol. Specifically, dioleyl thiodipropionate is preferably used.
エーテル系高分子活性剤としては、通常公知の方法によ
りエチレンオキシド(EO),プロピレンオキシド(P
O),ブチレンオキシド(BO)等のアルキレンオキシド
を重合したもの(ホモポリマー,コポリマー)、または
多価アルコールに付加重合したものをあげることができ
る。かかる化合物の末端基は水酸基であっても、アルコ
キシ基,フェノキシ基であっても良い。また共重合比率
についても15℃で液状を呈するならば特に限定する必要
はない。好ましい例としては、ポリテトラメチレングリ
コールもしくはポリエチレングリコールの両末端にエチ
レンオキサイドとプロピレンオキシドをランダム付加重
合したものをあげることができる。As the ether-based polymer activator, ethylene oxide (EO), propylene oxide (P
Examples thereof include those obtained by polymerizing alkylene oxides such as O) and butylene oxide (BO) (homopolymers, copolymers), or those obtained by addition polymerization of polyhydric alcohols. The terminal group of such a compound may be a hydroxyl group, an alkoxy group or a phenoxy group. Also, the copolymerization ratio is not particularly limited as long as it shows a liquid state at 15 ° C. Preferable examples include polytetramethylene glycol or polyethylene glycol in which ethylene oxide and propylene oxide are randomly addition polymerized at both ends.
かかるポリエーテルで通常よく繊維の加工用として用い
られるものは、分子量が7000未満であるが、本発明のB
成分として用いるためには分子量が7000以上で、かつ15
℃で液状を示す必要が有り、使用比率は8重量%以上と
する必要がある。分子量が7000未満の場合では処理剤の
平滑性が劣り、固状では平滑性のばらつきが大きくなる
と同時にゴムとの接着が低下し、また使用比率が8重量
%未満の場合には処理剤の平滑性が劣るとともに処理剤
の再乳化性が悪化するため好ましくない。Such polyethers, which are often used for fiber processing, have a molecular weight of less than 7,000,
For use as a component, the molecular weight is 7,000 or more, and 15
It is necessary to show a liquid state at ° C, and it is necessary to use it in an amount of 8% by weight or more. When the molecular weight is less than 7,000, the smoothness of the treating agent is poor, and when it is solid, the smoothness of the treating agent becomes large, and at the same time, the adhesion with the rubber is reduced. It is not preferable because the property is poor and the re-emulsification property of the treatment agent is deteriorated.
なお、本処理剤中では、A+Bの使用比率を90重量%以
下とする必要がある。90重量%を越えると処理剤の再乳
化性が悪くなるので好ましくない。In this treatment agent, the proportion of A + B used must be 90% by weight or less. If it exceeds 90% by weight, the re-emulsifying property of the treating agent is deteriorated, which is not preferable.
非イオン活性剤(C成分)としては、乳化作用を有する
とともに発煙性,平滑性に優れる多価アルコールの誘導
体、例えばヒマシ油,硬化ヒマシ油,トリメチロールプ
ロパン,グリセリン等の多価アルコールにエチレンオキ
シドを5〜40モル付加したもの、およびこれらのエチレ
ンオキシド付加多価アルコールと脂肪族カルボン酸のエ
ステル等があげられる。具体的には、ポリオキシエチレ
ン硬化ヒマシ油エーテル,ポリオキシエチレンソルビタ
ントリオレート等があげられる。かかる非イオン活性剤
(C成分)の分子量は800以上、2700以下で、その使用
割合は20重量%以下である必要がある。分子量が800未
満の場合には処理剤の発煙性が多くなるし、一方使用割
合が20重量%を越えると処理剤の平滑性が損われるため
好ましくない。As the nonionic activator (C component), a polyhydric alcohol derivative having an emulsifying action and excellent in smoke emission and smoothness, such as castor oil, hydrogenated castor oil, trimethylolpropane, and glycerin, are mixed with ethylene oxide. Examples thereof include those added with 5 to 40 moles, and esters of these ethylene oxide-added polyhydric alcohols and aliphatic carboxylic acids. Specific examples thereof include polyoxyethylene hydrogenated castor oil ether and polyoxyethylene sorbitan trioleate. The molecular weight of the nonionic activator (component C) is 800 or more and 2700 or less, and the usage ratio thereof is required to be 20% by weight or less. If the molecular weight is less than 800, the fuming property of the treating agent is increased, while if the proportion used exceeds 20% by weight, the smoothness of the treating agent is impaired, which is not preferable.
本発明の処理剤は、上記A,B,C成分の他に、制電剤、乳
化補助剤,酸化安定剤等を少量添加しても何ら差し支え
ない。例えば制電剤としては、オレイルフォスフェート
及びその塩(Na,K,アミン等)、ポリオキシエチレンオ
レイルフォスフェート及びその塩(Na,K,アミン等)、
ジオクチルスルフォサクシネートNa塩、アルカンスルフ
ォネート及びその塩(Na,K,アミン等)があげられる。In the treatment agent of the present invention, in addition to the components A, B and C, a small amount of an antistatic agent, an emulsification aid, an oxidation stabilizer, etc. may be added. For example, as an antistatic agent, oleyl phosphate and its salt (Na, K, amine, etc.), polyoxyethylene oleyl phosphate and its salt (Na, K, amine, etc.),
Examples include dioctyl sulfosuccinate Na salt, alkane sulfonate and salts thereof (Na, K, amine, etc.).
かかる処理剤をポリエステル繊維に付与するには、非含
水型または水で乳化したエマルジョンの形で、紡糸工程
において、ローラー給油,ノズル給油など従来より公知
の方法をとりうるが、フィラメント強度を8.5g/d以上と
するには高速製糸,高温熱処理が必要なため、非含水型
処理剤をノズル給油法で行うことが好ましい。To impart such a treating agent to polyester fibers, conventionally known methods such as roller lubrication and nozzle lubrication can be used in the spinning step in the form of a non-hydrous type or an emulsion emulsified with water, but the filament strength is 8.5 g. Since high-speed spinning and high-temperature heat treatment are required to achieve a value of / d or more, it is preferable to use a non-water-containing treatment agent by a nozzle lubrication method.
処理剤の付着量は、繊維に対し0.1〜2.0重量%、好まし
くは0.2〜1.0重量%とするのが望ましい。The amount of the treatment agent attached is preferably 0.1 to 2.0% by weight, more preferably 0.2 to 1.0% by weight, based on the fibers.
かくして得られるポリエステル繊維は、後述する230℃
で測定した発煙性が1500以下およびRFL浸透性が5cm以下
に維持されるという効果も呈する。発煙性が1500を越え
る場合には、RFL液で浸漬処理して処理コードとなす際
発煙が多くなる。またRFL浸透性が5cmを越えると、処理
コードの内部までRFL液が浸透し、コードを構成する各
フィラメントの動きを拘束するためと考えられるが、処
理コードの強力が低下する傾向にある。The polyester fiber thus obtained has a temperature of 230 ° C. which will be described later.
It also has the effect of maintaining the smoke emission of 1500 or less and the RFL permeability of 5 cm or less as measured by. If the smoke emission exceeds 1500, the amount of smoke increases when the treatment code is formed by immersion treatment with RFL solution. Further, if the RFL permeability exceeds 5 cm, it is considered that the RFL liquid permeates into the inside of the treated cord and restricts the movement of each filament constituting the cord, but the strength of the treated cord tends to decrease.
なお、本発明で用いるポリエステル繊維は、ポリエチレ
ンテレフタレートまたはこれを主体とするポリエステル
を、常法に従いエクストルーダにて溶融後、直接紡糸延
伸して得られるものである。The polyester fiber used in the present invention is obtained by directly spinning and drawing polyethylene terephthalate or a polyester mainly containing polyethylene terephthalate after melting in an extruder according to a conventional method.
(作用) フィラメント強度が8.5g/d以上の場合に、何故本発明の
効果が現れるかは、定かでないが現状では次のように考
えられる。(Function) It is not clear why the effect of the present invention appears when the filament strength is 8.5 g / d or more, but it is considered as follows at present under the present circumstances.
フィラメント強度を8.5g/d以上にするためには、ポリエ
ステル繊維の結晶化度及び配向度を極めて高くする必要
が有り、繊維表面の状態が変わり(繊維間の摩擦等が変
わる)、また伸度も低めの方向になる。その結果、コー
ドの引っ張り挙動が変わってくるために、処理コードの
強力をあげるには繊維間の平滑性をより一層向上させる
必要がでてくる。In order to increase the filament strength to 8.5 g / d or more, it is necessary to make the degree of crystallinity and orientation of the polyester fiber extremely high, the state of the fiber surface changes (friction between fibers changes), and the elongation Will also be lower. As a result, the tensile behavior of the cord is changed, and it is necessary to further improve the smoothness between fibers in order to increase the strength of the treated cord.
この要求を達成するために本発明で用いる処理剤は前記
構成をとっており、耐熱性が高く、また処理剤の表面強
度が高くなっている(フィラメント間の接圧が高くなっ
ても処理剤の膜がフィラメント表面に強固に被着してい
る)。そのため、フィラメント強度が8.5g/d以上のポリ
エステル繊維を得るためには採用される厳しい製糸条件
(高温熱処理,高紡糸張力,高延伸張力)に耐え、フィ
ラメント表面に十分な処理剤が残存し、フィラメント間
の摩擦を低下させて延伸性を向上させる。In order to achieve this requirement, the treating agent used in the present invention has the above-mentioned constitution and has a high heat resistance and a high surface strength of the treating agent (even if the contact pressure between filaments is high, the treating agent is high). Film is firmly attached to the filament surface). Therefore, it withstands the stringent spinning conditions (high temperature heat treatment, high spinning tension, high drawing tension) adopted to obtain polyester fibers with a filament strength of 8.5 g / d or more, and sufficient treatment agent remains on the filament surface, It reduces friction between filaments and improves drawability.
また、本発明で得られたポリエステル繊維を撚糸してコ
ードとなす場合でも、処理剤の表面強度が高いので、撚
糸時にフィラメント間に大きな圧力がかかっても、フィ
ラメント間に処理剤が十分残存する。そのため、RFL液
と本発明の処理剤との相溶性の関係よりRFLの浸透性が5
cm以下となり、処理コードの内部にRFL液があまり浸透
せず、コードを構成する各フィラメントの動きが自由と
なる。その結果処理コードの強力が向上する。Even when the polyester fiber obtained in the present invention is twisted to form a cord, the surface strength of the treating agent is high, so that the treating agent remains sufficiently between the filaments even if a large pressure is applied between the filaments during the twisting. . Therefore, because of the compatibility relationship between the RFL solution and the treatment agent of the present invention, the permeability of RFL is 5
Since it becomes less than cm, the RFL liquid does not penetrate much into the inside of the treated cord, and the movement of each filament constituting the cord becomes free. As a result, the processing code becomes more powerful.
また本発明で用いる処理剤は分子量が大きく耐熱性が高
いので、処理コード製造時の高温熱処理に耐え、発煙性
も低下する。Further, since the treating agent used in the present invention has a large molecular weight and high heat resistance, it withstands a high temperature heat treatment at the time of producing a treated cord and also has a low smoke generation property.
以上の効果が同時に発現されるので、本発明の処理剤を
用いた時に限ってのみ、所期の目的が達成できるものと
考えられる。Since the above effects are simultaneously exhibited, it is considered that the intended purpose can be achieved only when the treatment agent of the present invention is used.
(発明の効果) 本発明のポリエステル繊維は、発煙性が低いので、処理
コードとなす際の作業環境が改善される。また、RFL浸
透性も低いので強力の大きい処理コードが得られ、その
工業的効果は極めて大である。(Effect of the invention) Since the polyester fiber of the present invention has a low smoke generation property, the working environment when used as a treatment cord is improved. Further, since the RFL permeability is low, a treatment code having a large strength can be obtained, and its industrial effect is extremely large.
(実施例) 以下、実施例及び比較例によって、本発明を更に説明す
るが、本発明はこれに限定されるものではない。(Examples) Hereinafter, the present invention will be further described with reference to Examples and Comparative Examples, but the present invention is not limited thereto.
評価方法は、以下によった。The evaluation method was as follows.
試料:固有粘度0.95近辺のポリエチレンテレフタレート
を溶融し直接紡糸延伸法によって製造する際、別記処理
剤を非含水型油剤の形で、ノズル給油法を用い付着量0.
5重量%の糸条(1500De/250fil)をえた。Sample: When polyethylene terephthalate having an intrinsic viscosity of about 0.95 is melted and produced by the direct spin-drawing method, the separately-described treatment agent is in the form of a non-hydrous type oil agent, and the deposition amount is 0.
5% by weight yarn (1500De / 250fil) was obtained.
これを、タイヤコード用リング撚糸機を用い、撚数40×
40T/10cmの2本撚りコード(生コード)を作成した。Using a ring twisting machine for tire cords, twist 40x
40T / 10cm double twisted cord (raw cord) was created.
ついで、この生コードをシングルコードディッピングマ
シーンを用い、RFL液で浸漬処理し、130℃で2分間の乾
燥後、240℃で1分間の熱処理をおこなって処理コード
を得た。Then, this raw cord was immersed in an RFL solution using a single cord dipping machine, dried at 130 ° C. for 2 minutes, and then heat treated at 240 ° C. for 1 minute to obtain a treated cord.
ここで、RFL液としては表1に示す組成のPEXUL系接着剤
を、常法にしたがって熟成したものを用いた。Here, as the RFL solution, a PEXUL adhesive having the composition shown in Table 1 was aged according to a conventional method.
RFL液の付着量は、2.5重量%とした。 The amount of the RFL liquid deposited was 2.5% by weight.
各特性については、下記方法に従って測定した。Each property was measured according to the following methods.
延伸性:5000m/分でまきとった10kgのボビン表面(0.45m
2)の長さ1mm以上の毛羽の数をもって延伸性とした。Stretchability: 10kg bobbin surface (0.45m) spun at 5000m / min
Stretchability was defined as the number of fluffs with a length of 1 mm or more in 2 ).
発煙性:縦長(幅5cm,長さ50cm)の熱板ヒーター上に、
ほぼ接するよう糸条に250gの荷重をかけてたらし、カバ
ーをする。そして、ヒーター下部とカバーの間に設けた
スリット(幅5cm,奥行き1cm)を通して上がってくる空
気中の煙の量をヒーター上部に設けた小孔(径5mm)を
通して10l/分の速度で排気し、デジタル粉塵計(柴田化
学器械工業社製タイプP−3)で測定し、3分間の累積
値を煙濃度(回/分)とした。ヒーター温度は230℃と
した。Smoke emission: on a vertically long (5 cm wide, 50 cm long) hot plate heater,
Apply a load of 250g to the threads so that they are almost in contact, and cover. Then, the amount of smoke in the air rising through the slit (width 5 cm, depth 1 cm) provided between the heater lower part and the cover is exhausted at a rate of 10 l / min through the small hole (diameter 5 mm) provided on the heater upper part. It was measured with a digital dust meter (Type P-3 manufactured by Shibata Chemical Instruments Co., Ltd.) and the cumulative value for 3 minutes was defined as the smoke density (times / minute). The heater temperature was 230 ° C.
コード強力:インテスコ社製引張試験機で試験長25cmで
処理コードの強力を求め処理コード強力とした。Code strength: A tensile tester manufactured by Intesco was used to measure the strength of the treated cord with a test length of 25 cm, and the cord was treated as the treated cord.
再乳化性:RFL液と処理剤(各20%水溶液)を6:1の割合
いに混ぜ20cm×20cm角のガラス板上に、固形分の厚さが
0.4mmとなる量入れ、常温のドラフト中で風乾させなが
ら、表層の乾燥状態を肉眼で2日間観察した。Re-emulsification: Mix RFL solution and treatment agent (20% aqueous solution each) in a ratio of 6: 1, and put the solid content on a 20 cm x 20 cm square glass plate.
An amount of 0.4 mm was put in, air-dried in a draft at room temperature, and the dry state of the surface layer was visually observed for 2 days.
○…全体に均一な皮膜を形成 △…部分的に硬い皮膜を形成(全表面積の20%以内) ×…部分的に硬い皮膜を形成(全表面積の20%以上) RFL浸透性:200gの張力をかけた30cmのヤーンを垂直に
し、下端を20%水溶液のRFL液に浸漬し、5分後に液面
より上昇したRFL液の高さとした。20℃RH65%の雰囲気
下で行った。○: Uniform film is formed on the whole △: Partially hard film is formed (within 20% of the total surface area) ×… Partially hard film is formed (20% or more of the total surface area) RFL permeability: Tension of 200 g The 30 cm yarn to which the coating was applied was made vertical, and the lower end was immersed in the RFL liquid of a 20% aqueous solution, and after 5 minutes, the height of the RFL liquid rose from the liquid surface. It was conducted in an atmosphere of 20 ° C and RH65%.
実施例1〜8及び、比較例1〜8 フィラメント強度が9.0g/dとなるよう紡糸延伸条件を設
定し、また処理剤としは表2に示すものを使用した。そ
の結果を表3に示す。Examples 1 to 8 and Comparative Examples 1 to 8 The spinning and drawing conditions were set so that the filament strength was 9.0 g / d, and the treating agents shown in Table 2 were used. The results are shown in Table 3.
表3の結果から明らかなように、本発明(実施例1〜
8)によれば、処理コードの強力が高く、発煙性も少な
い高強力ポリエステル繊維を得ることができる。 As is clear from the results of Table 3, the present invention (Examples 1 to 1
According to 8), it is possible to obtain a high-strength polyester fiber having a high treated cord strength and a low smoke generation property.
しかし、A成分の分子量が600未満、A成分の割合が62
重量%未満、B成分の分子量が7000未満、B成分の割合
が8重量%未満、A+Bが90重量%を越える場合、C成
分の分子量が800未満、またはC成分の割合が20重量%
を越えるときは、延伸性,発煙性,コード強力,再乳化
性,RFL浸透性の何れかが満足されず不充分である。However, the molecular weight of A component is less than 600, and the ratio of A component is 62.
If less than wt%, the molecular weight of component B is less than 7,000, the proportion of component B is less than 8% by weight, and A + B exceeds 90% by weight, the molecular weight of component C is less than 800, or the proportion of component C is 20% by weight.
When it exceeds, the stretchability, smoke generation property, cord strength, re-emulsification property and RFL penetration property are not satisfied and are insufficient.
実施例9,10及び、比較例9〜12 フィラメント強度が8.0g/d〜9.5g/dとなるよう紡糸延伸
条件を変更し、処理剤としては実施例1もしくは比較例
1で用いたものを使用した。結果を表4に示す。なお、
実施例1と比較例1の結果もあわせて示す。 Examples 9 and 10 and Comparative Examples 9 to 12 The spinning and drawing conditions were changed so that the filament strength was 8.0 g / d to 9.5 g / d, and the treating agent used in Example 1 or Comparative Example 1 was used. used. The results are shown in Table 4. In addition,
The results of Example 1 and Comparative Example 1 are also shown.
この結果から明らかなように、本発明(実施例1,9,10)
によれば、処理コードの強力が高く、発煙性も少なく、
RFL浸透性の低い高強力ポリエステル繊維を得ることが
できる。As is clear from this result, the present invention (Examples 1, 9 and 10)
According to, the treatment code has high strength, less smoke emission,
High-strength polyester fibers with low RFL permeability can be obtained.
しかし、他の条件は満たしているが、A成分の分子量が
小さく本発明の条件を満たさない比較例1,10〜12は、フ
ィラメント強度が増加しても、処理コードの強力がほと
んど増加せず、満足な結果は得られない。また、処理剤
が本発明の条件を満たしていても、フィラメント強度が
低い場合は、処理コードの強力が低いため好ましくな
い。However, although the other conditions are satisfied, the molecular weight of the component A is small and Comparative Examples 1, 10 to 12 which do not satisfy the conditions of the present invention show that the strength of the treated cord hardly increases even if the filament strength increases. , I do not get a satisfactory result. Even if the treating agent satisfies the conditions of the present invention, if the filament strength is low, the strength of the treated cord is low, which is not preferable.
フロントページの続き (56)参考文献 特開 昭60−9919(JP,A) 特開 昭58−98419(JP,A) 特開 昭63−59483(JP,A)Continuation of front page (56) Reference JP-A-60-9919 (JP, A) JP-A-58-98419 (JP, A) JP-A-63-59483 (JP, A)
Claims (1)
テル化合物を主成分とする平滑剤(A成分)を62重量%
以上、 (b) 分子量が7000以上でかつ15℃で液状のエーテル
系高分子活性剤(B成分)を8重量%以上、 (c) 分子量が800以上、2700以下の非イオン活性剤
(C成分)を20重量%以下含有し、かつA+Bが90重量
%以下である処理剤が付与されたポリエステル繊維であ
って、該ポリエステル繊維は下記(i)−(iii)を同
時に満足することを特徴とする高強力ポリエステル繊
維。 (i) フィラメント強度≧8.5g/d (ii) 発煙性≦1500 (iii) RFL浸透性≦5cm(A) 62% by weight of a leveling agent (component A) containing a sulfur-containing ester compound having a molecular weight of 600 or more as a main component.
As described above, (b) 8% by weight or more of an ether type polymer activator (component B) having a molecular weight of 7,000 or more and 15 ° C., (c) a nonionic activator (component C) having a molecular weight of 800 or more and 2700 or less 20% by weight or less and A + B is 90% by weight or less, and a polyester fiber to which a treating agent is added, wherein the polyester fiber simultaneously satisfies the following (i)-(iii): High-strength polyester fiber that does. (I) Filament strength ≧ 8.5g / d (ii) Smoke emission ≦ 1500 (iii) RFL permeability ≦ 5cm
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63285898A JPH0742616B2 (en) | 1988-11-14 | 1988-11-14 | High strength polyester fiber |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63285898A JPH0742616B2 (en) | 1988-11-14 | 1988-11-14 | High strength polyester fiber |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02145869A JPH02145869A (en) | 1990-06-05 |
JPH0742616B2 true JPH0742616B2 (en) | 1995-05-10 |
Family
ID=17697450
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63285898A Expired - Lifetime JPH0742616B2 (en) | 1988-11-14 | 1988-11-14 | High strength polyester fiber |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0742616B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090092561A1 (en) * | 2007-10-09 | 2009-04-09 | Lupia Joseph A | Body-care and household products and compositions comprising specific sulfur-containing compounds |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5898419A (en) * | 1981-12-02 | 1983-06-11 | Touyoubou Pet Koode Kk | Polyester fiber of high strength with high thermal dimensional stability as well as chemical stability |
JPS609919A (en) * | 1983-06-29 | 1985-01-19 | Toray Ind Inc | Preparation of thermoplastic synthetic yarn |
JPS6359483A (en) * | 1987-01-23 | 1988-03-15 | 帝人株式会社 | Raw yarn for high speed stretching friction false twisting processing and method for false twisting of said raw yarn |
-
1988
- 1988-11-14 JP JP63285898A patent/JPH0742616B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH02145869A (en) | 1990-06-05 |
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