TWI555889B - Polyester fiber for rubber reinforcing and its manufacturing method - Google Patents

Polyester fiber for rubber reinforcing and its manufacturing method Download PDF

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TWI555889B
TWI555889B TW101111061A TW101111061A TWI555889B TW I555889 B TWI555889 B TW I555889B TW 101111061 A TW101111061 A TW 101111061A TW 101111061 A TW101111061 A TW 101111061A TW I555889 B TWI555889 B TW I555889B
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fiber
polyester
rubber
polyester fiber
epoxy
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TW101111061A
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TW201307628A (en
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Daisuke Ozaki
Shintaro Shimada
Fuyuki Terasaka
Satoshi Nagase
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Teijin Fibers Ltd
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Priority claimed from JP2011078798A external-priority patent/JP5542084B2/en
Priority claimed from JP2011078799A external-priority patent/JP5542085B2/en
Priority claimed from JP2011081894A external-priority patent/JP2012214659A/en
Priority claimed from JP2011081892A external-priority patent/JP2012214933A/en
Priority claimed from JP2011081895A external-priority patent/JP2012214934A/en
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    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M15/00Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
    • D06M15/19Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment with synthetic macromolecular compounds
    • D06M15/37Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M15/55Epoxy resins
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F11/00Chemical after-treatment of artificial filaments or the like during manufacture
    • D01F11/04Chemical after-treatment of artificial filaments or the like during manufacture of synthetic polymers
    • D01F11/08Chemical after-treatment of artificial filaments or the like during manufacture of synthetic polymers of macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/62Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M13/00Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment
    • D06M13/10Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment with compounds containing oxygen
    • D06M13/11Compounds containing epoxy groups or precursors thereof
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M13/00Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment
    • D06M13/322Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment with compounds containing nitrogen
    • D06M13/325Amines
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2101/00Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
    • D06M2101/16Synthetic fibres, other than mineral fibres
    • D06M2101/30Synthetic polymers consisting of macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M2101/32Polyesters

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
  • Artificial Filaments (AREA)

Description

橡膠補強用聚酯纖維及其製造方法 Rubber fiber for reinforcing rubber and manufacturing method thereof

本發明關於一種橡膠補強用纖維,進一步詳細而言關於一種橡膠補強用聚酯纖維,其在高溫動態疲勞後的接著性優異;及其製造方法。 The present invention relates to a rubber reinforcing fiber, and more particularly to a rubber reinforcing polyester fiber which is excellent in adhesion after high-temperature dynamic fatigue and a method for producing the same.

聚對苯二甲酸乙二酯及其衍生物所代表的聚酯纖維,係具有優異的機械力學特性、物理、化學的特性,而在工業上被大量生產,其用途以產業資材為首而多樣化,而為有用的纖維。特別是高強度且尺寸安定性優異的聚酯纖維為非常適合作為輪胎、輸送帶、軟管等的橡膠材料的補強材的材料,而最近愈來愈需要具有高度的性能。例如關於V型輸送帶等的輸送帶用繩,為了達到免養護,在作為高模數化甚至大型的高負荷包覆型輸送帶用繩時必須具有更高的耐疲勞性。另一方面,使用於輪胎簾布用途時,為了提升輪胎成形時的產率,以及低收縮化或者為了提升搭乘的舒適性的高模數化、另外在大型輪胎的運用上,會需要提升耐疲勞性等。 Polyester fibers represented by polyethylene terephthalate and its derivatives have excellent mechanical properties, physical and chemical properties, and are industrially produced in large quantities. Their uses are diversified by industrial materials. And is a useful fiber. In particular, a polyester fiber having high strength and excellent dimensional stability is a material which is very suitable as a reinforcing material for a rubber material such as a tire, a conveyor belt, a hose, etc., and more and more recently, it is required to have high performance. For example, in the case of a conveyor belt rope such as a V-belt, it is necessary to have higher fatigue resistance when it is used as a high modulus or even a large high-load coated conveyor belt rope. On the other hand, when used in tire cord applications, in order to improve the productivity of the tire during molding, and to reduce the shrinkage or to improve the comfort of riding comfort, and in the use of large tires, it is necessary to improve fatigue resistance. Sex and so on.

但是,若與其他泛用橡膠補強用纖維的嫘縈等相比,則聚酯纖維雖然具有高強度,但是也有模數低、收縮率大這些性質。於是,為了使聚酯纖維高模數化、低收縮率化,採用了由高配向的未延伸絲作為起始而使其延伸的方法(專利文獻1或專利文獻2等)。進一步為了提升紡絲性, 針對紡絲油劑等的改良現在還在持續進行(專利文獻3等)。 However, the polyester fiber has high strength, but has a low modulus and a large shrinkage ratio, as compared with the other fibers of the general-purpose rubber reinforcing fiber. Then, in order to increase the modulus of the polyester fiber and to reduce the shrinkage rate, a method of extending the unoriented yarn with a high orientation as a starting point (Patent Document 1 or Patent Document 2) is employed. Further to improve the spinnability, Improvements in the spinning oil agent and the like are now continuing (Patent Document 3, etc.).

另外,聚酯纖維是由極性低的分子構造所構成,因此與橡膠的接著性基本上會有問題。因此,聚酯纖維與橡膠的黏著劑廣泛採用間苯二酚-福馬林-乳膠(RFL)系黏著劑,其進一步改良也正在檢討當中。通常廣泛採用在以RFL系黏著劑進行處理之前,以接著性提升劑對纖維作前處理的二浴型處理方法。其他方面,關於對此二浴型處理方法在聚酯纖維側作改良之方法,已知有預先在紡絲步驟添加接著性提升劑的前處理聚酯纖維。(例如專利文獻4或專利文獻5) Further, since the polyester fiber is composed of a molecular structure having a low polarity, there is basically a problem in adhesion to rubber. Therefore, resorcinol-fomalin-latex (RFL)-based adhesives are widely used as adhesives for polyester fibers and rubber, and further improvements are under review. A two-bath treatment method in which fibers are pretreated with an adhesion promoter prior to treatment with an RFL-based adhesive is generally widely used. In other respects, as for the method for improving the two-bath type treatment method on the side of the polyester fiber, a pretreated polyester fiber in which an adhesion promoter is added in advance in the spinning step is known. (for example, Patent Document 4 or Patent Document 5)

但是,即使藉由任一方法,這些由以往的方法所得到的聚酯纖維,特別是在輸送帶等所要求的橡膠中之高溫動態疲勞後的接著性方面,現在還是有性能不足的問題。 However, even with any of these methods, the polyester fiber obtained by the conventional method has a problem of insufficient performance in terms of adhesion after high-temperature dynamic fatigue in a rubber required for a conveyor belt or the like.

專利文獻1:日本特開昭53-58032號公報 Patent Document 1: Japanese Laid-Open Patent Publication No. 53-58032

專利文獻2:日本特開昭57-154410號公報 Patent Document 2: Japanese Laid-Open Patent Publication No. SHO 57-154410

專利文獻3:日本特開平7-70819號公報 Patent Document 3: Japanese Laid-Open Patent Publication No. 7-70819

專利文獻4:日本特開昭52-96234號公報 Patent Document 4: Japanese Patent Laid-Open No. 52-96234

專利文獻5:日本特開2000-355875號公報 Patent Document 5: Japanese Laid-Open Patent Publication No. 2000-355875

在本發明在於提供一種橡膠補強用聚酯纖維,其係在與橡膠的接著時,高溫動態疲勞後之接著性極優異;及其 製造方法。 The present invention provides a rubber reinforcing polyester fiber which is excellent in adhesion to high-temperature dynamic fatigue when it is bonded to rubber; Production method.

本發明之橡膠補強用聚酯纖維,其係由以對苯二甲酸乙二酯為主要重覆單元,固有黏度為0.85以上的聚酯所構成之纖維,其特徵為:纖維中的末端羧基量為20當量/ton以上,藉由X射線小角繞射測得的長週期為9~12nm且在纖維表面附著有具有環氧基的表面處理劑。 The polyester fiber for rubber reinforcement according to the present invention is a fiber composed of polyester having ethylene terephthalate as a main repeating unit and having an intrinsic viscosity of 0.85 or more, and is characterized by a terminal carboxyl group amount in the fiber. The surface treatment agent having an epoxy group is attached to the surface of the fiber with a long period of 9 to 12 nm as measured by X-ray small angle diffraction of 20 eq/ton or more.

進一步而言,纖維表面的末端羧基量為10當量/ton以下、或纖維橫軸方向的結晶粒徑為35~80nm2、纖維中的末端甲基量為2當量/ton以下、纖維中的氧化鈦含量為0.05~3重量%、纖維表面的環氧指數為1.0×10-3當量/kg以下為佳。 Further, the amount of terminal carboxyl groups on the surface of the fiber is 10 equivalent/ton or less, or the crystal grain size in the transverse direction of the fiber is 35 to 80 nm 2 , and the amount of terminal methyl groups in the fiber is 2 equivalent/ton or less, and oxidation in the fiber The titanium content is 0.05 to 3% by weight, and the epoxy index of the fiber surface is preferably 1.0 × 10 -3 equivalent / kg or less.

另一個本發明之聚酯纖維之製造方法,其特徵為:將固有黏度為0.9以上且末端羧基量為15當量/ton以上的聚對苯二甲酸乙二酯聚合物熔融擠出,添加含有鹼性硬化觸媒的紡絲油劑之後,以2000~6000m/分鐘之速度抽取,接下來進行延伸,然後添加含有環氧化合物的整理油劑,而進行熟成處理。 Another method for producing a polyester fiber according to the present invention is characterized in that a polyethylene terephthalate polymer having an intrinsic viscosity of 0.9 or more and a terminal carboxyl group content of 15 equivalents/ton or more is melt-extruded, and an alkali is added. After the spinning oil of the hardening catalyst, it is extracted at a speed of 2000 to 6000 m/min, and then extended, and then a finishing oil containing an epoxy compound is added to perform a ripening treatment.

進一步係以熟成處理溫度在20~50℃的範圍、或熟成處理時間為50小時以上為佳,環氧硬化觸媒係以胺化合物為佳。 Further, it is preferred that the ripening treatment temperature is in the range of 20 to 50 ° C or the ripening treatment time is 50 hours or more, and the epoxy curing catalyst is preferably an amine compound.

依據本發明可提供一種橡膠補強用聚酯纖維,其在與橡膠的接著時,高溫動態疲勞後的接著性極優異;及其製造方法。 According to the present invention, it is possible to provide a polyester fiber for rubber reinforcement which is excellent in adhesion after high-temperature dynamic fatigue in the case of adhesion to rubber, and a method for producing the same.

本發明之橡膠補強用聚酯纖維係由對苯二甲酸乙二酯為主要重覆單元的聚酯所構成之纖維。此聚酯之主要重覆單元的含量係以相對於構成聚酯的全部二羧酸成分而言,此重覆單元為含有80莫耳%以上為佳。特別以含有90莫耳%以上的聚酯為佳。另外,如果在聚酯聚合物中含量少,則亦可為含有適當的第3成分的共聚物。 The polyester fiber for rubber reinforcement of the present invention is a fiber composed of polyester having ethylene terephthalate as a main repeating unit. The content of the main repeating unit of the polyester is preferably 80 mol% or more based on the total dicarboxylic acid component constituting the polyester. It is particularly preferable to contain a polyester of 90 mol% or more. Further, when the content in the polyester polymer is small, a copolymer containing an appropriate third component may be used.

另外,此聚酯纖維之固有黏度必須在0.85以上,在1.10以下為佳。進一步以在0.89~1.05的範圍,特別是在0.90~1.00的範圍為佳。若固有黏度未滿0.85,則聚酯纖維之強度不足,特別是在橡膠加硫步驟無法充分抑制強度降低。 Further, the inherent viscosity of the polyester fiber must be 0.85 or more, preferably 1.10 or less. Further, it is preferably in the range of 0.89 to 1.05, particularly in the range of 0.90 to 1.00. If the intrinsic viscosity is less than 0.85, the strength of the polyester fiber is insufficient, and in particular, the rubber vulcanization step cannot sufficiently suppress the strength reduction.

進一步而言,本發明之橡膠補強用聚酯纖維藉由X射線小角繞射測得的長週期必須為9~12nm。此處所謂的藉由X射線小角繞射測得的長週期,是指在纖維縱軸方向(將纖維紡絲的方向)聚酯聚合物中的結晶與結晶的間隔。本發明之橡膠補強用聚酯纖維,在此長週期會表現出短的結晶間的間隔。就其結果而言,結晶與結晶直接結合的緊伸分子(tie molecule)的數目變多,作為橡膠補強用纖維使用的情況,可使橡膠中的纖維的強度維持率保持在高值 。因此,如後述般,即使是在纖維聚合物中的末端羧基量比以往還多的情況,藉由環氧處理等的表面處理,可得到充分的耐久性。另外,藉由將纖維的長週期定在這樣的範圍,可使纖維的物性成為高模數,低收縮率這種適合於橡膠補強用纖維的物性。 Further, the long period of the rubber reinforcing polyester fiber of the present invention measured by X-ray small angle diffraction must be 9 to 12 nm. Here, the long period measured by the X-ray small angle diffraction means the interval between the crystal and the crystal in the polyester polymer in the longitudinal direction of the fiber (the direction in which the fiber is spun). The polyester fiber for rubber reinforcement of the present invention exhibits a short interval between crystals in this long period. As a result, the number of tie molecules directly bonded to crystals increases, and as a rubber reinforcing fiber, the strength maintenance rate of the fibers in the rubber can be maintained at a high value. . Therefore, as described later, even when the amount of terminal carboxyl groups in the fiber polymer is larger than in the related art, sufficient durability can be obtained by surface treatment such as epoxy treatment. In addition, by setting the long period of the fiber to such a range, the physical properties of the fiber can be made into a high modulus, and a low shrinkage ratio is suitable for the physical properties of the fiber for rubber reinforcement.

為了將長週期像這樣設定在12nm以下,可藉由高速紡絲來達成,在低速紡絲的情況,此長週期值會變大。另外,進行高速紡絲也會有限度,長週期會以9nm的範圍為下限。進一步而言,藉由X射線小角繞射測得的長週期係以10nm~11nm的範圍為佳。 In order to set the long period as described above to 12 nm or less, it can be achieved by high speed spinning, and in the case of low speed spinning, the long period value becomes large. In addition, high-speed spinning is limited, and the long period is limited to a range of 9 nm. Further, the long period system measured by X-ray small angle diffraction is preferably in the range of 10 nm to 11 nm.

另外,本發明之橡膠補強用聚酯纖維在纖維橫軸方向(與將纖維紡絲的方向垂直的方向)的結晶粒徑係以在35~80nm2的範圍為佳。本發明之聚酯纖維,其纖維縱軸的結晶間隔的長週期低達12nm以下,而為了製成高強度纖維,一定的結晶大小也是必要的,在本發明中,纖維橫軸方向的結晶粒徑係以成長至35nm2以上為佳。但是如果結晶粒徑過大,則纖維會變得剛直,耐疲勞性降低,因此以80nm2以下為佳。進一步而言,纖維橫軸方向的結晶粒徑係以在40~70nm2的範圍為佳。像這樣,藉由結晶往纖維橫軸方向成長,緊伸分子在纖維橫軸方向亦容易發展,因此在纖維的縱橫方向構築出三維的構造,而成為如本發明般的橡膠補強用方面特別合適的纖維。另外,藉由這種三維構造,纖維的損失係數Tan δ變低。就結果而言,可抑制反覆施加應力下的發熱量,可將反覆施加應力後的接著 性能保持得很高,而成為在橡膠補強用途方面特別合適的纖維。 Further, the polyester fiber for rubber reinforcement of the present invention preferably has a crystal grain size in the range of 35 to 80 nm 2 in the transverse direction of the fiber (direction perpendicular to the direction in which the fiber is spun). In the polyester fiber of the present invention, the long period of the crystal spacing of the longitudinal axis of the fiber is as low as 12 nm or less, and in order to form a high-strength fiber, a certain crystal size is also necessary. In the present invention, the crystal grain in the transverse direction of the fiber is required. The diameter system is preferably grown to 35 nm 2 or more. However, if the crystal grain size is too large, the fibers become rigid and the fatigue resistance is lowered, so that it is preferably 80 nm 2 or less. Further, the crystal grain size in the transverse direction of the fiber is preferably in the range of 40 to 70 nm 2 . In this way, since the crystal grows in the direction of the transverse axis of the fiber, the stretched molecules are easily developed in the direction of the transverse axis of the fiber. Therefore, a three-dimensional structure is formed in the longitudinal and lateral directions of the fiber, and it is particularly suitable for the rubber reinforcing aspect as in the present invention. Fiber. Further, with this three-dimensional structure, the fiber loss coefficient Tan δ becomes low. As a result, the amount of heat generated under the repeated application of stress can be suppressed, and the subsequent performance after repeated stress application can be kept high, and it is particularly suitable for use in rubber reinforcement applications.

再者,本發明之橡膠補強用聚酯纖維,其聚合物全體的羧基量必須為20當量/ton以上,且其纖維表面必須附著有具有環氧基的表面處理劑。以往,特別是在高溫或高振動等的高負荷環境下所使用的橡膠補強用聚酯纖維,為了使其耐熱劣化性提升,將聚合物的羧基量保持在15當量/ton以下,更理想的情況保持在10當量/ton以下為一般常見的手段。但是,對於橡膠補強用聚酯纖維而言,除了維持纖維的強度以外,與橡膠接著性維持的必要性也很高,如本發明之聚酯纖維般,藉由X射線小角繞射測得的長週期低達9~12nm,且在對表面實施環氧處理的情況羧基量為20當量/ton以上,作為橡膠補強用尤其適合,本發明人等發現了這些現象。進一步而言,聚合物中的羧基量宜為末端羧基量的上限在40當量/ton以下,甚至在30當量/ton以下,尤其以在21~25當量/ton的範圍為佳。 Further, in the polyester fiber for rubber reinforcement of the present invention, the amount of the carboxyl group of the entire polymer must be 20 equivalents/ton or more, and a surface treatment agent having an epoxy group must be adhered to the surface of the fiber. More preferably, in order to improve the heat deterioration resistance, the polyester fiber for rubber reinforcement used in a high-load environment such as high temperature or high vibration is preferably kept at a level of 15 equivalents/ton or less. Maintaining a condition below 10 eq/ton is a common and common approach. However, in the case of the polyester reinforcing polyester fiber, in addition to maintaining the strength of the fiber, the necessity of maintaining the adhesiveness with the rubber is also high, as measured by the X-ray small angle diffraction of the polyester fiber of the present invention. The inventors of the present invention found these phenomena as long as the long period is as low as 9 to 12 nm and the amount of the carboxyl group is 20 equivalent/ton or more in the case of performing epoxy treatment on the surface. Further, the amount of the carboxyl group in the polymer is preferably such that the upper limit of the amount of terminal carboxyl groups is 40 equivalents/ton or less, even 30 equivalents/ton or less, particularly preferably in the range of 21 to 25 equivalents/ton.

在本發明之橡膠補強用聚酯纖維的表面附著有具有環氧基的表面處理劑。此處表面處理劑係以含有一分子中具有2個以上環氧基的環氧化合物之一種或兩種以上的混合物的環氧化合物為佳。較具體而言,係以含鹵素的環氧類為佳,可列舉例如藉由表氯醇多元醇或多價酚的合成所得到的物質,以甘油聚縮水甘油醚或聚甘油聚縮水甘油醚、間苯二酚二縮水甘油醚、山梨醇聚縮水甘油醚、乙二醇二 縮水甘油醚等的化合物為佳。這種含有環氧化合物的表面處理劑在纖維表面的附著量係以0.05~1.5重量%為佳,宜為0.10~1.0重量%。在表面處理劑中亦可因應必要混合平滑劑、乳化劑、抗靜電劑或其他添加劑等。 A surface treatment agent having an epoxy group is attached to the surface of the polyester fiber for rubber reinforcement of the present invention. Here, the surface treatment agent is preferably an epoxy compound containing one or a mixture of two or more kinds of epoxy compounds having two or more epoxy groups in one molecule. More specifically, it is preferably a halogen-containing epoxy group, and examples thereof include those obtained by synthesis of epichlorohydrin polyol or polyvalent phenol, glycerol polyglycidyl ether or polyglycerol polyglycidyl ether. , resorcinol diglycidyl ether, sorbitol polyglycidyl ether, ethylene glycol II A compound such as glycidyl ether is preferred. The amount of the surface treatment agent containing the epoxy compound adhered to the surface of the fiber is preferably from 0.05 to 1.5% by weight, preferably from 0.10 to 1.0% by weight. A smoothing agent, an emulsifier, an antistatic agent, or other additives may be mixed in the surface treatment agent as necessary.

這種附著有本發明之具有環氧基的表面處理劑的橡膠補強用聚酯纖維,其纖維表面的環氧指數係以1.0×10-3當量/kg以下為佳。進一步而言,表面處理聚酯纖維每1kg的環氧指數係以0.01×10-3~0.5×10-3當量/kg為佳。在纖維表面的環氧指數高的情況,會有未反應的環氧化合物多的傾向,例如在撚絲步驟帶有黏性的浮垢會在導紗鉤類等大量產生、纖維的步驟通過性降低,同時會有導致撚絲不均等的製品品質降低的問題。 This attachment of the present invention has an epoxy group having a rubber reinforcing agent, a surface treatment of polyester fibers with an epoxy-based index to the fiber surface 1.0 × 10 -3 eq / kg or less is preferable. Further, the epoxy index of the surface-treated polyester fiber per 1 kg is preferably 0.01 × 10 -3 to 0.5 × 10 -3 equivalent / kg. In the case where the epoxy index of the fiber surface is high, there is a tendency for a large amount of unreacted epoxy compound. For example, viscous scum in the filting step may be generated in a large amount in the yarn hook, and the step of the fiber is passed. When it is lowered, there is a problem that the quality of the product which causes unevenness of the crepe is lowered.

本發明之橡膠補強用聚酯纖維像這樣的方式附著有具有環氧基的表面處理劑,而進一步而言宜為環氧硬化觸媒附著於此纖維表面。此處環氧硬化觸媒係使本發明之必須成分的環氧化合物硬化之硬化劑。合適的環氧硬化觸媒具體而言可列舉胺化合物,其中脂肪族胺化合物為佳。更佳為在碳數4~22之脂肪族胺加成2~20莫耳的環氧乙烷及/或環氧丙烷而成的胺化合物。 The polyester fiber for rubber reinforcement of the present invention has a surface treatment agent having an epoxy group as described above, and further preferably an epoxy curing catalyst adheres to the surface of the fiber. Here, the epoxy curing catalyst is a hardening agent which hardens an epoxy compound which is an essential component of the present invention. A suitable epoxy hardening catalyst is specifically an amine compound, and an aliphatic amine compound is preferred. More preferably, it is an amine compound obtained by adding 2 to 20 moles of ethylene oxide and/or propylene oxide to an aliphatic amine having 4 to 22 carbon atoms.

而這種本發明之橡膠補強用聚酯纖維的表面(原絲表面)的末端羧基量係以10當量/ton以下為佳。在本發明之橡膠補強用聚酯纖維中聚合物全體的羧基量如前述般為20當量/ton以上,而藉由與附著於纖維表面的環氧化合物的反應,纖維表面的羧基量係以較低於此值的10當量 /ton以下為佳。像這樣,聚合物中的羧基在纖維表面藉由與環氧基進行反應,本發明之橡膠補強用聚酯纖維可具有極優異的接著性能。此時,纖維表面的末端羧基量殘存過多的情況,會有耐熱性或接著性降低的傾向。 On the other hand, the surface of the rubber reinforcing polyester fiber of the present invention (the surface of the raw yarn) preferably has a terminal carboxyl group content of 10 equivalents/ton or less. In the polyester fiber for rubber reinforcement of the present invention, the amount of the carboxyl group of the entire polymer is 20 equivalents/ton or more as described above, and the amount of the carboxyl group on the surface of the fiber is determined by the reaction with the epoxy compound attached to the surface of the fiber. 10 equivalents below this value /ton below is better. As described above, the carboxyl group in the polymer reacts with the epoxy group on the surface of the fiber, and the polyester fiber for rubber reinforcement of the present invention can have extremely excellent adhesion properties. In this case, when the amount of terminal carboxyl groups on the surface of the fiber remains excessive, heat resistance or adhesion tends to decrease.

另外,本發明之橡膠補強用聚酯纖維,其纖維中的末端甲基量係以2當量/ton以下為佳。進一步以不含有末端甲基為佳。這是因為聚酯聚合物中的甲基的反應性低,不會與環氧基反應的緣故。這種聚酯聚合物中的末端甲基由原料中的對苯二甲酸二甲酯所產生的情形很多。因此,本發明之橡膠補強用聚酯纖維係以由不使用對苯二甲酸二甲酯的直接聚合法(直接酯化法)所產生的聚酯聚合物所構成為佳。在構成纖維的聚合物中沒有末端甲基或含少量的情況,可確保與表面處理劑中的環氧基的高反應性,並可確保高接著性或表面保護性能。 Further, in the polyester fiber for rubber reinforcement of the present invention, the amount of terminal methyl groups in the fibers is preferably 2 equivalents/ton or less. It is further preferred that the terminal methyl group is not contained. This is because the methyl group in the polyester polymer has low reactivity and does not react with the epoxy group. The terminal methyl group in this polyester polymer is produced from the dimethyl terephthalate in the raw material. Therefore, the polyester fiber for rubber reinforcement of the present invention is preferably composed of a polyester polymer produced by a direct polymerization method (direct esterification method) in which dimethyl terephthalate is not used. In the case where there is no terminal methyl group or a small amount in the polymer constituting the fiber, high reactivity with the epoxy group in the surface treatment agent can be ensured, and high adhesion or surface protection property can be ensured.

在本發明之橡膠補強用聚酯纖維之中,纖維中之氧化鈦含量係以0.05~3重量%的範圍為佳。通常在高強度聚酯纖維之中含有氧化鈦之會導致異物造成製絲性的降低,因此大多要避免這種情形。但是,為了防止生產步驟中的摩擦造成強度的降低或橡膠中的聚酯纖維的耐疲勞性的降低,維持最終製品的強度的觀點看來,在聚酯纖維中含有少量這種氧化鈦亦為合適。若氧化鈦含量少於0.05重量%,則為了使在延伸步驟等輥筒與纖維之間所產生的應力分散的平滑效果會有不足的傾向,對於最終所得到的纖維的高強度化而言會有不利的傾向。相反地,在含量高於3重 量%的情況,在氧化鈦會在聚合物內部成為異物而阻礙延伸性,最終所得到的纖維的強度也會有降低的傾向。 In the polyester fiber for rubber reinforcement of the present invention, the content of the titanium oxide in the fiber is preferably in the range of 0.05 to 3% by weight. Usually, the inclusion of titanium oxide in the high-strength polyester fiber causes the foreign matter to cause a decrease in the spinnability, so this situation is mostly avoided. However, in order to prevent a decrease in strength due to friction in the production step or a decrease in fatigue resistance of the polyester fiber in the rubber, and to maintain the strength of the final product, it is also considered that a small amount of such titanium oxide is contained in the polyester fiber. Suitable. When the content of the titanium oxide is less than 0.05% by weight, the smoothing effect of dispersing the stress generated between the roll and the fiber in the stretching step tends to be insufficient, and the strength of the finally obtained fiber is increased. There are disadvantages. Conversely, the content is higher than 3 In the case of amount %, the titanium oxide becomes a foreign matter in the polymer to hinder the elongation, and the strength of the finally obtained fiber tends to decrease.

這種本發明之橡膠補強用聚酯纖維的強度係以在4.0~10.0cN/dtex的範圍為佳。進一步以在5.0~9.5cN/dtex為佳。在強度過低的情況是理所當然耐久性差,在過高的情況,就結果而言橡膠的耐久性會有變差的傾向。例如若在極限的高強度進行生產,則在製絲步驟會有容易發生斷絲的傾向,會有在工業纖維的品質安定性發生問題的傾向。 The strength of the rubber reinforcing polyester fiber of the present invention is preferably in the range of 4.0 to 10.0 cN/dtex. Further, it is preferably 5.0 to 9.5 cN/dtex. In the case where the strength is too low, the durability is poor, and in the case where the strength is too high, the durability of the rubber tends to be deteriorated as a result. For example, when the production is carried out at a high strength, the yarn breaking tends to occur in the spinning step, and there is a tendency that the quality stability of the industrial fiber is problematic.

另外,纖維在180℃的乾熱收縮率係以1~15%為佳。 Further, the dry heat shrinkage ratio of the fiber at 180 ° C is preferably from 1 to 15%.

在乾熱收縮率過高的情況,加工時的尺寸變化會有變大的傾向,使用纖維的成形品的尺寸安定性容易變差。 When the dry heat shrinkage rate is too high, the dimensional change during processing tends to become large, and the dimensional stability of the molded article using the fiber tends to be deteriorated.

此外,在以短纖維的形態使用本發明的聚酯纖維的情況,切斷前的纖維的物性只要在如上述般的範圍即可,例如乾熱收縮率之值係以在1~15%的範圍為佳。 Further, when the polyester fiber of the present invention is used in the form of a short fiber, the physical properties of the fiber before the cutting may be in the range as described above, for example, the value of the dry heat shrinkage ratio is 1 to 15%. The range is good.

本發明的聚酯纖維的單絲纖度並無特別限定,而從製絲性的觀點看來,係以0.1~100dtex/單絲為佳。特別是從作為軟管、輸送帶等的橡膠補強用纖維或產業資材用纖維的強度、耐熱性或接著性的觀點看來,係以1~20dtex/單絲為佳。 The monofilament fineness of the polyester fiber of the present invention is not particularly limited, and is preferably from 0.1 to 100 dtex/monofilament from the viewpoint of the yarn-forming property. In particular, it is preferably from 1 to 20 dtex/monofilament from the viewpoint of strength, heat resistance or adhesion of the fiber for rubber reinforcement or the fiber for industrial materials such as a hose or a conveyor belt.

關於總纖度亦無特別限制,而以10~10000dtex為佳,特別是作為軟管、輸送帶等的橡膠補強用纖維或產業資材用纖維係以250~6000dtex為佳。另外,關於總纖度, 宜為例如將2根1000dtex之纖維合絲,而使總纖度成為2000dtex,可在紡絲、延伸的途中或分別在紡絲、延伸結束之後進行2~10根的合絲。 The total fineness is not particularly limited, and is preferably from 10 to 10,000 dtex, and particularly preferably as a rubber reinforcing fiber such as a hose or a conveyor belt or a fiber for industrial materials, preferably 250 to 6000 dtex. In addition, regarding the total fineness, For example, it is preferable to combine two filaments of 1000 dtex to have a total fineness of 2000 dtex, and to perform 2 to 10 filaments in the middle of spinning or stretching or after spinning and stretching.

這種本發明之橡膠補強用聚酯纖維可藉由例如另一個本發明的聚酯纖維之製造方法而得到。 The rubber reinforcing polyester fiber of the present invention can be obtained, for example, by the production method of another polyester fiber of the present invention.

本發明之聚酯纖維之製造方法,係將固有黏度為0.9以上且末端羧基量為15當量/ton以上的聚對苯二甲酸乙二酯聚合物熔融擠出,在添加含有環氧硬化觸媒的紡絲油劑之後,以2000~6000m/分鐘的速度抽取,接下來在延伸之後,添加含有環氧化合物的整理油劑,進行熟成處理之製造方法。 The method for producing a polyester fiber of the present invention comprises melt-extruding a polyethylene terephthalate polymer having an intrinsic viscosity of 0.9 or more and a terminal carboxyl group content of 15 equivalents/ton or more, and adding an epoxy hardening catalyst. After the spinning oil is applied at a rate of 2000 to 6000 m/min, a finishing oil containing an epoxy compound is added after the stretching, and a manufacturing method of the ripening treatment is performed.

在本發明中熔融擠出所使用的聚對苯二甲酸乙二酯聚合物,係聚酯的主要重覆單元為對苯二甲酸乙二酯的聚合物。此處,此聚酯的主要重覆單元的含量係以相對於構成聚酯的全部二羧酸成分而言,其重覆單元為含有80莫耳%以上為佳,特別以含有90莫耳%以上的聚酯為佳。另外,如果在聚酯聚合物中含量少,則亦可為含有適當的第3成分的共聚物。 In the polyethylene terephthalate polymer used for melt extrusion in the present invention, the main repeating unit of the polyester is a polymer of ethylene terephthalate. Here, the content of the main recoating unit of the polyester is preferably 80 mol% or more, particularly 90 mol%, based on the total dicarboxylic acid component constituting the polyester. The above polyester is preferred. Further, when the content in the polyester polymer is small, a copolymer containing an appropriate third component may be used.

另外,此聚酯聚合物的固有黏度必須為0.9以上,進一步在0.93~1.10,特別是在0.95~1.07的範圍為佳。若固有黏度未滿0.9,則熔融紡絲所得到的聚酯纖維強度降低,難以得到高強度聚酯纖維。 Further, the inherent viscosity of the polyester polymer must be 0.9 or more, and further preferably 0.93 to 1.10, particularly preferably 0.95 to 1.07. When the intrinsic viscosity is less than 0.9, the strength of the polyester fiber obtained by melt spinning is lowered, and it is difficult to obtain a high-strength polyester fiber.

此外,在本發明之聚酯纖維之製造方法中,其特徵為:聚合物的固有黏度為0.9以上,同時聚合物的末端羧基 量高達15當量/ton以上。上限係以30當量/ton以下為佳,進一步而言,在聚合物階段的末端羧基量係在16~25當量/ton的範圍,特別以在18~23當量/ton的範圍為佳。認為通常在橡膠補強用的高強度聚酯纖維之中,末端羧基量必須少。因此儘管生產性低,大多是使用末端羧基量多的聚合物。但是,在橡膠纖維複合體中的耐久性方面,纖維強度以及橡膠.纖維間的接著力為重要的,本發明人等矚目於此,以這種方式將末端羧基量調節在高範圍,以2000~6000m/分鐘的高速進行紡絲,並與其他條件組合,亦即將高速紡絲與最適合的環氧處理作組合,藉此達成得到更為適合的橡膠補強用的聚酯纖維。進一步在本發明之製造方法中,沒有必要刻意減少末端羧基量,因此在聚合物聚合時的產率或生產性亦提升,此聚合物進一步亦可降低纖維的生產成本。 Further, in the method for producing a polyester fiber of the present invention, the polymer has an intrinsic viscosity of 0.9 or more and a terminal carboxyl group of the polymer. The amount is up to 15 equivalents/ton or more. The upper limit is preferably 30 equivalents/ton or less, and further, the terminal carboxyl group amount in the polymer stage is in the range of 16 to 25 equivalents/ton, particularly preferably in the range of 18 to 23 equivalents/ton. It is considered that the amount of terminal carboxyl groups in the high-strength polyester fiber for rubber reinforcement is usually small. Therefore, in view of low productivity, a polymer having a large amount of terminal carboxyl groups is often used. However, in terms of durability in rubber fiber composites, fiber strength and rubber. The adhesion between the fibers is important, and the inventors of the present invention have focused on this, and in this way, the amount of terminal carboxyl groups is adjusted to a high range, and spinning at a high speed of 2000 to 6000 m/min is combined with other conditions, that is, High-speed spinning is combined with the most suitable epoxy treatment to achieve a more suitable polyester fiber for rubber reinforcement. Further, in the production method of the present invention, it is not necessary to intentionally reduce the amount of terminal carboxyl groups, so that the yield or productivity at the time of polymer polymerization is also improved, and the polymer can further reduce the production cost of the fiber.

另外,關於熔融紡絲的聚酯聚合物的聚合方法,現在已知有由對苯二甲酸二甲酯與乙二醇所製作的DMT法(酯交換法)與由對苯二甲酸與乙二醇所作製作的直接聚合法(直接酯化法),在本發明之製造方法之中,任一方法皆可使用。但是,在以DMT法所製作的聚對苯二甲酸乙二酯中,其末端基除了在本發明中所必須使用的羧基之外,還有由對苯二甲酸二甲酯所產生的甲基末端存在。為了不與整理油劑中的環氧基發生反應,故此甲基末端以少為佳,在本發明中,聚酯聚合物係以不存在末端甲基,以直接聚合法所製作的聚酯聚合物為佳。藉由使用直接聚合法的聚 酯聚合物,可確保在纖維表面的羧基與環氧基的反應性在較高水準。 Further, regarding the polymerization method of the melt-spun polyester polymer, a DMT method (transesterification method) made of dimethyl terephthalate and ethylene glycol and a terephthalic acid and an ethylene compound are known. A direct polymerization method (direct esterification method) for producing an alcohol, and any of the methods of the present invention can be used. However, in the polyethylene terephthalate produced by the DMT method, the terminal group has a methyl group derived from dimethyl terephthalate in addition to the carboxyl group which is necessarily used in the present invention. The end exists. In order not to react with the epoxy group in the finishing oil, the methyl terminal is preferably as small as possible. In the present invention, the polyester polymer is polymerized by a direct polymerization method in the absence of a terminal methyl group. Things are better. By using direct polymerization The ester polymer ensures a high level of reactivity of the carboxyl groups on the surface of the fiber with the epoxy group.

進一步而言,本發明所使用的聚酯聚合物係以聚合物中的氧化鈦含量係以0.05~3重量%的範圍為佳。若氧化鈦含量少於0.05重量%,則在纖維化之後的延伸步驟等之中,為了使輥筒與纖維之間所產生的應力分散的平滑效果會有不足的傾向,對於最終所得到的纖維的高強度化會有不利的傾向。相反地,在含量高於3%的情況,氧化鈦會在聚合物內部成為異物而阻礙延伸性,最終所得到的纖維的強度也會有降低的傾向。通常在高強度聚酯纖維的製造之中,由於聚合物中含有氧化鈦會導致異物造成製絲性降低,因此大多要避免這種情形。但是,為了防止生產步驟中的摩擦造成強度降低、或防止橡膠中的聚酯纖維的耐疲勞性的降低,宜為在聚酯聚合物中含有少量這種氧化鈦。 Further, the polyester polymer used in the present invention preferably has a titanium oxide content in the polymer of 0.05 to 3% by weight. When the content of the titanium oxide is less than 0.05% by weight, in the stretching step after the fiberization or the like, the smoothing effect of dispersing the stress generated between the roll and the fiber tends to be insufficient, and the fiber finally obtained is obtained. The high strength will have an unfavorable tendency. On the other hand, when the content is more than 3%, the titanium oxide becomes a foreign matter inside the polymer to hinder the elongation, and the strength of the finally obtained fiber tends to decrease. In general, in the production of high-strength polyester fibers, since titanium oxide is contained in the polymer, the foreign matter causes a decrease in the yarn-making property, and thus it is often avoided. However, in order to prevent a decrease in strength due to friction in the production step or to prevent a decrease in fatigue resistance of the polyester fiber in the rubber, it is preferred to contain a small amount of such titanium oxide in the polyester polymer.

另外,為了將聚酯聚合物的固有黏度定為0.9以上,本發明所使用的聚酯聚合物亦以固相聚合為佳。在本發明之製造方法之中,至少在聚合物階段的固有黏度在熔融紡絲前的階段需要高達0.9以上。 Further, in order to set the intrinsic viscosity of the polyester polymer to 0.9 or more, the polyester polymer used in the present invention is preferably solid phase polymerization. In the production method of the present invention, the intrinsic viscosity at least in the polymer stage needs to be as high as 0.9 or more at the stage before melt spinning.

在本發明之聚酯纖維之製造方法中,必須以2000~6000m/分鐘的高速抽取如上述般的聚酯聚合物,接下來進行延伸。像這樣以高速抽取的情況,在延伸前的階段纖維成為部分配向絲,然後與延伸組合,藉此成為高模數、低收縮率的聚酯纖維。進一步而言,藉由像這樣進行高速紡絲,亦可提升其生產性。 In the method for producing a polyester fiber of the present invention, it is necessary to extract the polyester polymer as described above at a high speed of from 2,000 to 6,000 m/min, and then carry out the stretching. In the case of high-speed extraction as described above, the fiber becomes a partial alignment yarn at the stage before the elongation, and then combined with the extension, thereby forming a polyester fiber having a high modulus and a low shrinkage ratio. Further, by performing high-speed spinning like this, the productivity can be improved.

由金屬紡嘴噴出聚酯聚合物的噴出量,從生產性的層面看來,係以在420g/分鐘~1800g/分鐘的範圍為佳,進一步以在500g/分鐘~1000g/分鐘為佳。另外,聚合物噴出時,紡絲拉伸(聚合物由金屬紡嘴噴出的線速度/抽取速度)係以500~4000的範圍為佳,進一步以1000~2500為佳。藉由採用這種高紡絲拉伸比可促進纖維之配向結晶化。 The discharge amount of the polyester polymer sprayed from the metal spun nozzle is preferably in the range of 420 g/min to 1800 g/min, and more preferably 500 g/min to 1000 g/min, from the viewpoint of productivity. Further, when the polymer is ejected, the spinning stretching (the linear velocity/extraction speed at which the polymer is ejected from the metal spun nozzle) is preferably in the range of 500 to 4,000, more preferably in the range of 1,000 to 2,500. The alignment crystallization of the fibers can be promoted by using such a high spinning draw ratio.

像這樣,在本發明之製造方法之中,必須以高速進行紡絲,而進一步以在由金屬紡嘴噴出之後,通過熔融聚合物溫度以上的加熱紡絲筒為佳。此時加熱紡絲筒的長度係以10~500mm為佳。由金屬紡嘴噴出之後,聚合物容易立刻配向、容易發生斷絲,因此宜以這種方式使用加熱紡絲筒使其遲延冷卻。通過加熱紡絲筒的紡絲條,接下來宜為吹送30℃以下的冷風使其冷卻。進一步以25℃以下的冷風為佳。 As described above, in the production method of the present invention, it is necessary to spin at a high speed, and it is more preferable to use a heated spinneret having a molten polymer temperature or higher after being ejected from a metal spun nozzle. At this time, the length of the heating spinning drum is preferably 10 to 500 mm. After being ejected from the metal spout, the polymer tends to be immediately aligned and is prone to breakage, so it is preferable to use a heated spinneret to delay cooling in this manner. By heating the spinneret of the spinning cylinder, it is preferably cooled by blowing cold air of 30 ° C or less. Further, cold air of 25 ° C or less is preferred.

此外,像這樣藉由高速紡絲所得到的聚酯纖維,其藉由X射線小角繞射測得的長週期係以12nm以下為佳。為了使長週期像這樣降低,係以使熔融紡絲速度更高速為佳,在低速紡絲中,此長週期值會變大。另外在工業上,長週期的下限係以9nm左右為佳。進一步而言,此藉由X射線小角繞射測得的長週期係以10nm~11nm的範圍為佳。 Further, the polyester fiber obtained by high-speed spinning as described above preferably has a long period of 12 nm or less as measured by X-ray small angle diffraction. In order to reduce the long period like this, it is preferable to make the melt spinning speed higher, and in the low speed spinning, the long period value becomes large. In addition, in the industry, the lower limit of the long period is preferably about 9 nm. Further, the long period system measured by X-ray small angle diffraction is preferably in the range of 10 nm to 11 nm.

此處所謂的長週期是指在纖維縱軸方向(將纖維加以紡絲的方向)聚酯聚合物中結晶與結晶的間隔。在此長週 期小的情況,表示在聚酯纖維中結晶間的間隔短。而長週期在這種範圍的情況,其結果,分子不會發生中斷,結晶與結晶直接連結的緊伸分子的數量變多,在使用作為橡膠補強用纖維的情況,可將橡膠中的纖維的強度維持率保持在高的值。因此,即使在聚合物中的末端羧基量比以往更多的條件進行紡絲的本申請案之製造方法的情況,藉由環氧處理等的表面處理,可得到充分的耐久性。另外,若在這種長週期的範圍,則使纖維的物性為高模數,低收縮率,而成為適合於橡膠補強用纖維的物性。 The term "long period" as used herein refers to the interval between crystallization and crystallization in the polyester polymer in the direction of the longitudinal axis of the fiber (the direction in which the fibers are spun). Long week here In the case of a small period, it means that the interval between crystals in the polyester fiber is short. On the other hand, in the case where the long period is in this range, the number of the molecules which are directly linked to the crystal and the crystal is not interrupted, and the fiber in the rubber can be used in the case of using the fiber for rubber reinforcement. The strength maintenance rate is maintained at a high value. Therefore, even in the case of the production method of the present application in which the amount of terminal carboxyl groups in the polymer is spun more than the conventional conditions, sufficient durability can be obtained by surface treatment such as epoxy treatment. In addition, in the range of such a long period, the physical properties of the fiber are high modulus and low shrinkage, and the physical properties of the fiber for rubber reinforcement are obtained.

另外,像這樣使進行高速紡絲所得到的纖維延伸的條件係以在紡絲後延伸1.5~5.0倍為佳。像這樣藉由高倍率的延伸,可得到較高強度的延伸纖維。 Further, the conditions for extending the fibers obtained by high-speed spinning are preferably 1.5 to 5.0 times after spinning. Such a high-strength extended fiber can be obtained by stretching at a high magnification like this.

本發明中之聚酯纖維之延伸方法可藉由從抽取輥筒抽取後暫時加以纏繞,所謂分段延伸法進行來延伸,然而宜為由抽取輥筒連續地進行延伸步驟,供給未延伸絲的所謂直接延伸法進行延伸。另外,延伸條件以1段至多段延伸為佳,延伸負荷率係以60~95%為佳。延伸負荷率是指進行延伸時的張力相對於纖維實際上斷絲的張力之比。 The method for extending the polyester fiber in the present invention can be extended by being temporarily entangled after being extracted from the extraction roller, which is carried out by a so-called segment stretching method. However, it is preferable to continuously carry out the stretching step by the extraction roller to supply the unstretched wire. The so-called direct extension method is extended. In addition, the extension condition is preferably extended from 1 to more stages, and the elongation load ratio is preferably 60 to 95%. The extension load ratio is the ratio of the tension at the time of stretching to the tension of the fiber actually broken.

延伸時的預熱溫度,係以在比聚酯未延伸絲的玻璃轉移點低20℃的溫度以上,比結晶化開始溫度低20℃的溫度以下進行為佳。延伸倍率依照紡絲速度而定,而以相對於破裂延伸倍率而言延伸負荷率成為60~95%的延伸倍率進行延伸為佳。另外,為了維持纖維強度並提升尺寸安定性,係以在延伸步驟中在170℃至纖維熔點以下的溫度進 行熱固定為佳。進一步以延伸時的熱固定溫度為170~270℃的範圍為佳。 The preheating temperature at the time of stretching is preferably at least 20 ° C lower than the glass transition point of the polyester undrawn yarn, and preferably lower than the crystallization start temperature by 20 ° C or lower. The stretching ratio is determined in accordance with the spinning speed, and is preferably extended at a stretching ratio in which the elongation load ratio is 60 to 95% with respect to the breaking stretch ratio. In addition, in order to maintain fiber strength and improve dimensional stability, the temperature is increased from 170 ° C to the melting point of the fiber in the stretching step. Heat fixation is preferred. Further, it is preferable that the heat setting temperature at the time of stretching is 170 to 270 °C.

進一步而言,本發明之聚酯纖維之製造方法,前提在於使用前處理聚酯纖維,此前處理方法是在聚合物的熔融擠出後添加含有環氧硬化觸媒的紡絲油劑,然後以高速抽取,接下來進行延伸,然後添加含有環氧化合物的整理油劑,進行加熱處理。 Further, the method for producing the polyester fiber of the present invention is premised on the use of the pretreated polyester fiber. The prior treatment method is to add a spinning oil agent containing an epoxy hardening catalyst after melt extrusion of the polymer, and then High-speed extraction, followed by extension, and then adding a finishing oil containing an epoxy compound for heat treatment.

熔融紡絲之後的紡絲油劑中所含有的環氧硬化觸媒,只要是可使之後整理油劑所含有的環氧化合物硬化的環氧硬化劑即可,鹼性硬化觸媒為佳,特別以胺化合物為佳。較具體而言,例如脂肪族胺化合物等的、更佳為在碳數4~22之脂肪族胺加成環氧乙烷及/或環氧丙烷2~20莫耳而得的胺化合物為最適合。 The epoxy curing catalyst contained in the spinning oil agent after melt spinning may be an epoxy curing agent which can cure the epoxy compound contained in the finishing oil agent, and an alkaline curing catalyst is preferable. In particular, an amine compound is preferred. More specifically, for example, an aliphatic amine compound or the like, more preferably an amine compound having an alkylamine having 4 to 22 carbon atoms and 2 or 20 moles of propylene oxide is the most Suitable for.

在本發明之製造方法中,紡絲油劑除了可含有上述環氧硬化觸媒之外,還可含有平滑劑、乳化劑、抗靜電劑等的通常的聚酯纖維之紡絲油劑所使用的物質以作為其他紡絲油劑構成成分。但是,在此紡絲油劑中係以不含環氧化合物為佳。較具體的其他成分可列舉平滑劑例如礦物油、脂肪酸酯類;乳化劑例如高級醇類或環氧乙烷(EO)加成物;抗靜電劑例如陰離子系、陽離子系的各種界面活性劑等。 In the production method of the present invention, the spinning oil agent may contain, in addition to the above epoxy curing catalyst, a usual polyester fiber spinning agent such as a smoothing agent, an emulsifier or an antistatic agent. The substance is used as a constituent of other spinning oils. However, it is preferred that the spinning oil is free of an epoxy compound. Specific examples of other specific components include smoothing agents such as mineral oils and fatty acid esters; emulsifiers such as higher alcohols or ethylene oxide (EO) adducts; and antistatic agents such as anionic surfactants, cationic surfactants, and the like. .

這種紡絲油劑中各成分的比例,係以環氧硬化觸媒(胺化合物等)3~20重量%、平滑劑30~80重量%、乳化劑20~70重量%、其他添加劑適量而成為100重量%的組合 為佳。藉由設定為這種配方,可提升所得到的前處理絲的接著性或耐久性,並且可發揮紡絲油劑原本的平滑性、集束性的機能,同時可減少在製絲步驟中的導紗鉤或延伸輥筒等的污染。 The ratio of each component in the spinning oil is 3 to 20% by weight of an epoxy curing catalyst (amine compound, etc.), 30 to 80% by weight of a smoothing agent, 20 to 70% by weight of an emulsifier, and other additives. Become a combination of 100% by weight It is better. By setting this formulation, the adhesion or durability of the obtained pretreated filament can be improved, and the original smoothness and bundling function of the spinning oil can be exerted, and the guide in the spinning step can be reduced. Contamination of yarn hooks or extension rollers.

本發明之橡膠補強用纖維可藉由如上述般的另一個本發明之聚酯纖維之製造方法等而得到。進一步為了使用於橡膠補強,將本發明之橡膠補強用聚酯纖維製成複絲,以實施撚絲而製成繩的形態來使用亦為適合。這種橡膠補強用聚酯纖維繩藉由將複絲纖維加以撚絲,強度利用率會平均化,其橡膠中的耐疲勞性提升。撚數係以在50~1000次/m的範圍為佳,進行下撚與上撚並且合絲的繩亦為適合。撚係數係以K=T.D1/2(T為每10cm的撚數、D為撚絲繩的纖度)為990~2500為佳。 The rubber reinforcing fiber of the present invention can be obtained by a method for producing a polyester fiber of the present invention as described above or the like. Further, in order to use for rubber reinforcement, it is also suitable to use the polyester fiber for rubber reinforcement of the present invention as a multifilament yarn and to form a rope by applying a twisted yarn. This rubber reinforcing polyester fiber rope is obtained by twisting the multifilament fiber, and the strength utilization rate is averaged, and the fatigue resistance in the rubber is improved. The number of turns is preferably in the range of 50 to 1000 times/m, and the string of the lower jaw and the upper jaw is also suitable. The coefficient of 捻 is K=T. D 1/2 (T is the number of turns per 10 cm, and D is the fineness of the string) is preferably 990 to 2500.

此外,構成合絲前的絲條的單絲數係以50~3000根為佳。藉由製成這種複絲,耐疲勞性或柔軟性會更提升。在纖度過小的情況,會有強度不足的傾向。相反地,在纖度過大的情況,會有變得過粗而無法柔軟性的問題,或在紡絲時容易發生單絲間的膠著,難以安定製造纖維的傾向。 Further, the number of filaments constituting the yarn before the yarn joining is preferably from 50 to 3,000. By making such a multifilament, fatigue resistance or softness is further enhanced. In the case where the fineness is too small, there is a tendency that the strength is insufficient. On the other hand, when the fineness is too large, there is a problem that it becomes too thick to be flexible, or it is likely to cause sticking between the filaments at the time of spinning, and it is difficult to stably manufacture the fibers.

另外,進一步本發明之橡膠補強用聚酯纖維係以在其表面添加纖維.橡膠用的RFL(間苯二酚.福馬林.乳膠)系黏著劑為佳。藉由將接著處理後的本發明之橡膠補強用聚酯纖維埋入未加硫橡膠並進行加硫,可製成纖維-橡膠複合體,最適合使用作為橡膠資材的輸送帶或軟管等。 In addition, the polyester fiber for rubber reinforcement of the present invention is to add fibers to the surface thereof. RFL (resorcinol. Formalin. Latex) adhesive for rubber is preferred. The rubber-reinforcing polyester fiber of the present invention which has been subjected to the subsequent treatment is embedded in an unsulfurized rubber and vulcanized, whereby a fiber-rubber composite can be obtained, and a conveyor belt or a hose which is a rubber material is most preferably used.

這種本發明之橡膠補強用聚酯纖維可保持高模數、低收縮率之物性,同時聚合物中的羧基末端與表面處理劑中的環氧基會發生反應,而具有高接著性。另外,固有黏度高,纖維軸方向的長週期小、耐久性優異的纖維,藉由其纖維表面的環氧基與羧基末端產生表面保護效果的相乘效果,會成為橡膠中的接著耐久性極優異的纖維。因此特別是本發明之橡膠補強用聚酯纖維,即使在橡膠中發生彎曲疲勞後,仍然能夠將與此橡膠的接著性或耐疲勞性保持在高水準,而成為高溫動態疲勞後的接著性極優異的橡膠補強用的聚酯纖維。特別是作為V型輸送帶等的伴隨著彎曲或高速旋轉等運動的纖維-橡膠複合體,即使在發生高負荷的動態變形的狀態,也可確保高耐疲勞性,同時由於為高模數.低收縮率,因此亦兼具免養護性等,能夠以高水準滿足各種需要的特性。 The rubber reinforcing polyester fiber of the present invention can maintain physical properties of high modulus and low shrinkage, and the carboxyl terminal in the polymer reacts with the epoxy group in the surface treating agent to have high adhesion. In addition, a fiber having a high intrinsic viscosity, a small long period in the fiber axis direction, and excellent durability can be used as a durability end in rubber by the effect of multiplying the epoxy group on the surface of the fiber with the surface protection effect at the carboxyl end. Excellent fiber. Therefore, in particular, the polyester fiber for rubber reinforcement of the present invention can maintain the adhesiveness or fatigue resistance of the rubber at a high level even after bending fatigue in the rubber, and becomes a susceptibility pole after high-temperature dynamic fatigue. Excellent polyester fiber for rubber reinforcement. In particular, a fiber-rubber composite which is subjected to movement such as bending or high-speed rotation, such as a V-belt, can ensure high fatigue resistance even in a state of high-load dynamic deformation, and at the same time, it is a high modulus. Since it has a low shrinkage rate, it is also a maintenance-free property, and it can satisfy various characteristics at a high level.

進一步而言,本發明之橡膠補強用的聚酯纖維適合以繩、織物、短纖維等的各式各樣的形態而使用作為纖維補強複合體。 Further, the polyester fiber for rubber reinforcement of the present invention is suitably used as a fiber-reinforcing composite in various forms such as rope, woven fabric, and short fiber.

例如在撚絲而製成纖維繩的形態的情況,可使用作為軟管補強用繩或輸送帶補強用繩。 For example, in the case of a form of a fiber rope which is twisted, it is possible to use a rope for reinforcing a hose or a belt for reinforcing a belt.

在使用本發明之聚酯纖維作為軟管補強用繩的情況,可保持高模數、低收縮率的物性,同時具有高接著性。另外,由於長週期小、耐久性優異的纖維,其纖維表面的環氧基與羧基末端產生表面保護效果的相乘效果,因此成為軟管基體中接著耐久性極優異的纖維繩。此外,使用本發 明之聚酯纖維的軟管補強用纖維繩在軟管基體中即使彎曲疲勞之後,其與基體的接著性或耐疲勞性還能夠保持在高水準,而成為高溫動態疲勞後的接著性極優異的軟管補強用纖維繩。這種軟管補強用纖維繩最適合使用於各種軟管,特別是橡膠軟管。 When the polyester fiber of the present invention is used as a hose reinforcing cord, physical properties of a high modulus and a low shrinkage ratio can be maintained while having high adhesion. In addition, since the fiber having a long period of time and excellent durability has an effect of multiplying the epoxy group on the surface of the fiber with the surface of the carboxyl group to produce a surface protection effect, it is a fiber rope excellent in durability in the hose base. In addition, use this hair When the fiber rope for reinforcing the hose of the polyester fiber is bent and fatigued in the hose base, the adhesion to the substrate or the fatigue resistance can be maintained at a high level, and the adhesion after high-temperature dynamic fatigue is extremely excellent. Hose reinforcement fiber rope. This type of hose reinforcement fiber rope is most suitable for use in a variety of hoses, especially rubber hoses.

軟管係以由上述本發明之聚酯纖維所構成之軟管補強用纖維繩、及橡膠或樹脂所構成的纖維補強軟管為佳。 The hose is preferably a fiber-reinforced hose composed of the above-mentioned polyester fiber of the present invention and a fiber-reinforced hose composed of rubber or resin.

這種軟管如果是例如橡膠軟管,則可如下述方式製造。首先藉由編結機(braider)將所得到的纖維繩以既定角度配置在由管狀橡膠所構成的內層上,使其成為既定密度。接下來,在其上配置層間橡膠薄片之後,再度藉由編結機配置纖維繩,進行此步驟既定次數。最後配置由用以保護外側補強纖維的覆蓋用橡膠所構成之外層,然後,使其在例如蒸氣加硫釜中進行蒸氣加硫,而製成橡膠軟管。進一步而言,上述纖維繩的配置係以設定為螺旋構造為佳。 Such a hose, if it is, for example, a rubber hose, can be manufactured as follows. First, the obtained fiber rope is placed on the inner layer made of tubular rubber at a predetermined angle by a braider to have a predetermined density. Next, after the interlayer rubber sheet is placed thereon, the fiber rope is again disposed by the knitting machine, and this step is performed a predetermined number of times. Finally, an outer layer is formed by covering rubber for protecting the outer reinforcing fibers, and then steam vulcanized in, for example, a steam vulcanization kettle to form a rubber hose. Further, the arrangement of the above-mentioned fiber ropes is preferably set to a spiral structure.

近年來,使用纖維補強軟管的狀況逐漸變得更加嚴苛。例如汽車的引擎室變得更加緊密,為了提高能量效率也逐漸朝向引擎室內的高溫化發展。在這種情況,特別是在剎車系統配管用等的用途,使軟管的大小不會變化,在高溫或施加張力的狀態中,補強纖維繩必須具有高水準的尺寸安定性。進一步而言,特別是在可動部分使用軟管的情況,除了軟管內的氣體或液體的內壓變動之外,外在物理因素使軟管形狀變化時,甚至會要求具有耐久性。 In recent years, the use of fiber-reinforced hoses has become more stringent. For example, the engine room of a car has become more compact, and in order to improve energy efficiency, it has gradually developed toward the high temperature in the engine room. In this case, particularly in the use of piping for piping, etc., the size of the hose does not change, and in the state of high temperature or tension, the reinforcing fiber rope must have a high level of dimensional stability. Further, particularly in the case where the hose is used in the movable portion, in addition to the internal pressure variation of the gas or liquid in the hose, external physical factors may require durability even when the shape of the hose is changed.

本發明申請案之聚酯纖維為低收縮且尺寸安定性優異 ,同時與橡膠的接著性優異,並提升了耐疲勞性。使用這種本發明之聚酯纖維的軟管能夠以高水準滿足上述要求。 The polyester fiber of the application of the invention has low shrinkage and excellent dimensional stability At the same time, it has excellent adhesion to rubber and improves fatigue resistance. The hose using the polyester fiber of the present invention can satisfy the above requirements at a high level.

另外,本發明之橡膠補強用的聚酯纖維亦適合使用作為輸送帶補強用的纖維材料。此輸送帶補強用纖維材料,係以將所得到的聚酯纖維製成複絲,並且實施撚絲製成繩的形態來使用的輸送帶補強用纖維材料為佳。或將所得到的聚酯纖維以織物的形態來使用的輸送帶補強用纖維材料亦為適合。 Further, the polyester fiber for rubber reinforcement of the present invention is also suitably used as a fiber material for reinforcing a conveyor belt. The belt reinforcing fiber material is preferably a belt reinforcing fiber material obtained by forming the obtained polyester fiber into a multifilament and using a twisted yarn to form a rope. Further, a fiber material for a belt reinforcement used in the form of a woven fabric of the obtained polyester fiber is also suitable.

例如輸送帶補強用纖維材料為織物的情況,構成此織物的經絲係以由本發明之聚酯纖維所構成之絲條為佳。絲條係以上述纖維繩形態為佳。 For example, in the case where the reinforcing fiber material for the belt is a woven fabric, the warp yarn constituting the woven fabric is preferably a yarn composed of the polyester fiber of the present invention. The yarn is preferably in the form of the above-mentioned fiber rope.

較具體而言,在以織物形輸送帶補強用材料來使用的情況,對於如上述般的本發明之聚酯纖維實施撚絲,將1000~1500根排列作為經絲,將這些經絲配上聚醯胺纖維或聚乙烯醇纖維等的合成纖維的無撚絲、或撚係數5000以下的撚絲作為緯絲,同時進行織布,而製成輸送帶補強用纖維材料為佳。 More specifically, when it is used as a material for a belt-shaped belt reinforcement, the polyester fiber of the present invention as described above is subjected to a twisted yarn, and 1000 to 1500 are arranged as warp yarns, and these warp yarns are used. It is preferable that the non-twisted yarn of the synthetic fiber such as polyamide fiber or polyvinyl alcohol fiber or the twisted yarn having a twist coefficient of 5,000 or less is used as the weft, and the woven fabric is simultaneously woven to form a fiber material for reinforcing the belt.

此織物的織物組織並未受到特別限定。但是,斜紋組織或緞紋組織在一定的伸長時強度會提高,在使用作為輸送帶的基布時,以少量的拉伸即可產生高張力,因此在輸送帶運行時可減輕噪音的產生,故特別適合,而適合使用於輸送器用的輸送帶等的輸送帶。 The fabric structure of this fabric is not particularly limited. However, the twill weave or the satin weave is increased in strength at a certain elongation, and when a base fabric as a conveyor belt is used, a high tension can be generated with a small amount of stretching, so that noise generation can be reduced when the conveyor belt is operated. Therefore, it is particularly suitable, and is suitable for use in a conveyor belt such as a conveyor belt for a conveyor.

這些織物與上述纖維繩相同地,以在其表面添加黏著劑為佳。例如在橡膠補強用途上,使用RFL系接著處理 劑進行處理為最適合。藉由將經過接著處理的本發明之輸送帶補強用纖維材料埋入未加硫橡膠並進行加硫,可使輸送帶成形。 These woven fabrics are preferably the same as the above-mentioned fiber ropes in that an adhesive is added to the surface thereof. For example, in rubber reinforcement applications, RFL is used to process The agent is processed to be most suitable. The conveyor belt can be formed by embedding the subsequently-treated belt material reinforcing fiber material of the present invention in an unsulfurized rubber and vulcanizing it.

本發明之聚酯纖維可保持高模數、低收縮率的物性,同時具有高接著性。另外,耐久性優異的纖維,在基體中的接著耐久性亦極為優異。因此這種含有本發明之聚酯纖維的輸送帶補強用纖維材料,即使在基體中發生彎曲疲勞後仍然能夠將與此基體的接著性或耐疲勞性保持在高水準,而為高溫動態疲勞後的接著性極優異的輸送帶補強用纖維材料。特別是V型輸送帶等的經常彎曲或高速旋轉等的運動的纖維.基體複合體,即使在發生高負荷的動態變形的狀態,也可確保高耐疲勞性,並且由於為高模數.低收縮率,因此亦兼具免養護性等,能夠以高水準滿足各種需要的特性。 The polyester fiber of the present invention can maintain physical properties of high modulus and low shrinkage while having high adhesion. Further, the fiber excellent in durability is extremely excellent in adhesion durability in the matrix. Therefore, the fiber material for reinforcing the belt containing the polyester fiber of the present invention can maintain the adhesion or fatigue resistance of the substrate at a high level even after bending fatigue in the matrix, and after high temperature dynamic fatigue A fiber material for belt reinforcement for excellent adhesion. In particular, V-shaped conveyor belts and other fibers that are often bent or rotated at high speed. The matrix composite ensures high fatigue resistance even in the state of high dynamic deformation, and is due to high modulus. Since it has a low shrinkage rate, it is also a maintenance-free property, and it can satisfy various characteristics at a high level.

這種使用本發明之聚酯纖維的輸送帶補強用纖維材料特別適合使用於作為V型輸送帶等的動力傳達輸送帶的芯線。圖1及圖2例示了其代表性的使用例。圖1係表示所得到的V型輸送帶1之縱剖面圖。該V型輸送帶,可為以天然纖維或合成纖維系織成的附橡膠的布2僅存在於輸送帶的上表面或下表面這種類型的輸送帶。由本發明之聚酯纖維所構成之芯線3埋設在與壓縮橡膠層5相接的接著橡膠層4。在壓縮橡膠層5中,往輸送帶寬度方向混有短纖維6。 Such a belt reinforcing fiber material using the polyester fiber of the present invention is particularly suitably used for a core of a power transmission belt which is a V-shaped belt or the like. 1 and 2 illustrate a representative use case thereof. Fig. 1 is a longitudinal sectional view showing the obtained V-shaped belt 1. The V-shaped conveyor belt may be a type of conveyor belt in which the rubber-coated cloth 2 woven from natural fibers or synthetic fibers is present only on the upper surface or the lower surface of the conveyor belt. The core wire 3 composed of the polyester fiber of the present invention is embedded in the adhesive rubber layer 4 which is in contact with the compression rubber layer 5. In the compression rubber layer 5, short fibers 6 are mixed in the width direction of the conveyor belt.

另外,使用本發明之聚酯纖維的纖維繩的使用例不受 如圖1所示般的類型的V型輸送帶所限定,亦可使用作為附橡膠的布2被覆輸送帶的整周的包覆型的V型輸送帶的芯線,另外還可使用作為位在如圖2所示般上述壓縮橡膠層5,在輸送帶長邊方向具有複數個肋條7的肋條型V型輸送帶8的芯線。 Further, the use of the fiber rope using the polyester fiber of the present invention is not affected. As defined in the V-shaped conveyor belt of the type shown in Fig. 1, it is also possible to use a core of a V-shaped conveyor belt of the entire circumference of the conveyor belt as a rubber-coated cloth 2, and it is also possible to use it as a bit. As shown in Fig. 2, the above-mentioned compression rubber layer 5 has a core wire of a rib-type V-shaped conveyor belt 8 having a plurality of ribs 7 in the longitudinal direction of the conveyor belt.

另外,輸送帶補強用纖維材料亦可為織物,而此情況下,例如藉由對上述聚酯纖維實施撚絲,將1000~1500根排列作為經絲,將該等經絲配上聚醯胺纖維、聚酯纖維,或聚乙烯醇纖維等的合成纖維之無撚絲、或撚係數5000以下的撚絲作為緯絲,同時進行織布,可製成所希望的輸送帶補強用纖維材料的補強用基布。織物組織係以斜紋組織或緞紋組織為佳。藉由製成斜紋組織或緞紋組織,在一定伸長時的強度提高,在使用作為輸送帶的基布時,以少量的拉伸即可產生高張力,此外還可減輕輸送帶運作時的噪音的產生。特別適合使用於輸送器用的輸送帶等的輸送帶。 In addition, the fiber material for reinforcing the conveyor belt may be a woven fabric. In this case, for example, by twisting the polyester fiber, 1000 to 1500 are arranged as warp yarns, and the warp yarns are blended with polyamine. A non-twisted yarn of a synthetic fiber such as a fiber, a polyester fiber, or a polyvinyl alcohol fiber, or a twisted yarn having a twist coefficient of 5,000 or less is used as a weft yarn, and a woven fabric is simultaneously produced to obtain a desired fiber material for reinforcing a belt. Reinforce the base fabric. The woven fabric is preferably twill or satin weave. By making a twill weave or a satin weave, the strength is increased at a certain elongation, and when a base fabric as a conveyor belt is used, a high tension can be generated with a small amount of stretching, and the noise during operation of the conveyor belt can be reduced. The production. It is particularly suitable for use in conveyor belts such as conveyor belts for conveyors.

使用以這種方式所得到的本發明之聚酯纖維的輸送帶補強用纖維材料係與橡膠或樹脂等的高分子一起使用,能夠製成纖維.高分子複合體的輸送帶。此時,高分子係以橡膠彈性體為佳。此複合體由於補強所使用的上述聚酯纖維的耐熱性或尺寸安定性優異,因此製成複合體時的成形性非常優異。特別適合作為橡膠輸送帶補強用,可適合使用於例如V型輸送帶或輸送器用的輸送帶等。 The fiber material for reinforcing the belt using the polyester fiber of the present invention obtained in this manner is used together with a polymer such as rubber or resin to form a fiber. Conveyor belt for polymer composites. In this case, the polymer is preferably a rubber elastomer. Since the polyester fiber used for reinforcement is excellent in heat resistance and dimensional stability, the composite is excellent in moldability when it is made into a composite. It is particularly suitable for use as a rubber conveyor belt reinforcement, and can be suitably used for, for example, a V-belt or a conveyor belt for a conveyor.

進一步而言,本發明之橡膠補強用的聚酯纖維亦可適 合使用於橡膠補強用短纖維。 Further, the polyester fiber for reinforcing rubber of the present invention may also be suitable Used in short fibers for rubber reinforcement.

以往,在短纖維補強複合體的領域中,特別是在重視耐疲勞性的用途,施加重覆的負荷時,會有所添加的短纖維的接著性低的問題。特別在高溫狀態的耐疲勞性方面,纖維與橡膠的接著性降低,其脫離部分會成為成形品的缺點。若受到負荷則容易由此部分發生龜裂,而導致疲勞特性降低的結果。特別在耐彎曲疲勞性的提升效果方面,現在還是有性能不足的問題。 Conventionally, in the field of short-fiber-reinforcing composites, particularly in applications where fatigue resistance is emphasized, when a heavy load is applied, there is a problem that the adhesion of the added short fibers is low. In particular, in terms of fatigue resistance in a high temperature state, the adhesion between the fiber and the rubber is lowered, and the detached portion is a disadvantage of the molded article. If it is subjected to a load, it is likely to be cracked in this portion, resulting in a decrease in fatigue characteristics. Especially in terms of the improvement of the bending fatigue resistance, there is still a problem of insufficient performance.

由本發明之聚酯纖維所構成之橡膠補強用短纖維可解決這種問題點,而為補強效果及耐彎曲疲勞性的提升效果優異的橡膠補強用短纖維。 The short fiber for rubber reinforcement which is composed of the polyester fiber of the present invention can solve such a problem, and is a short fiber for rubber reinforcement which is excellent in the reinforcing effect and the bending fatigue resistance.

使用本發明之聚酯纖維的橡膠補強用短纖維的纖維長係以0.3~10.0mm的長度為佳。在未滿0.3mm的情況,會有難以得到短纖維產生的補強效果的傾向,另外,在長於10.0mm的情況,短纖維彼此容易發生糾結,會有在橡膠內無法均勻分散的傾向。 The fiber length of the short fiber for rubber reinforcement using the polyester fiber of the present invention is preferably from 0.3 to 10.0 mm. When it is less than 0.3 mm, it is difficult to obtain the reinforcing effect by the short fibers, and when it is longer than 10.0 mm, the short fibers are likely to be entangled with each other, and there is a tendency that the fibers are not uniformly dispersed in the rubber.

另外,聚酯短纖維的單絲纖度係以0.1~100dtex/根為佳。進一步從強度、耐熱性或接著性的觀點看來,係以1~20dtex/根為佳。 Further, the monofilament fineness of the polyester staple fiber is preferably from 0.1 to 100 dtex/root. Further, from the viewpoint of strength, heat resistance or adhesion, it is preferably from 1 to 20 dtex/root.

這種橡膠補強用聚酯短纖維可藉由將如上述方式進行紡絲、延伸所得到的本發明之聚酯纖維切成既定長度而得到。 Such a polyester reinforcing polyester staple fiber can be obtained by cutting a polyester fiber of the present invention obtained by spinning and stretching as described above into a predetermined length.

此橡膠補強用聚酯短纖維,其纖維表面附著有具有環氧基的表面處理劑,而從操作性的層面看來,其製造方法 係以採用在長纖維階段進行表面處理,然後切斷的手段為佳。此處具有環氧基的表面處理劑係含有上述環氧化合物。 The polyester reinforcing short fiber has a surface treating agent having an epoxy group attached to the surface of the fiber, and the manufacturing method is from the viewpoint of operability. It is preferred to use a surface treatment in the long fiber stage and then cut off. The surface treating agent having an epoxy group herein contains the above epoxy compound.

進一步而言,橡膠補強用聚酯短纖維係以在其表面添加纖維.橡膠用的RFL(間苯二酚.福馬林.乳膠)系黏著劑為佳。由長纖維切成短纖維在添加RFL黏著劑前後進行皆可,而從操作性的層面看來,以在添加RFL黏著劑後進行切斷為佳。將經過接著處理後的本發明之橡膠補強用聚酯短纖維混練至未加硫橡膠,在橡膠中埋入短纖維後進行加硫,藉此可製成較適合的纖維.橡膠複合體。 Further, the polyester reinforcing polyester staple fiber is added to the surface of the fiber. RFL (resorcinol. Formalin. Latex) adhesive for rubber is preferred. Cutting the long fibers into short fibers can be performed before and after the addition of the RFL adhesive, and from the viewpoint of operability, it is preferable to perform the cutting after the addition of the RFL adhesive. The rubber reinforcing polyester staple fiber of the present invention which has been subjected to the subsequent treatment is kneaded to an unvulcanized rubber, and short fibers are embedded in the rubber, followed by vulcanization, thereby making a suitable fiber. Rubber compound.

這種由本發明之聚酯纖維所構成之橡膠補強用聚酯短纖維可保持適合基體補強的高模數、低收縮率的物性,同時具有高接著性。另外,還會成為耐久性優異的纖維,橡膠中的接著耐久性極優異的短纖維。 The polyester reinforcing polyester staple fiber composed of the polyester fiber of the present invention can maintain a high modulus of low modulus and a low shrinkage property suitable for matrix reinforcement, and has high adhesion. In addition, it is a fiber excellent in durability and a short fiber excellent in adhesion durability in rubber.

特別是這種橡膠補強用聚酯短纖維,會成為即使在橡膠中發生彎曲疲勞後,仍然能夠將其與橡膠的接著性或耐疲勞性保持在高水準,在高溫動態疲勞後的接著性極優異的橡膠補強用的聚酯短纖維。特別是作為經常彎曲或高速旋轉等的運動的纖維.橡膠複合體,即使在受到高負荷的動態變形的狀態,也可確保高耐疲勞性,並且為高模數.低收縮率,因此亦兼具免養護性等,能夠以高水準滿足各種需要的特性。 In particular, the polyester short fiber for rubber reinforcement can maintain the adhesiveness or fatigue resistance of the rubber at a high level even after bending fatigue in the rubber, and the adhesive pole after dynamic fatigue at high temperature. Excellent polyester staple fiber for rubber reinforcement. Especially as a fiber that often bends or rotates at high speed. The rubber composite ensures high fatigue resistance even in the state of high dynamic deformation, and is high modulus. Since it has a low shrinkage rate, it is also a maintenance-free property, and it can satisfy various characteristics at a high level.

以這種方式所得到的橡膠補強用聚酯短纖維可與橡膠一起使用,而製成強度與耐久性優異的成形體。例如將未 加硫橡膠與橡膠補強用短纖維藉由捏合機等加以混練,使其分散之後,藉由加硫,可得到短纖維補強橡膠成形品。所得到的成形品,其強度與對疲勞性優異,因此最適合使用作為輸送帶、軟管、輪胎等各種橡膠製品。 The polyester reinforcing polyester staple fiber obtained in this manner can be used together with a rubber to form a molded body excellent in strength and durability. For example, it will not The vulcanized rubber and the short fiber for rubber reinforcement are kneaded by a kneader or the like to be dispersed, and then a short fiber-reinforced rubber molded article can be obtained by vulcanization. Since the obtained molded article is excellent in strength and fatigue resistance, it is most suitably used as various rubber products such as a conveyor belt, a hose, and a tire.

[實施例] [Examples]

在下述實施例進一步對本發明作較具體說明,而本發明的範圍並不受這些實施例所限定。另外,各種特性係藉由下述方法作測定。 The invention is further illustrated in the following examples, which are not to be construed as limited. In addition, various characteristics were measured by the following methods.

(1)固有黏度: (1) Intrinsic viscosity:

對於使聚酯碎片、聚酯纖維在100℃、以60分鐘溶於鄰氯酚而成的稀薄溶液,在35℃下使用烏氏粘度計作測定,由所測得的值求得。表記為IV。 A thin solution obtained by dissolving polyester chips and polyester fibers in o-chlorophenol at 100 ° C for 60 minutes was measured at 35 ° C using an Ubbelohde viscometer and determined from the measured values. The table is IV.

(2)末端羧基量 (2) The amount of terminal carboxyl groups

將使用粉碎機製成粉末狀的聚酯樣品40.00克,及苄醇100ml加至燒瓶,在氮氣流下且在215±1℃的條件下,花費4分鐘使聚酯樣品溶於苄醇。溶解後,使樣品溶液冷卻至室溫之後,添加適量的酚紅的苄醇0.1質量%溶液,藉由N規定的氫氧化鈉的苄醇溶液,迅速進行滴定,將變色發生為止的滴入量定為Aml。在100ml的苄醇中添加相同量的酚紅之苄醇0.1質量%溶液作為空白試樣,藉由N規定的氫氧化鈉之苄醇溶液迅速地滴定,將變色發生為 止的滴入量定為Bml。由這些值藉由下述式計算聚酯樣品中的末端COOH基含量(末端羧基量)。 A powder sample of 40.00 g of a polyester sample and a benzyl alcohol 100 ml were added to the flask using a pulverizer, and the polyester sample was dissolved in benzyl alcohol under a nitrogen stream at 215 ± 1 ° C for 4 minutes. After the solution is dissolved, the sample solution is cooled to room temperature, and an appropriate amount of a phenol red benzyl alcohol 0.1% by mass solution is added thereto, and the benzyl alcohol solution of sodium hydroxide is used to rapidly titrate the amount of the dying. Set to Aml. Adding the same amount of phenol red benzyl alcohol 0.1% by mass solution to 100 ml of benzyl alcohol as a blank sample, and rapidly titrating with a benzyl alcohol solution of N-specified sodium to cause discoloration to occur as The amount of drip was determined to be Bml. From these values, the terminal COOH group content (end carboxyl group amount) in the polyester sample was calculated by the following formula.

末端COOH基含量(當量/ton)=(A-B)×103×N×106/40 Terminal COOH group content (equivalent/ton) = (AB) × 10 3 × N × 10 6 / 40

此外,此處使用的苄醇是利用將試藥特級的物品蒸餾,並保管在遮光瓶的苄醇。當量濃度為N的氫氧化鈉的苄醇溶液,係使用藉由定法事先藉由濃度已知的硫酸溶液進行滴定,正確地求得當量濃度N的溶液。 Further, the benzyl alcohol used herein is a benzyl alcohol which is distilled in a light-shielding bottle by using an article which is a reagent grade. A benzyl alcohol solution of sodium hydroxide having an equivalent concentration of N is titrated with a sulfuric acid solution having a known concentration in advance by a predetermined method to accurately obtain a solution having an equivalent concentration N.

(3)表面羧基量(纖維表面末端羧基量) (3) The amount of surface carboxyl groups (the amount of carboxyl groups at the end of the fiber surface)

依據JIS K0070-3.1項中和滴定法求得纖維表面的羧基量(酸價)。亦即,在約5g纖維試樣中加入二乙醚/乙醇=1/1溶液50ml,並添加作為指示劑的酚酞溶液數滴,在室溫以超音波振動15分鐘。以0.1ml氫氧化鉀乙醇溶液(係數值f=1.030)對此溶液滴定,將指示劑的淺紅色持續30秒鐘時定為終點,測定指示劑的滴入量,由以下的算式算出酸價。 The amount of carboxyl groups (acid value) on the surface of the fiber was determined according to the JIS K0070-3.1 neutralization titration method. That is, 50 ml of a diethyl ether/ethanol = 1/1 solution was added to about 5 g of the fiber sample, and a few drops of the phenolphthalein solution as an indicator were added, and ultrasonic vibration was performed for 15 minutes at room temperature. The solution was titrated with 0.1 ml of potassium hydroxide ethanol solution (coefficient value f = 1.030), and the light red color of the indicator was determined as the end point for 30 seconds, and the amount of the indicator was measured. The acid value was calculated from the following formula. .

酸價A(當量/ton)=(B×1.030×100)/S[此處,B表示0.1ml氫氧化鉀乙醇溶液滴定量(ml)、S表示試樣量(g)]。 Acid value A (equivalent/ton) = (B × 1.030 × 100) / S [here, B represents 0.1 ml of a potassium hydroxide ethanol solution titration (ml), and S represents a sample amount (g)].

(4)末端甲基量 (4) terminal methyl group

使聚酯水解,分成酸成分和二元醇成分之後,以氣相層析定量酸的甲酯成分,並由此值算出。 After the polyester was hydrolyzed and separated into an acid component and a glycol component, the methyl ester component of the acid was quantified by gas chromatography, and the value was calculated from this value.

(5)氧化鈦含量 (5) Titanium oxide content

各元素的含量係使用螢光X射線裝置(Rigaku公司,3270E型)作測定,進行定量分析。在進行此螢光X射線測定時,將聚酯纖維樹脂聚合物樣品以壓延機在260℃加熱2分鐘,同時在7MPa的加壓條件下製作出具有平坦面的測試成形體並實施測定。 The content of each element was measured by a fluorescent X-ray apparatus (Rigaku Corporation, Model 3270E) for quantitative analysis. In the case of this X-ray measurement, the polyester fiber resin polymer sample was heated at 260 ° C for 2 minutes in a calender, and a test molded body having a flat surface was produced under a pressure of 7 MPa and measured.

(6)纖維橫軸方向結晶粒徑(X射線繞射) (6) Crystal grain size in the transverse direction of the fiber (X-ray diffraction)

關於聚酯組成物.纖維的X射線繞射測定,係使用X射線繞射裝置(Rigaku股份有限公司製RINT-TTR3、Cu-K α射線、管電壓=50kV、電流300mA,平行光束法)進行。長週期間隔係使用X射線小角散射測定裝置,藉由以往周知的方法,亦即以波長1.54Å的Cu-K α射線作為射線源,從與纖維軸成直角的方向來照射,由所得到的子午線干涉的繞射線,使用布拉格公式作計算(單位;nm2)。纖維橫軸方向結晶粒徑係由X射線廣角繞射得到赤道線掃描的(010)(100)強度分布曲線,使用謝樂公式(Scherrer formula)由分布曲線中的半寬度求得。 About polyester composition. The X-ray diffraction measurement of the fiber was carried out using an X-ray diffraction apparatus (RINT-TTR3, Cu-Kα ray, tube voltage = 50 kV, current 300 mA, parallel beam method, manufactured by Rigaku Co., Ltd.). The long-period interval is obtained by irradiating a direction perpendicular to the fiber axis by a conventionally known method, that is, a Cu-K α ray having a wavelength of 1.54 Å as a radiation source by using a conventionally known method. The ray of the meridian interference is calculated using the Bragg formula (unit; nm 2 ). The crystal grain size in the transverse direction of the fiber was obtained by X-ray wide-angle diffraction to obtain an (010) (100) intensity distribution curve of the equatorial line scan, which was obtained from the half width in the distribution curve using the Scherrer formula.

(7)環氧指數(EI) (7) Epoxy index (EI)

對於加熱處理後之該聚酯纖維依照JIS K-7236測定環氧指數(EL:纖維每1kg的環氧當量數)。 The polyester fiber after the heat treatment was measured for the epoxy index (EL: the number of epoxy equivalents per 1 kg of the fiber) in accordance with JIS K-7236.

(8)纖維的強拉伸率(%)及中間拉伸率(%) (8) Strong tensile ratio (%) of fiber and intermediate stretching ratio (%)

使用拉伸荷重測定器(島津製作所股份有限公司製Autograph),依照JIS-L1013作測定。此外中間拉伸率表示在強度4cN/dtex時的拉伸率。 A tensile load measuring instrument (Autograph manufactured by Shimadzu Corporation) was used for measurement in accordance with JIS-L1013. Further, the intermediate stretch ratio indicates the elongation at a strength of 4 cN/dtex.

(9)乾熱收縮率(%) (9) Dry heat shrinkage rate (%)

依據JIS-L1013,放置在20℃、65%RH的溫濕度控制的房間24小時後,在無荷重狀態下,在乾燥機內進行180℃×30min熱處理,由熱處理前後試樣的長度差值作計算。 According to JIS-L1013, after being placed in a room controlled by temperature and humidity of 20 ° C and 65% RH for 24 hours, heat treatment at 180 ° C × 30 min in a dryer under no load condition, and the difference in length of the sample before and after heat treatment Calculation.

(10)步驟評估 (10) Step evaluation

關於本發明之前處理聚酯纖維之步驟評估,從生產安定性、撚絲浮垢、生產效率、經濟性的層面來考量,以+++:優異;++:普通;+:不良的3階段來評估聚合物成本。 Regarding the evaluation of the steps of treating the polyester fiber before the present invention, it is considered from the aspects of production stability, silk scum, production efficiency, economy, +++: excellent; ++: ordinary; +: bad 3 stage To evaluate polymer costs.

(11)耐熱強度維持率 (11) Heat resistance strength retention rate

將2根聚酯纖維實施上撚470次/m、下撚470次/m而製成原繩,將此原繩浸漬於RFL黏著劑,在張力下並在240℃處理2分鐘而得到處理繩,測定該處理繩的強度 ,將測得的值定為強度A。然後,將處理繩埋入加硫模具中,在80℃下加硫120分鐘,將促進加硫後的處理繩取出並測定強度,將所測得值定為強度B,藉由B/A(%)的算式求得強度維持率。 Two polyester fibers were placed on the upper 捻470 times/m and the lower jaw was 470 times/m to prepare a raw rope. The raw rope was immersed in an RFL adhesive, and treated under tension at 240 ° C for 2 minutes to obtain a treated rope. , measuring the strength of the treated rope , the measured value is determined as the intensity A. Then, the treatment rope is embedded in a vulcanization mold, and sulfur is added at 80 ° C for 120 minutes, and the treated rope after the promotion of the sulfurization is taken out and the strength is measured, and the measured value is determined as the strength B by B/A ( The formula of %) finds the strength maintenance rate.

(12)初期剝離接著力 (12) Initial peeling force

此值表示處理繩與橡膠的接著力。將繩以36根/2.54cm(inch)拉整齊,以0.5mm厚的天然橡膠為主成分的摻合了支撐物的未加硫橡膠薄片夾住。使這些薄片往直向重合,在150℃的溫度下,以50kg/cm2的壓延壓力進行加硫30分鐘,接下來,沿著繩方向切成長條狀。將沿著所製作出的樣品的長條的薄片往相對於橡膠薄片面而言90度的方向,以200mm/分鐘的速度剝離,將此剝離所需要的力以N/2.54cm(inch)表示。此外,此初期剝離接著力是在室溫作測定而得的值。 This value represents the adhesion of the treated rope to the rubber. The rope was pulled neatly at 36 pieces/2.54 cm (inch), and the non-sulfurized rubber sheet with the support added with 0.5 mm thick natural rubber as a main component was sandwiched. These sheets were superposed in the straight direction, and vulcanized at a temperature of 150 ° C at a rolling pressure of 50 kg/cm 2 for 30 minutes, and then cut into strips along the rope direction. The long piece of the sample to be produced was peeled off at a speed of 200 mm/min in a direction of 90 degrees with respect to the surface of the rubber sheet, and the force required for the peeling was expressed by N/2.54 cm (inch). . Further, the initial peeling adhesion force is a value obtained by measuring at room temperature.

(13)動態疲勞後與橡膠的接著性能評估(擦鞋測定(1)) (13) Evaluation of the subsequent performance of rubber after dynamic fatigue (shoe-shoe measurement (1))

將2.5mm厚的SBR/NR系橡膠夾住,將所得到的繩以26根/2.54cm(inch)的密度製作出互相平行排列的2層單布層,進一步將各單布層的外側以1.5mm厚的SBR/NR系橡膠覆蓋後,以溫度150℃、30分鐘、90kg/cm2的條件進行加硫,製作出長度500mm、寬度5mm、厚度5.5mm的輸送帶。 The 2.5 mm thick SBR/NR-based rubber was sandwiched, and the obtained rope was made into a two-layer single-layer layer which was arranged in parallel with each other at a density of 26 pieces/2.54 cm (inch), and the outer side of each single-layer layer was further After covering with a 1.5 mm thick SBR/NR-based rubber, vulcanization was carried out under the conditions of a temperature of 150 ° C, 30 minutes, and 90 kg/cm 2 to prepare a conveyor belt having a length of 500 mm, a width of 5 mm, and a thickness of 5.5 mm.

接下來,對此輸送帶施加50kg/2.54cm(inch)的荷重 ,並安裝在直徑50mm的滑輪,在溫度100℃,花費5小時實施30000循環的反覆伸張壓縮疲勞。將伸張壓縮疲勞後的輸送帶的單布層間以300mm/分鐘的速度剝離,求得所得到的平均剝離接著力(N/2.54cm(inch))以作為高溫動態疲勞後的接著力。 Next, a load of 50 kg / 2.54 cm (inch) is applied to the conveyor belt. And installed on a 50mm diameter pulley, at a temperature of 100 ° C, it takes 5 hours to carry out 30,000 cycles of repeated tensile compression fatigue. The single cloth layer of the conveyor belt after stretching and compressing fatigue was peeled off at a speed of 300 mm/min, and the obtained average peeling adhesion force (N/2.54 cm (inch)) was obtained as an adhesive force after high-temperature dynamic fatigue.

此評估方法稱為動態彎曲測試,所謂擦鞋測試的評估方法。 This evaluation method is called dynamic bending test, the so-called shoe-shoe test evaluation method.

(14)軟管疲勞性 (14) Hose fatigue

施加壓力使軟管內的壓力成為3.5kg/cm2,在彎曲成85°的狀態以850rpm的轉速旋轉,每29分鐘改變旋轉方向,測量軟管破裂為止的時間(分鐘)。 Pressure was applied so that the pressure in the hose became 3.5 kg/cm 2 , and the rotation was performed at 850 rpm in a state of being bent at 85°, the rotation direction was changed every 29 minutes, and the time (minutes) until the hose was broken was measured.

(15)輸送帶張力維持率 (15) Conveyor belt tension maintenance rate

在直徑100mm的兩個滑輪間架設V型輸送帶,將初期安裝的張力定為900N,將運行中的滑輪轉速定為3600r.p.m.,在室溫進行運行測試。然後在運行4小時後使其停止,進一步測定放涼24小時後的輸送帶張力,測定相對於初期安裝的張力而言的張力維持率(%)。 A V-shaped conveyor belt was placed between the two pulleys with a diameter of 100 mm, the initial installation tension was set to 900 N, and the running pulley speed was set to 3600 r.p.m., and the operation test was performed at room temperature. Then, after running for 4 hours, the pressure was stopped, and the belt tension after cooling for 24 hours was further measured, and the tension maintenance ratio (%) with respect to the tension of the initial mounting was measured.

(16)輸送帶尺寸變化率 (16) Conveyor belt dimensional change rate

將加硫之後的輸送帶外周長與經過30天後的V型輸送帶外周長之差除以加硫之後之輸送帶外周長,算出輸送帶的尺寸變化率(%)。 The difference in the dimensional change (%) of the conveyor belt was calculated by dividing the difference between the outer circumference of the conveyor belt after vulcanization and the outer circumference of the V-belt after 30 days by the outer circumference of the conveyor belt after vulcanization.

(17)擦鞋測定(shoeshine test)(2)(輸送帶動態疲勞後與橡膠的接著性能評估) (17) Shoeshine test (2) (Evaluation of the subsequent performance of rubber after dynamic fatigue of the conveyor belt)

對將聚酯纖維製成芯線的V型輸送帶及基布補強輸送帶施加50kg/2.54cm(inch)的荷重,並安裝在直徑50mm的滑輪,在溫度100℃下花費5小時實施30000循環的反覆伸張壓縮疲勞。將伸張壓縮疲勞後的輸送帶的單布層間以300mm/分鐘之速度剝離,將所得到的平均剝離接著力(N/2.54cm(inch))定為高溫動態疲勞後之接著力而求得。 A load of 50 kg/2.54 cm (inch) is applied to a V-shaped conveyor belt and a base fabric reinforcing conveyor belt in which a polyester fiber is made into a core wire, and is mounted on a pulley having a diameter of 50 mm, and it takes 5 hours at a temperature of 100 ° C to carry out 30,000 cycles. Repeated compression and fatigue. The single cloth layer of the conveyor belt after stretching and compression fatigue was peeled off at a speed of 300 mm/min, and the obtained average peeling adhesion force (N/2.54 cm (inch)) was determined as the adhesion force after high-temperature dynamic fatigue.

(18)短纖維補強橡膠成形品的降伏拉伸強度、破裂拉伸率 (18) Degraded tensile strength and fracture elongation of short fiber reinforced rubber molded articles

此值表示以短纖維補強的橡膠成形品之補強效果與延伸率,依據JIS K6301,將3號啞鈴狀測試片以500mm/分鐘的拉伸速度斷裂時的降伏點荷重除以測試片的剖面積所得到的值定為降伏拉伸強度(kg/cm2),將斷裂時的標線間延伸率定為破裂拉伸率(%)。 This value indicates the reinforcing effect and elongation of the rubber molded article reinforced with short fibers. According to JIS K6301, the drop point load when the No. 3 dumbbell-shaped test piece is broken at a tensile speed of 500 mm/min is divided by the sectional area of the test piece. The obtained value was defined as the tensile strength at break (kg/cm 2 ), and the elongation between the lines at the time of the fracture was defined as the elongation at break (%).

(20)短纖維補強橡膠成形品的彎曲疲勞壽命 (20) Bending fatigue life of short fiber reinforced rubber molded articles

判定以短纖維補強的橡膠成形品的耐疲勞性的指標,使用東洋製機股份有限公司的DeMattia式彎曲疲勞測試機,在80℃氣體環境下,以5Hz的週期使3號啞鈴狀測試片彎曲25%,將發生龜裂為止的次數定為彎曲疲勞壽命(萬次)。 The DeMattia-type bending fatigue tester of Toyo Seiki Co., Ltd. was used to determine the fatigue resistance of the rubber-formed product reinforced with short fibers, and the dumbbell-shaped test piece No. 3 was bent at a cycle of 5 Hz in a gas atmosphere of 80 °C. 25%, the number of occurrences of cracks is defined as the bending fatigue life (10,000 times).

[實施例1] [Example 1] (a)紡絲油劑的調製 (a) Modulation of spinning oil

將由三油酸甘油酯65份、POE(10)月桂基胺基醚12份、POE(20)硬化蓖麻油醚8份、POE(20)硬化蓖麻油三油酸酯12份、POE(8)油基磷酸酯Na2份、抗氧化劑1份所構成之油劑組成分10份加熱至50℃。 65 parts of triolein, 12 parts of POE (10) lauryl amine ether, 8 parts of hardened castor oil ether of POE (20), 12 parts of hardened castor oil trioleate of POE (20), POE (8) The oil composition consisting of oleyl phosphate Na2 part and 1 part of antioxidant was heated to 50 ° C in 10 parts.

(b)完工油劑之調製 (b) Modulation of finished oil

將由聚甘油聚縮水甘油醚(Nagase Chem Tex公司製「DENAKOL EX-512」)60份、壬二酸二異辛酯30份、POE(8)硬化蓖麻油醚8份、磺基琥珀酸二異辛酯Na2份所構成之油劑組成分45份加熱至40℃之後,徐緩添加至加熱至40℃的軟化水55份,同時攪拌之後,冷卻至18℃。 60 parts of polyglycerol polyglycidyl ether ("DENAKOL EX-512" manufactured by Nagase Chem Tex Co., Ltd.), 30 parts of diisooctyl sebacate, 8 parts of hardened castor oil ether of POE (8), and diisophoric sulfosuccinate After 45 parts of the oil component composed of the octyl ester Na2 part was heated to 40 ° C, it was slowly added to 55 parts of demineralized water heated to 40 ° C, and after stirring, it was cooled to 18 ° C.

(c)聚酯纖維之製造 (c) Manufacture of polyester fibers

使用固相聚合後碎片的固有黏度(以35℃鄰氯酚溶劑作測定)1.03,末端羧基量為20當量/ton,末端甲基量為0當量/ton,氧化鈦含量為0.05wt%的藉由直接聚合法所得到的聚對苯二甲酸乙二酯碎片,以紡絲拉伸1777的條件,藉由熔融紡絲法,得到384單絲的聚酯纖維。 The intrinsic viscosity of the chips after solid phase polymerization (measured by o-chlorophenol solvent at 35 ° C) was 1.03, the amount of terminal carboxyl groups was 20 equivalents/ton, the amount of terminal methyl groups was 0 equivalents/ton, and the content of titanium oxide was 0.05 wt%. The polyethylene terephthalate chips obtained by the direct polymerization method were obtained by a melt spinning method to obtain 384 monofilament polyester fibers under the conditions of a spinning stretch of 1777.

在由金屬紡嘴紡出並以2800m/分鐘抽取的未延伸絲添加藉由上述方法所調製出的紡絲油劑,使其成為相對於纖維100份而言油劑附著成分0.4份(脂肪族胺化合物成分附著量0.048重量%)之後,在60℃的第1輥筒進行抽 取,在第1輥筒與60℃的第2輥筒之間進行第1段延伸至1.25倍,進一步在第2輥筒與180℃的第3輥筒之間進行第2段延伸至合計延伸倍率為1.43倍,接下來在第3輥筒與第4輥筒之間以延伸倍率1.0倍進行延伸之後,藉由輥筒式油劑添加法添加由上述方法調製成的完工油劑,使其成為相對於纖維100份而言油劑附著成分為0.2重量份(環氧化合物成分附著量0.12重量%),在第4輥筒與纏繞機之間,藉由交絡(IL)噴嘴賦予交絡之後,以5000m/分鐘之速度纏繞各10kg。所得到的纖維係具有固有黏度為0.91、纖度為1130dtex、強度為6.9cN/dtex、拉伸率為12%的力學特性,末端羧基量為22當量/ton,長週期為10nm、纖維表面末端羧基量為7當量/ton、纖維橫軸方向的結晶粒徑為45nm2、末端甲基量為0當量/ton、氧化鈦含量為0.05wt%、表面環氧基量為0.1×10-3當量/kg。 The spinning oil prepared by the above method was added to the undrawn yarn which was spun from a metal spout and extracted at 2800 m/min, so that it became 0.4 parts of the oil adhering component with respect to 100 parts of the fiber (aliphatic After the amount of the amine compound component adhered was 0.048% by weight, the first roll was taken at 60 ° C, and the first roll was extended to 1.25 times between the first roll and the second roll at 60 ° C, and further in the second stage. The second stage is extended between the roll and the third roll of 180 ° C to a total stretch ratio of 1.43 times, and then extended by a stretch ratio of 1.0 times between the third roll and the fourth roll. In the roller type oil additive method, the finished oil agent prepared by the above method is added so as to be 0.2 parts by weight (the epoxy compound component adhesion amount is 0.12% by weight) based on 100 parts of the fiber. Between the 4 rolls and the winding machine, after the entanglement was given by the interlacing (IL) nozzle, each 10 kg was wound at a speed of 5000 m/min. The obtained fiber system had mechanical properties of an intrinsic viscosity of 0.91, a fineness of 1,130 dtex, a strength of 6.9 cN/dtex, and a tensile ratio of 12%. The terminal carboxyl group amount was 22 equivalent/ton, the long period was 10 nm, and the fiber surface terminal carboxyl group. The amount is 7 equivalents/ton, the crystal grain size in the transverse direction of the fiber is 45 nm 2 , the terminal methyl group amount is 0 equivalent/ton, the titanium oxide content is 0.05 wt%, and the surface epoxy group amount is 0.1 × 10 -3 equivalent / Kg.

將以這樣的方式所得到的纖維在30℃的溫度下進行熟成處理360小時。儘管紡絲速度快,在生產步驟中的浮垢產生量少。 The fiber obtained in this manner was subjected to a ripening treatment at a temperature of 30 ° C for 360 hours. Despite the high spinning speed, the amount of scum generated in the production step is small.

所得到的聚酯纖維實施470次/m的下撚之後,將其2根合併,實施470次/m的上撚而得到繩,對此繩使用間苯二酚.福馬林.乳膠接著液(RFL液)進行接著處理,在240℃下收縮熱處理2分鐘,而製成處理繩。 After the obtained polyester fiber was subjected to squatting at 470 times/m, two of them were combined, and a 470 times/m upper sputum was applied to obtain a rope, and resorcinol was used for the rope. Fomalin. The latex binder (RFL solution) was subjected to subsequent treatment, and heat treatment was carried out at 240 ° C for 2 minutes to prepare a treated rope.

關於所得到的聚酯纖維及繩的物性,強度為134N、拉伸率為13%、44N時的拉伸率為3.9%、177℃乾熱收縮率為2.7%。 The physical properties of the obtained polyester fiber and rope were 134 N, the elongation was 13%, the elongation at 44 N was 3.9%, and the dry heat shrinkage at 177 ° C was 2.7%.

使用此繩實施擦鞋測定的結果,動態疲勞後繩的剝離接著力為550N/inch,而保持非常高的接著力。將所得到的聚酯纖維及處理繩之物性與接著評估結果揭示於表1及表2。 As a result of performing the shoe-shoe measurement using this rope, the peeling force of the rope after dynamic fatigue was 550 N/inch, while maintaining a very high adhesion force. The physical properties of the obtained polyester fiber and treated rope and the results of subsequent evaluation are disclosed in Tables 1 and 2.

[比較例1] [Comparative Example 1]

除了將實施例1之固相聚合後的碎片的末端羧基由20當量/ton改變為9當量/ton,使用末端甲基量為5當量/ton的聚酯碎片以外,係以與實施例1同樣的方式進行,最終纖度為相同的1130dtex、固有黏度為0.91之聚酯纖維,將其加以撚絲而得到處理繩。將所得到的聚酯纖維及處理繩的物性、及接著評估結果一併揭示於表1及表2。與實施例1相比,纖維的末端羧基量為18當量/ton,而為較低,可得到通常的剝離接著力,耐熱強度維持率亦足夠。但是,在動態疲勞後的接著性(擦鞋測定)之中為不良的。 The same procedure as in Example 1 was carried out except that the terminal carboxyl group of the fragment obtained by solid phase polymerization of Example 1 was changed from 20 equivalents/ton to 9 equivalents/ton, and polyester chips having a terminal methyl group amount of 5 equivalents/ton were used. The method was carried out, and the final fineness was the same 1130 dtex polyester fiber having an intrinsic viscosity of 0.91, which was twisted to obtain a treated rope. The physical properties of the obtained polyester fiber and treated cord, and the results of subsequent evaluation are shown in Tables 1 and 2. Compared with Example 1, the amount of terminal carboxyl groups of the fibers was 18 equivalents/ton, and was lower, and a usual peeling adhesion force was obtained, and the heat-resistant strength maintaining ratio was also sufficient. However, it is unfavorable in the adhesion (shoe-shoe measurement) after dynamic fatigue.

[比較例2] [Comparative Example 2]

與比較例1不同,除了不採用環氧化合物,並使用將胺成分由紡絲油劑去除的非胺系的紡絲油劑之外,以與比較例1同樣的方式進行。將所得到的聚酯纖維及處理繩的物性與接著評估結果一併揭示於表1及表2。與比較例1相比,甚至在動態疲勞後的接著性(擦鞋測定)之中為不良。 In the same manner as in Comparative Example 1, except that the epoxy compound was not used and the non-amine-based spinning oil agent in which the amine component was removed by the spinning oil agent was used. The physical properties of the obtained polyester fiber and treated cord are shown in Tables 1 and 2 together with the results of subsequent evaluation. Compared with Comparative Example 1, it was poor even in the adhesion (shoe-shoe measurement) after dynamic fatigue.

[實施例2] [Embodiment 2]

除了將實施例1的30℃、360小時的熟成處理改變為60℃、加熱處理80小時以外,係以與實施例1同樣的方式進行。由於不進行熟成處理就進行加熱處理,因此在生產步驟中浮垢的產生量較多。將所得到的聚酯纖維及處理繩的物性、及接著評估結果一併揭示於表1及表2。 The same procedure as in Example 1 was carried out except that the aging treatment at 30 ° C and 360 hours of Example 1 was changed to 60 ° C and heat treatment was carried out for 80 hours. Since the heat treatment is performed without performing the aging treatment, the amount of scum generated in the production step is large. The physical properties of the obtained polyester fiber and treated cord, and the results of subsequent evaluation are shown in Tables 1 and 2.

[實施例3] [Example 3]

除了將實施例1之紡絲速度定為2800m/分鐘~3200m/分鐘,為了調和物性,將單絲數由384改變為500,並調整延伸倍率以外,係以與實施例1同樣的方式進行,得到最終纖度相同為1130dtex、固有黏度為0.91之聚酯纖維,以及將其撚絲而得的處理繩。將所得到的聚酯纖維及處理繩之物性、接著評估結果揭示於表3及表4。 The spinning speed of Example 1 was set to 2800 m/min to 3200 m/min, and in order to adjust the physical properties, the number of filaments was changed from 384 to 500, and the stretching ratio was adjusted, and the same procedure as in Example 1 was carried out. A polyester fiber having a final fineness of 1130 dtex and an intrinsic viscosity of 0.91 and a treated cord obtained by twisting it were obtained. The physical properties of the obtained polyester fiber and treated rope, and the results of the evaluation are shown in Tables 3 and 4.

[實施例4] [Example 4]

將實施例1的紡絲速度定為2500m/分鐘,為了調和物性,而將單絲數定為384~249,並調整延伸倍率以外,係以與實施例1同樣的方式進行,而得到最終纖度相同為1130dtex、固有黏度為0.91之聚酯纖維,以及將其撚絲而得的處理繩。將所得到的聚酯纖維及處理繩之物性、接著評估結果一併揭示於表3及表4。 The spinning speed of Example 1 was set to 2,500 m/min, and in order to adjust the physical properties, the number of filaments was set to 384 to 249, and the stretching ratio was adjusted, and the final fineness was obtained in the same manner as in Example 1. The same polyester fiber of 1130 dtex and intrinsic viscosity of 0.91, and a treated rope obtained by twisting it. The physical properties of the obtained polyester fiber and the treated rope and the results of the evaluation are collectively shown in Tables 3 and 4.

[比較例3] [Comparative Example 3]

與實施例1有所不同,除了不採用環氧化合物,並且使用將胺成分由紡絲油劑去除的非胺系的紡絲油劑以外,係以與實施例1同樣的方式進行。將所得到的聚酯纖維及處理繩之物性及接著評估結果一併揭示於表3及表4。不但在動態疲勞後的接著性(擦鞋測定)之中為不良,而橡膠中的耐熱強度維持率也降低。 In the same manner as in Example 1, except that the epoxy compound was not used and the non-amine-based spinning oil agent which removed the amine component by the spinning oil agent was used. The physical properties of the obtained polyester fiber and treated rope and the results of subsequent evaluation are shown in Tables 3 and 4. Not only is it poor in the adhesion after the dynamic fatigue (shoe-shoe measurement), but the heat-resistant strength retention rate in the rubber is also lowered.

[比較例4] [Comparative Example 4]

使用固有黏度(以35℃鄰氯酚溶劑作測定)1.03,末端羧基量為20當量/ton,末端甲基量為0當量/ton的聚對苯二甲酸乙二酯碎片,以紡絲拉伸60的條件藉由熔融紡絲法得到250單絲之聚酯纖維。 A polyethylene terephthalate chip having an intrinsic viscosity (measured by an o-chlorophenol solvent at 35 ° C) of 1.03, a terminal carboxyl group of 20 equivalents/ton, and a terminal methyl group of 0 equivalent/ton was used for spinning and drawing. The condition of 60 was obtained by melt spinning to obtain 250 monofilament polyester fibers.

在由金屬紡嘴紡出並以600m/分鐘抽取的未延伸絲添加上述方法藉由所調製出的紡絲油劑,使其成為相對於纖維100份而言油劑附著成分0.4份(脂肪族胺化合物成分附著量0.048重量%)之後,在100℃的第1輥筒進行抽取 ,在第1輥筒與120℃的第2輥筒之間,進行第1段延伸成3.0倍,進一步在第2輥筒與190℃的第3輥筒之間,進行第2段延伸至合計延伸倍率成為5.0倍,接下來,在第3輥筒與第4輥筒之間進行延伸倍率0.97倍的延伸之後,藉由輥筒式油劑添加法添加由上述方法調製成的完工油劑,使其成為相對於纖維100份而言油劑附著成分為0.2重量份(環氧化合物成分附著量0.12重量%),在第4輥筒與纏繞機之間,藉由交絡(IL)噴嘴賦予交絡之後,以3400m/分鐘的速度纏繞各10kg。此外,上述以外的條件係與實施例1同樣。低速紡絲,浮垢的發生量為低水準的狀態。 Adding the above-mentioned method to the unstretched yarn spun from a metal spout and extracting at 600 m/min, by using the prepared spinning oil agent, it becomes 0.4 parts of the oil adhering component with respect to 100 parts of the fiber (aliphatic After the amount of the amine compound component adhered to 0.048% by weight, the first roll was taken at 100 ° C. The first stage is extended to 3.0 times between the first roll and the second roll of 120 ° C, and the second stage is extended to the total between the second roll and the third roll of 190 ° C. The stretching ratio is 5.0 times. Then, after extending the stretching ratio of 0.97 times between the third roller and the fourth roller, the finishing oil prepared by the above method is added by a roller type oil addition method. The amount of the oil-binding component is 0.2 parts by weight (0.12% by weight of the epoxy compound component) with respect to 100 parts of the fiber, and the entanglement is imparted by the collateral (IL) nozzle between the fourth roller and the winding machine. Thereafter, each 10 kg was wound at a speed of 3400 m/min. Further, the conditions other than the above are the same as in the first embodiment. Low-speed spinning, the amount of scum generated is in a low level state.

所得到的纖維係具有纖度為1130dtex、固有黏度為0.91,強度為7.6cN/dtex、拉伸率為14%之力學特性,末端羧基量為22當量/ton,長週期為14nm、纖維表面末端羧基量為7當量/ton、纖維橫軸方向的結晶粒徑為35nm2,末端甲基量為0當量/ton、氧化鈦含量為0.05wt%、表面環氧基量為0.1×10-3當量/kg。將所得到的聚酯纖維及處理繩之物性與接著評估結果一併揭示於表3及表4。 The obtained fiber system had a mechanical property of a fineness of 1,130 dtex, an intrinsic viscosity of 0.91, a strength of 7.6 cN/dtex, and a tensile ratio of 14%, a terminal carboxyl group amount of 22 equivalent/ton, a long period of 14 nm, and a fiber surface terminal carboxyl group. The amount is 7 equivalents/ton, the crystal grain size in the transverse direction of the fiber is 35 nm 2 , the terminal methyl group amount is 0 equivalent/ton, the titanium oxide content is 0.05 wt%, and the surface epoxy group amount is 0.1 × 10 -3 equivalent / Kg. The physical properties of the obtained polyester fiber and treated rope are shown in Tables 3 and 4 together with the results of subsequent evaluation.

與實施例3相比,此比較例4的長週期高達14nm、拉伸強度並未觀察到差異,儘管如此,乾熱收縮率或中間荷重拉伸率也很大,只有初期接著力為同等,但是在橡膠中耐熱協力維持率或動態疲勞後之接著性(擦鞋測定)之中明顯為不良。 Compared with Example 3, the long period of this Comparative Example 4 was as high as 14 nm, and no difference was observed in the tensile strength. However, the dry heat shrinkage ratio or the intermediate load stretch ratio was also large, and only the initial adhesion force was equal. However, it is clearly poor in the heat-resistant synergy retention rate in the rubber or the adhesion after the dynamic fatigue (shoe-shoe measurement).

[實施例5] [Example 5]

對實施例1所得到的聚酯纖維實施470次/m的下撚之後,將其2根合併並實施470次/m的上撚而得到繩,對此繩使用間苯二酚-福馬林-乳膠接著液(RFL液)進行接著處理,並在240℃下進行收縮熱處理2分鐘,而製成處理繩。 After the polyester fiber obtained in Example 1 was subjected to squatting at 470 times/m, two of the polyester fibers were combined and subjected to a 470 times/m upper sputum to obtain a rope, and resorcinol-formalin was used for the rope. The latex binder (RFL solution) was subjected to subsequent treatment, and subjected to shrink heat treatment at 240 ° C for 2 minutes to prepare a treated rope.

使由所得到的聚酯纖維所構成之繩使用未加硫橡膠成形為軟管,接下來在153℃下蒸氣加硫35分鐘,得到橡膠軟管。將所得到的橡膠軟管的疲勞性評估的結果揭示於 表5。 The cord composed of the obtained polyester fiber was molded into a hose using unvulcanized rubber, and then vulcanized by steam at 153 ° C for 35 minutes to obtain a rubber hose. Revealing the results of the fatigue evaluation of the obtained rubber hose table 5.

[比較例5] [Comparative Example 5]

除了使用比較例1之纖維代替實施例1所得到的纖維以外,係以與實施例4同樣的方式製成橡膠軟管,並且評估性能。將結果一併記載於表5。 A rubber hose was prepared in the same manner as in Example 4 except that the fiber of Comparative Example 1 was used instead of the fiber obtained in Example 1, and the properties were evaluated. The results are collectively shown in Table 5.

[實施例6] [Embodiment 6]

使用實施例1所得到的聚酯纖維,以下撚數200T/m、上撚數120T/m進行撚絲,而得到1100dtex/2/3之繩(輸送帶補強用纖維材料)。使作為接著處理劑的環氧/異氰酸酯附著在此繩後,在160℃實施熱處理60秒鐘,在245℃實施熱處理80秒鐘,進一步使RFL(間苯二酚.福馬林.乳膠)附著在此繩,在160℃實施熱處理60秒鐘,在235℃實施熱處理60秒鐘。使用所得到的繩作為芯線,而製作 出V型輸送帶1。將所得到的V型輸送帶之輸送帶張力維持率、輸送帶尺寸變化率、擦鞋測定的結果彙整揭示於表6。 Using the polyester fiber obtained in Example 1, the following yarns were obtained by twisting 200 T/m and having a number of turns of 120 T/m to obtain a rope of 1100 dtex/2/3 (fiber material for belt reinforcement). After attaching the epoxy/isocyanate as a treatment agent to the rope, heat treatment was performed at 160 ° C for 60 seconds, and heat treatment was performed at 245 ° C for 80 seconds to further attach RFL (resorcinol. Formalin. Latex). This rope was heat-treated at 160 ° C for 60 seconds, and heat-treated at 235 ° C for 60 seconds. Using the obtained rope as a core wire, and making The V-shaped conveyor belt 1 is taken out. The conveyance belt tension maintenance ratio of the obtained V-shaped conveyor belt, the conveyor belt dimensional change rate, and the result of the shoe-shoe measurement are summarized in Table 6.

[實施例7、8、比較例6~9] [Examples 7, 8, and Comparative Examples 6 to 9]

除了使用實施例3、4、比較例1~4之纖維代替實施例1所得到的纖維以外,係以與實施例6同樣的方式製成V型輸送帶,並且評估性能。將結果表一併記載於6、7。 A V-shaped conveyor belt was produced in the same manner as in Example 6 except that the fibers of Examples 3 and 4 and Comparative Examples 1 to 4 were used instead of the fibers obtained in Example 1, and the properties were evaluated. The results are shown together in Figures 6 and 7.

[實施例9] [Embodiment 9]

將實施例1所得到的纖維浸漬於間苯二酚.福馬林.乳膠系黏著劑,使其在175℃的氣體環境下乾燥1分鐘之後,在230℃的氣體環境下熱處理2分鐘。將這種方式所得到的接著處理聚酯纖維藉由切割刀切斷,得到纖維長為3.0mm的聚酯短纖維。 The fiber obtained in Example 1 was immersed in resorcinol. Fomalin. The latex-based adhesive was dried in a gas atmosphere at 175 ° C for 1 minute, and then heat-treated in a gas atmosphere at 230 ° C for 2 minutes. The subsequently treated polyester fiber obtained in this manner was cut by a cutter to obtain a polyester staple fiber having a fiber length of 3.0 mm.

將此橡膠補強用聚酯短纖維,以5容量%摻合至以天然橡膠、苯乙烯丁二烯為主成分的未加硫橡膠中,使用MS式加壓捏合機(DS3-10MHHS,森山製作所股份有限公 司製)混練3分鐘。以適當的厚度進行薄片壓延而使短纖維配向,藉由壓延加硫製作出橡膠薄片,並在短纖維的配向方向切出樣品,而製成短纖維補強橡膠成形品,並且評估性能。 The polyester reinforcing short fiber was blended into an unvulcanized rubber containing natural rubber and styrene butadiene as a main component, and a MS type pressure kneader (DS3-10MHHS, Moriyama Manufacturing Co., Ltd.) was used. Limited company System) mixed for 3 minutes. The sheet was calendered at an appropriate thickness to align the staple fibers, and a rubber sheet was produced by calendering and vulcanization, and a sample was cut out in the direction of the alignment of the short fibers to prepare a short fiber-reinforced rubber molded article, and the properties were evaluated.

結果如表8所示,降伏點拉伸強度=14.0kg/cm2、彎曲疲勞壽命=16.0萬次,而且補強性、耐疲勞性皆可得到優異的效果。 As a result, as shown in Table 8, the tensile strength at the point of depression was 14.0 kg/cm 2 and the bending fatigue life was 166,000 times, and excellent effects were obtained in both the reinforcing property and the fatigue resistance.

[實施例10、11、比較例10~13] [Examples 10 and 11, Comparative Examples 10 to 13]

除了使用實施例3、4、比較例1~4之纖維代替實施例1所得到的纖維以外,係以與實施例9同樣的方式製成短纖維補強橡膠成形品,並且評估性能。將結果一併記載於表8、9。 A short fiber reinforced rubber molded article was produced in the same manner as in Example 9 except that the fibers of Examples 3 and 4 and Comparative Examples 1 to 4 were used instead of the fibers obtained in Example 1, and the properties were evaluated. The results are shown together in Tables 8 and 9.

1‧‧‧V型輸送帶 1‧‧‧V belt

2‧‧‧附橡膠的布 2‧‧‧With rubber cloth

3‧‧‧芯線 3‧‧‧core

4‧‧‧接著橡膠層 4‧‧‧Next rubber layer

5‧‧‧壓縮橡膠層 5‧‧‧Compressed rubber layer

6‧‧‧短纖維 6‧‧‧ Short fiber

7‧‧‧肋條 7‧‧‧ Ribs

8‧‧‧肋條型V型輸送帶 8‧‧‧ Rib type V conveyor belt

圖1係表示使用本發明之繩作為芯線的輸送帶的其中一個實施形態之剖面圖。 BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a cross-sectional view showing one embodiment of a conveyor belt using a cord of the present invention as a core.

圖2係表示使用本發明之繩作為芯線的輸送帶的其他例子之剖面圖。 Fig. 2 is a cross-sectional view showing another example of a conveyor belt using the cord of the present invention as a core.

1‧‧‧V型輸送帶 1‧‧‧V belt

2‧‧‧附橡膠的布 2‧‧‧With rubber cloth

3‧‧‧芯線 3‧‧‧core

4‧‧‧接著橡膠層 4‧‧‧Next rubber layer

5‧‧‧壓縮橡膠層 5‧‧‧Compressed rubber layer

6‧‧‧短纖維 6‧‧‧ Short fiber

Claims (10)

一種橡膠補強用聚酯纖維,其特徵為:由以對苯二甲酸乙二酯為主要重覆單元之固有黏度為0.85以上的聚酯所構成之纖維,並且纖維中之末端羧基量係20當量/ton以上,藉由X射線小角繞射測得的長週期係9~12nm,且在纖維表面附著有具有環氧基的表面處理劑。 A polyester reinforcing polyester fiber characterized by comprising a polyester composed of polyester having an intrinsic viscosity of 0.85 or more with ethylene terephthalate as a main repeating unit, and the amount of terminal carboxyl groups in the fiber is 20 equivalents. Above /ton, the long-period system measured by X-ray small angle diffraction is 9 to 12 nm, and a surface treatment agent having an epoxy group is attached to the surface of the fiber. 如申請專利範圍第1項之橡膠補強用聚酯纖維,其中纖維表面之末端羧基量係10當量/ton以下。 The polyester fiber for rubber reinforcement according to the first aspect of the invention, wherein the amount of terminal carboxyl groups on the surface of the fiber is 10 equivalents/ton or less. 如申請專利範圍第1項之橡膠補強用聚酯纖維,其中纖維橫軸方向的結晶尺寸係35~80nm2The polyester fiber for rubber reinforcement according to the first aspect of the patent application, wherein the crystal size in the transverse direction of the fiber is 35 to 80 nm 2 . 如申請專利範圍第1項之橡膠補強用聚酯纖維,其中纖維中之末端甲基量係2當量/ton以下。 The polyester fiber for rubber reinforcement according to the first aspect of the patent application, wherein the terminal methyl group in the fiber is 2 equivalent/ton or less. 如申請專利範圍第1項之橡膠補強用聚酯纖維,其中纖維中之氧化鈦含量係0.05~3重量%。 The polyester fiber for rubber reinforcement according to the first aspect of the patent application, wherein the content of the titanium oxide in the fiber is 0.05 to 3% by weight. 如申請專利範圍第1項之橡膠補強用聚酯纖維,其中纖維表面之環氧指數係1.0×10-3當量/kg以下。 The polyester fiber for rubber reinforcement according to the first aspect of the patent application, wherein the epoxy index of the fiber surface is 1.0 × 10 -3 equivalent / kg or less. 一種聚酯纖維之製造方法,其特徵為:將固有黏度為0.9以上且末端羧基量為15當量/ton以上的聚對苯二甲酸乙二酯聚合物熔融擠出,在添加含有環氧硬化觸媒的紡絲油劑之後,以2000~6000m/分鐘之速度抽取,接下來進行延伸,然後添加含有環氧化合物的整理油劑,而進行熟成處理。 A method for producing a polyester fiber, characterized in that a polyethylene terephthalate polymer having an intrinsic viscosity of 0.9 or more and a terminal carboxyl group content of 15 equivalent/ton or more is melt-extruded, and an epoxy hardening contact is added thereto. After the spinning oil of the medium, the mixture is drawn at a speed of 2000 to 6000 m/min, and then extended, and then a finishing oil containing an epoxy compound is added to perform a ripening treatment. 如申請專利範圍第7項之聚酯纖維之製造方法,其中熟成處理溫度係在20~50℃的範圍。 The method for producing a polyester fiber according to claim 7, wherein the ripening treatment temperature is in the range of 20 to 50 °C. 如申請專利範圍第7項之聚酯纖維之製造方法,其中熟成處理時間係50小時以上。 The method for producing a polyester fiber according to claim 7, wherein the ripening treatment time is 50 hours or longer. 如申請專利範圍第7項之聚酯纖維之製造方法,其中環氧硬化觸媒係胺化合物。 A method for producing a polyester fiber according to claim 7, wherein the epoxy hardening catalyst is an amine compound.
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