TW200934897A - Conjugate fiber having low-temperature processability, nonwoven fabric and formed article using the conjugate fiber - Google Patents

Conjugate fiber having low-temperature processability, nonwoven fabric and formed article using the conjugate fiber Download PDF

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Publication number
TW200934897A
TW200934897A TW97148048A TW97148048A TW200934897A TW 200934897 A TW200934897 A TW 200934897A TW 97148048 A TW97148048 A TW 97148048A TW 97148048 A TW97148048 A TW 97148048A TW 200934897 A TW200934897 A TW 200934897A
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Taiwan
Prior art keywords
fiber
component
ethylene
woven fabric
composite
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TW97148048A
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Chinese (zh)
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TWI367967B (en
Inventor
Masahito Katsuya
Toshikatsu Fujiwara
Hirokazu Terada
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Es Fiber Visions Co Ltd
Es Fiber Visions Hong Kong Ltd
Es Fiber Visions Lp
Es Fiber Visions Aps
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    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/28Formation of filaments, threads, or the like while mixing different spinning solutions or melts during the spinning operation; Spinnerette packs therefor
    • D01D5/30Conjugate filaments; Spinnerette packs therefor
    • 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
    • D01F8/00Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
    • D01F8/04Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers
    • D01F8/06Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyolefin as constituent
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D10/00Physical treatment of artificial filaments or the like during manufacture, i.e. during a continuous production process before the filaments have been collected
    • D01D10/02Heat treatment
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D10/00Physical treatment of artificial filaments or the like during manufacture, i.e. during a continuous production process before the filaments have been collected
    • D01D10/04Supporting filaments or the like during their treatment
    • D01D10/049Supporting filaments or the like during their treatment as staple fibres
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D10/00Physical treatment of artificial filaments or the like during manufacture, i.e. during a continuous production process before the filaments have been collected
    • D01D10/06Washing or drying
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/28Formation of filaments, threads, or the like while mixing different spinning solutions or melts during the spinning operation; Spinnerette packs therefor
    • D01D5/30Conjugate filaments; Spinnerette packs therefor
    • D01D5/32Side-by-side structure; Spinnerette packs therefor
    • DTEXTILES; PAPER
    • D02YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02GCRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
    • D02G3/00Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
    • D02G3/02Yarns or threads characterised by the material or by the materials from which they are made
    • DTEXTILES; PAPER
    • D02YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02GCRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
    • D02G3/00Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
    • D02G3/44Yarns or threads characterised by the purpose for which they are designed
    • D02G3/443Heat-resistant, fireproof or flame-retardant yarns or threads
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H1/00Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/54Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties by welding together the fibres, e.g. by partially melting or dissolving
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H1/00Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/54Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties by welding together the fibres, e.g. by partially melting or dissolving
    • D04H1/541Composite fibres, e.g. sheath-core, sea-island or side-by-side; Mixed fibres
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H13/00Other non-woven fabrics
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2321/00Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D10B2321/02Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds polyolefins
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2401/00Physical properties
    • D10B2401/04Heat-responsive characteristics
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/29Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
    • Y10T428/2913Rod, strand, filament or fiber
    • Y10T428/2929Bicomponent, conjugate, composite or collateral fibers or filaments [i.e., coextruded sheath-core or side-by-side type]
    • Y10T428/2931Fibers or filaments nonconcentric [e.g., side-by-side or eccentric, etc.]
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T442/00Fabric [woven, knitted, or nonwoven textile or cloth, etc.]
    • Y10T442/60Nonwoven fabric [i.e., nonwoven strand or fiber material]
    • Y10T442/608Including strand or fiber material which is of specific structural definition

Abstract

A conjugate fiber having low-temperature processability, and the shrink is restrained, and having excellent thermal adhesive, and the processability of the card-passing ability is excellent when processing the fiber to a nonwoven fabric, and the nonwoven fabric having excellent texture can be obtained fluffy. And this invention provides a nonwoven fabric and a formed article having excellent low-temperature processability, fluffiness and texture. A conjugate fiber is formed as a side-by-side type cross section by a first component including at least 75 wt% of an ethylene. α -olefin of melting point of 70 to 100 DEG C, and a second component including crystalline poly propylene, characterized in that: in the cross section of fiber perpendicular to a axis of fiber, the 55 to 90% of outer circumference of fiber is occupied by the first component, a borderline of the first and second component is a curve projecting toward the first component, and an area ratio of first and second component (first component/second component) is at a range of 70/30 to 30/70. A nonwoven fabric is obtained by nonwoven fabric forming process using the conjugate fiber. A formed article is obtained by using the conjugate fiber.

Description

200934897200934897

/ ^pn.uuC 六、發明說明: 【發明所屬之技術領域】 本發明是關於一種具有熱加工時之低溫加工性、且抑 制收縮而具有良好的熱黏接性的複合纖維。另外,本發明 是關於一種使用該複合纖維的蓬鬆性與質感優異的不織布 及成形體。 【先前技術】 〇 自先前以來,提出有各種具有低溫加工性的複合纖 維’一直使用容易調整炫點的乙烯.心婦烴共聚物來作為 構成複合纖維的成分。例如,提出有鞘芯 型 合纖維,其是使用具有90〜125ΐ的低熔點的聚乙烯系樹 脂與具有的高㈣的聚乙烯系麵的「混合 物」來作為複合成分的一種成分(例如,彖昭利文獻i)。 =’提出有潛在捲縮性複合纖維,其是^含有乙稀.α_ 共聚物的成分與含有聚酯樹脂的成分「分別」用作複 ❹ 種f分(例如’參照專利文獻2)。 .、、丨而,先則的具有低溫加工性的複合纖維在實用上尚 ίί—步改善的餘地。例如,專利文獻1中所提出的複合 m、雖然使用具有90〜125°c的低、熔點的聚乙烯系樹 :為了生產穩定性,而實質上於大於等於30 wt°/〇 (重 5 =比)的範圍内「混合」具有120〜135。⑽高熔點的 :、系樹脂’來料複合纖賴-種成分,因此有損低 二一=11 ’而並不充分滿足要求。另外,專利文獻2是關 ;利用以乙烯· 烯烴共聚物為成分的複合纖維在熱 4 200934897 處理時容易收縮的性質的潛在捲縮 在捲縮性的複合纖維並不適於獲得&到2 ’值此種潛 好的不織布。 勾抑制的質地良 另外,此種具有潛在捲縮 ❹ ❹ 其之多種成分間的收縮性的差異,在此用了構成 後容易產生剝離,在加工為不織布時,若於熱處理 性成分與不㈣的其他成分纽_,則於的黏接 近使由黏接性成分形成的纖維與 t t,接 不良情況。因此料會產生無法魏顿布的強度的 如此b 7為止作為具有低 ,魏^ ::良於低温加工性或不織布_或強;== 【【=:;公開第00/36200號小科 【發明ί容】 日本專利特開雇-2迎1號公報 本發2的目的在於提供—種複 工性,且收縮得到抑制,目士 ή 、,低概加 工為不織布時的尤其是進好的熱黏接性,而且在加 過性優異,可獲得蓬髮且加工的情況下’其梳棉通 的還在於提供—種地良好的不織布。本發明的目 織布及成频。 加碍優異、賴且㈣良好的不 本發月者進仃銳意研究的結果發現,藉由構成特定的 5 200934897[Technical Field of the Invention] The present invention relates to a composite fiber which has low-temperature workability at the time of hot working and which suppresses shrinkage and has good thermal adhesion. Further, the present invention relates to a nonwoven fabric and a molded body which are excellent in bulkiness and texture using the conjugate fiber. [Prior Art] Since the prior art, various types of composite fibers having low-temperature workability have been proposed, and ethylene-hipon hydrocarbon copolymers which are easy to adjust the glare have been used as components constituting the composite fibers. For example, a sheath core type fiber is used, which is a "mixture" of a polyethylene-based resin having a low melting point of 90 to 125 Å and a high (four) polyethylene-based surface as a component of a composite component (for example, 彖Zhaoli literature i). = 'There is a latent crimping conjugate fiber which is used as a conjugate of the component containing the ethylene-α-copolymer and the component containing the polyester resin, respectively (for example, refer to Patent Document 2). . . . , 丨 , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , For example, the composite m proposed in Patent Document 1 uses a polyethylene tree having a low melting point of 90 to 125 ° C: substantially 30 Å / 〇 or more for weight stability (weight 5 = "Mixed" in the range of ratio) has 120 to 135. (10) The high melting point: the resin is used to feed the composite fiber-based component, so that it is less than 21% and does not sufficiently satisfy the requirements. Further, Patent Document 2 is closed; the use of a composite fiber comprising an ethylene·olefin copolymer as a component in the heat 4 200934897 is likely to shrink during the shrinkage of the composite fiber in the crimped composite fiber is not suitable for obtaining & Value this kind of potential non-woven fabric. The texture of the hook suppression is good. In addition, the difference in shrinkage between the various components of the potential crimping crucible is likely to cause peeling after the composition is used. When the processing is non-woven, the heat-treating component is not (4). The other component, New Zealand, is close to the adhesion of the fiber formed by the adhesive component to the tt. Therefore, it is expected that the strength of the Weidun cloth will not be as high as B, so that it is low, Wei ^ :: good for low temperature processing or non-woven _ or strong; == [[=:; public 00/36200 No. Japanese Patent Application No. 2 No. 1 No. 1 The purpose of the present invention is to provide a kind of reworkability, and the shrinkage is suppressed, and the appearance is low, and the processing is low, especially when it is not woven. The heat-adhesive property, and in the case where the addition property is excellent, and the hair can be obtained and processed, the carding pass is also to provide a good non-woven fabric. The woven fabric of the present invention and the frequency of formation. The result of intensive research, and (4) good non-performed people who have made in-depth research have found that by constructing a specific 5 200934897

f ^pn.uuC 並列型截面的複合纖維可達成上述課題’該複合纖維中, 有利於複合纖維的低溫加工性的成分即熱處理時主要軟 化、熔融的熔點更低的成分是形成為含有大於等於特定量 的特定乙烯.烯烴共聚物的成分,將其作為第〗成分, 並且將含有結晶性聚丙烯的成分作為第2成分。 ❹ ❹ 因此,本發明是一種複合纖維,其是由含有至少75 wt°/〇的溶點為7〇〜議。c的乙烯·α_烯烴共聚物的第1成 分、與含有結晶性聚丙稀的第2成分構成並列型截面而 成,該複合纖維的特徵在於:在與纖維車由(fiber狀 直角的纖維截面中,第1成分占纖維外周的55〜90%,第 第2成分的邊界線描向第1成分侧彎曲為凸 ==第1成分與第2成分的面積比率(第!成分/ 弟乂成分)為70/30〜30/70的範圍。 於本發明的實施態樣中,所使用 物,可八n \ 7便用之乙烯烯烴共聚 物了舉出子量分佈(斷聽)^. 〜0.91 g/cm3,並且基於ASTMD] :5在度為?.87 #^ίγΑ?ι ο χταα 且於/V 度為 190 C、 MI) ^ 35 ^ M)為10〜35g/1〇min的乙婦·心歸煙 上述複合纖維於l〇〇°c下進彳 w 出小於等於5G%的熱收縮率^卩5讀熱處理後可顯示 可對本發明的複合纖維進行 織布,另和可對本發明的複合纖維化處奸製造不 發明的複合纖維所獲得的不織布進^仃加工’或對由本 體。 浥仃加工,而製作出成形 6 200934897 π磁;Γ此本發明亦進步針對—種對上述複合纖維進行 ^布化處理所獲得的不織布、使用上述複合纖維所獲得 、形體、及使用上述不織布所獲得的成形體。 接法5述不織布化處理的例子可舉出減黏接法、熱水黏 [發明效果] 〜1〇〇本γ!ΓΛ複合纖維是將含有至少75 wt%的溶點為70 100C的乙烯·α•稀烴共聚物的成分作為第1成分且呈 ΐ如===型截面:在與纖維轴成直角的纖維截面 '該第1成w纖維外周的55〜9G%,該第i成分 成分的邊界線描緣出向第i成分側f曲為凸狀的曲^, 為,第1成分與第2成分的面積比率(第1成分/第2成分) ‘ 0^30、〜30/70的範圍。因含有該乙烯.心稀烴共聚物的 虛成为主要覆蓋纖維表面,故於loot:或loot:以下的熱 =度好的熱黏接性,,具有良好的低;盈 卜因含有結晶性聚丙烯的第2成分露出於· 面=面的-部分’故可降低乙稀· α_烯煙共聚物特有的表 摩擦的局度’不添加潤滑劑等或少量添加潤滑劑, 中的穩定生產’尤其是在進行梳棉加工 令該W棉步驟中的纖維通過性變得良好。 中,形狀的一般的二成分並列型戴面形狀 是以==之虞。本發明的複合纖維的並列型戴面 下方式構成,即,含有乙烯.α,烴共聚 軏占周面長度的55〜·,該第丨成分與第 7 200934897f ^pn.uuC The composite fiber of the parallel cross-section can achieve the above-mentioned problem. In the composite fiber, a component which is advantageous for the low-temperature workability of the conjugate fiber, that is, a component which is mainly softened during heat treatment and has a lower melting point after melting is formed to have a ratio of greater than or equal to A component of a specific amount of the specific ethylene-olefin copolymer is used as a component, and a component containing a crystalline polypropylene is used as a second component. ❹ ❹ Therefore, the present invention is a composite fiber which is composed of a melting point containing at least 75 wt/min. The first component of the ethylene/α-olefin copolymer of c and the second component containing the crystalline polypropylene are formed into a side-by-side cross section, and the conjugate fiber is characterized in that it is a fiber cross section of a fiber-shaped right angle. In the middle, the first component accounts for 55 to 90% of the outer circumference of the fiber, and the boundary line of the second component is curved toward the first component side to be convex == the area ratio of the first component to the second component (the first component / the younger component) It is in the range of 70/30 to 30/70. In the embodiment of the present invention, the amount of the ethylene olefin copolymer used in the invention can be exemplified by a sub-quantity distribution (interruption) ^. g/cm3, and based on ASTM D]: 5 in the degree of ?.87 #^ίγΑ?ι ο χταα and /V degree is 190 C, MI) ^ 35 ^ M) is 10~35g/1〇min of the woman · 心 归 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述The composite fiber is sterilized to produce a non-woven fabric obtained by a composite fiber which is not invented, or a pair of bodies.浥仃Processing, and forming the forming 6 200934897 π magnetic; 本 本 本 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 2009 The obtained shaped body. 5. The example of the non-woven treatment of the fifth method is a reduction bonding method or a hot water adhesion [effect of the invention] ~1 〇〇 γ ΓΛ ΓΛ composite fiber is an ethylene containing at least 75 wt% of a melting point of 70 100 C· The component of the α•dilute hydrocarbon copolymer is a first component and has a cross section such as ===: a fiber cross section at right angles to the fiber axis, and 55 to 9 G% of the outer circumference of the first w fiber, the i component component The boundary line of the boundary line is curved to the i-th component side, and the area ratio of the first component to the second component (the first component/the second component) is a range of '0^30, 〜30/70. . Since the virginity of the ethylene-containing dilute hydrocarbon copolymer mainly covers the surface of the fiber, the thermal adhesiveness with good heat=degree under the loot: or loot: has a good low; the blister contains a crystalline poly The second component of propylene is exposed to the surface of the surface of the surface of the surface of the surface of the surface of the surface of the surface of the surface of the surface of the surface of the surface of the surface of the surface of the surface of the surface of the surface of the surface of the surface of the surface of the surface of the surface. 'In particular, the carding process makes the fiber passability in the W cotton step good. In the shape of the general two-component side-by-side type, the shape is =. The conjugate fiber of the present invention is constituted by a side-by-side type, that is, a mixture comprising ethylene.α, a hydrocarbon copolymerized yttrium having a circumferential length of 55 〜·, the 丨 component and the seventh 200934897

J\JjL /^pii.uuC 界線描繪出向第1成分侧彎曲為凸狀的曲線,且該第 分與第2成分的面積比率(第!成分/第2成分)為7〇= 〜30/70的範圍’因此不易弓丨起成分關離,尤其是在進 行梳棉加工時,不會妨礙梳棉步驟中的纖維通過性或加工 為不織布後的不織布強度,而發揮較好的作業性。另外, 組合有半月形狀的-般的二成分並列型的截面形狀中,存 在容易引絲處理所導致的收縮的方面,但—般認為,本 發明的複合纖維藉由轉定的乙烯.α__共聚物作為第 1成分,且採用特㈣纖維截面形狀,而有效地抑制收縮。 使用本發明的複合纖維所得的不織布蓬鬆且柔軟,教 處理時的收縮少,因此幾乎沒有縮幅(寬度相對於不織;^ 的加工方向的減少)’生產性、f地良好。另外,本發明的 複合纖維由於是以含魏點為7G〜胸。C的乙稀.心稀煙 共聚物的齡作為有效齡,故可騎⑽。以湖。C以下 的熱處理加工。因此,本發明的複合纖維的不織布化或成 开ί加工時亦可使用蒸氣或熱水等媒體,故可根據用途、 環境、、狀況’自範隨相選項帽擇合適料織布化條 件或成形加工條件。 為讓本發明之上述特徵和優點能更明顯易懂,下文特 舉實施例,並配合所賴式作詳細說明如下。 【實施方式】 八你f =合纖維是以含有乙婦·α,烴共聚物的成 1 '、、、刀。所谓該乙烯·α-烯烴共聚物,是指由乙 婦及α稀烴卿成者,,频而言可舉出: 8 200934897 丙烯、丁烯q、戊烯、己烯d、 心烯烴。該些㈣烴之中,較好η辛;^等直鏈狀 ㈣是他。乙稀讀 η專於30mol%(莫耳百分比),更好的是::二 旦Γΐα 1烴含量通常為大於等於lmol%。此時的含 里疋才曰((α-婦烴)/( α_婦烴+乙稀) 3 ❹ ο =二量二多,則存在於纖維製造靖固化ί慢: 5起纖等而有損生產性的傾向。若^ 夂 30 «以内,則纖維的剛性充分 二】置為 時’梳棉步驟中的纖維通過性良好。尤其疋進仃梳棉加工 所使用的乙烯·α-稀烴共聚物的溶點為^ 較好的是80〜觸。c。藉由耽或啊以上的溶點 止纖維間料等,例如於纖轉造步财使塗佈於纖維 面的抗靜電劑等處理劑乾燥時,不㈣起纖維間炫著^The J\JjL /^pii.uuC boundary is a curve in which the first component side is curved to be convex, and the area ratio (the first component/second component) of the first component and the second component is 7〇= 〜30/70. The range 'is therefore difficult to remove the components, especially when the carding process is performed, the fiber passability in the carding step or the non-woven strength after the non-woven fabric is not hindered, and the workability is improved. Further, in the cross-sectional shape of the two-component side-by-side type in which the half-moon shape is combined, there is a tendency that shrinkage due to the wire drawing process is easy, but it is generally considered that the composite fiber of the present invention is converted by ethylene. α__ The copolymer is used as the first component, and the cross-sectional shape of the special (four) fiber is used to effectively suppress shrinkage. The non-woven fabric obtained by using the conjugate fiber of the present invention is bulky and soft, and has little shrinkage during the teaching. Therefore, there is almost no shrinkage (a reduction in the width of the machined surface with respect to the woven fabric), and productivity is good. Further, the composite fiber of the present invention has a Wei-containing point of 7 G to chest. Ethylene of C. Heart-thin smoke The age of the copolymer is as effective as it can be used (10). Take the lake. Heat treatment below C. Therefore, when the conjugate fiber of the present invention is not woven or processed, a medium such as steam or hot water can be used, so that the woven fabric can be selected according to the use, the environment, and the condition. Forming processing conditions. The above described features and advantages of the present invention will become more apparent and understood. [Embodiment] Eight you f = a fiber is a 1 ', , and a knife containing a polyethylene-α, a hydrocarbon copolymer. The ethylene·α-olefin copolymer is a compound derived from a mother or an alpha-dilute hydrocarbon, and the frequency thereof is as follows: 8 200934897 Propylene, butene q, pentene, hexene d, and heart olefin. Among these (four) hydrocarbons, it is preferred that η 辛; ^ and other linear (four) is him. The ethylene reading η is exclusively for 30 mol% (% of moles), and more preferably: the hydrocarbon content of the 二α 1 is usually 1 mol% or more. At this time, the 疋 疋 曰 ( ((α-women hydrocarbon) / ( α _ female hydrocarbon + ethylene) 3 ❹ ο = two more than two, it exists in the fiber manufacturing Jing curing ί slow: 5 fiber and so on The tendency to impair productivity. If ^ 夂 30 « inside, the rigidity of the fiber is sufficient. 2] When the fiber is in the carding step, the fiber passability is good. Especially the ethylene·α-dilute hydrocarbon used in the carding process. The melting point of the copolymer is preferably 80 to 150. The melting point of the copolymer is used to prevent the fiber material, such as an antistatic agent applied to the fiber surface. When the treatment agent is dry, it does not (four) swell between the fibers ^

,情況。’而發揮良好的生產性。另外,藉由熔點為刚。C c X下可將在將纖維加工為不織布或成形體時 加工溫度設定A loot:或川代以下,可使用蒸氣或熱水等 作為熱處理的媒體,可選擇使用溫度相對較低的媒體的加 工方法。並且,不必擔心對構成纖維的本來不熔融的其他 成分造成影響,故較好。 具他 此處所謂的熔點,是以示差掃描熱量計(differential scanning cal〇rimetry,DSC)測定乙烯,α•烯烴共聚物後 的熔融峰值溫度。當確認到多個熔融峰值時,以最大的熔 融峰值的溫度作為熔點,當確認到多個大小相近的熔融峰 200934897,Happening. And play a good productivity. In addition, the melting point is just. C c X can be used to process the fiber into a non-woven fabric or a molded body. The processing temperature is set to A loot: or below the Chuo Dynasty. Steam or hot water can be used as a medium for heat treatment, and processing with a medium having a relatively low temperature can be selected. method. Further, it is not necessary to worry about the influence of other components constituting the fibers which are not originally melted. The melting point referred to herein is the melting peak temperature of ethylene and α•olefin copolymers measured by differential scanning calorimetry (DSC). When a plurality of melting peaks are confirmed, the temperature of the maximum melting peak is taken as the melting point, and when a plurality of melting peaks having similar sizes are confirmed, 200934897

JUZ/3pil.UOC 值時’以更低側的炫融峰值溫度作為炼點。 t烯共聚物的重量平均分子量(Mw)與數 ^刀子量(Mn)的比即分子量分佈(Mw/Mn)較好 曰=h5〜2.5’更好的是L7〜2.3。若分子量分佈(Mw/Mn) 疋在,i.5〜2.5的範圍内,則可獲得纖維製造步驟中的紡絲 ϋ變得良好、纖維物性方面亦具有充分強度的複合纖維, 故較好。 φ 3乙烯.α _烯烴共聚物的密度較好的是0.87〜0.91 g/Cm3 ’特別好的是0.88〜0.90 g/cm3。若乙烯· α·稀烴共 聚物的密度大於等於〇·87 g/cm3,則將該共聚物加工為纖 維時的表面黏性為適度,纖維製造時不易引起膠著,適合 於用作纖維的主體構成成分。另一方面,若該密度為小於 等於0.91 g/cm3,則乙烯.α_稀烴共聚物的熔點相對較低, 為l〇〇°C或loot以下,適合用作本發明中使用的乙烯.α_ 稀煙共聚物。 若考慮到纖維製造步驟中的穩定生產,則乙稀· 〇^稀 〇 烴共聚物的熔融指數(ΜΙ)較好的是10〜35 g/l〇 min,更 好的是15〜30 g/10 min的範圍。此處所謂的mi,是基於 ASTMD-1238且於190°C、負荷為21.2N的條件下所測定 的值。 所使用的乙烯·α-烯烴共聚物既可為單獨一種,亦可 為兩種或兩種以上的混合物。 於本發明所使用的乙烯· α-烯烴共聚物中,可於不損 及本發明目的之範圍内調配各種添加劑。例如,潤滑劑、 200934897When the JUZ/3pil.UOC value is used, the peak temperature of the lower side is used as the refining point. The ratio of the weight average molecular weight (Mw) of the t-ene copolymer to the number of knives (Mn), that is, the molecular weight distribution (Mw/Mn) is preferably 曰 = h5 to 2.5', more preferably L7 to 2.3. When the molecular weight distribution (Mw/Mn) is in the range of i. 5 to 2.5, it is preferable to obtain a composite fiber which is excellent in the spinning enthalpy in the fiber production step and has sufficient strength in terms of fiber physical properties. The density of the φ 3 ethylene.α-olefin copolymer is preferably 0.87 to 0.91 g/cm 3 ', particularly preferably 0.88 to 0.90 g/cm 3 . When the density of the ethylene·α·dilute hydrocarbon copolymer is 大于·87 g/cm 3 or more, the surface viscosity of the copolymer when processed into a fiber is moderate, and the fiber is less likely to cause sticking during the production of the fiber, and is suitable for use as a main body of the fiber. Composition. On the other hand, if the density is 0.91 g/cm3 or less, the melting point of the ethylene.α_dilute hydrocarbon copolymer is relatively low, being 10 ° C or less, suitable for use as the ethylene used in the present invention. __ dilute smoke copolymer. The melt index (ΜΙ) of the ethylene 〇 〇 〇 〇 hydrocarbon copolymer is preferably from 10 to 35 g/l 〇 min, more preferably from 15 to 30 g/, in view of stable production in the fiber production step. 10 min range. Here, mi is a value measured based on ASTMD-1238 at 190 ° C and a load of 21.2 N. The ethylene·α-olefin copolymer to be used may be either a single one or a mixture of two or more kinds. In the ethylene·α-olefin copolymer used in the present invention, various additives can be formulated within a range not detracting from the object of the present invention. For example, Lubricant, 200934897

juz,/^pu.uuC 耐熱穩定劑、抗氧化劑、耐候穩定劑、抗靜電劑、著色劑 等。可較好地用作潤滑劑的有油酸醯胺或界酸醯胺等脂肪 酸醯胺、硬脂酸丁醋等脂肪酸醋、聚乙稀蝶或聚丙稀壤等 聚稀烴蠛、硬脂酸約等金屬息等。特別好地使用的是油酸 . _、芥酸_、硬脂酸_、二十二麵胺等脂肪酸酿 胺。 為了可於低溫下參與熱黏接,尤其是為了不織布化或 成形加工時的熱媒體可使用蒸氣或熱水,本發明的複合纖 維中的第1成分中必須包含有效量的上述乙烯·α_烯烴共 聚物。以第1成分的重量基準,該乙烯·烯烴共聚物的 含量為大於等於75%,較好的是大於等於85%,特別好的 是樹脂原料占1〇〇〇/。。若上述乙烯· α_烯烴共聚物於第1 成分中為大於等於75 wt%,則就可主要表現出乙烯.α-烯 烴共聚物的性能方面而言較好。 在上述乙烯.烯烴共聚物以第1成分的重量基準而 含有大於等於75%的條件下,除了該乙烯·α_烯烴共聚物 〇 以外’亦可包含於第1成分中的樹脂原料,例如可舉出: 低密度聚乙烯、高密度聚乙烯、乙烯-乙酸乙烯酯共聚物、 丙烯共聚物等。該些樹脂原料可利用以下方法混合:於樹 脂的狀態下預先均勻地混合的方法;或於纖維製造步驟中 使乙婦·α-烯烴共聚物溶融而擠出時,自播出機的中途的 進料口投入的方法。 本發明的複合纖維以含有結晶性聚丙烯的成分作為 第2成分。所謂該結晶性聚丙烯,是丙烯均聚物、或丙烯 200934897Juz, /^pu.uuC Heat stabilizers, antioxidants, weather stabilizers, antistatic agents, colorants, etc. It can be preferably used as a lubricant, such as fatty acid decylamine such as oleic acid amide or phthalic acid amide, fatty acid vinegar such as butyl vinegar, butyl phthalate or polyacrylonitrile, and stearic acid. About waiting for metal and so on. Very good use of oleic acid. _, erucic acid _, stearic acid _, behenylamine and other fatty acid amines. In order to participate in thermal bonding at a low temperature, in particular, steam or hot water may be used for the heat medium during the non-woven or forming process, the first component of the composite fiber of the present invention must contain an effective amount of the above ethylene·α_ Olefin copolymer. The content of the ethylene/olefin copolymer is 75% or more, preferably 85% or more, based on the weight of the first component, and particularly preferably 1% of the resin raw material. . When the ethylene/α-olefin copolymer is 75 wt% or more in the first component, it is preferable to mainly exhibit the performance of the ethylene.α-olefin copolymer. In the case where the ethylene-olefin copolymer contains 75% or more by weight based on the weight of the first component, the resin raw material which can be contained in the first component other than the ethylene/α-olefin copolymer oxime can be, for example, For example: low density polyethylene, high density polyethylene, ethylene-vinyl acetate copolymer, propylene copolymer, and the like. These resin raw materials can be mixed by the following method: a method of uniformly mixing in advance in a state of a resin; or when a polyethylene-α-olefin copolymer is melted and extruded in a fiber production step, in the middle of a self-producing machine The method of inputting the feed port. The conjugate fiber of the present invention contains a component containing crystalline polypropylene as the second component. The crystalline polypropylene is a propylene homopolymer or propylene 200934897

JUZ/^pn.UUC 與少量的(通常為小於等於2wt%的)α-烯烴的共聚物, 此種結晶性聚丙烯有使用齊格勒—納他觸媒(Ziegler_Natta catalyst)或一戊金屬觸媒(metallocene catalyst)所獲得的 通用的聚丙稀。 本發明中的結晶性聚丙烯,較好的是如下者:熔點為 150〜165°C、較好的是155〜165°C,熔體質量流動速率 (melt mass-flow rate ’ ]\«^=230。(:,21.2 N)處於 〇.1 〜 ❹ 8(^/1〇111丨11的範圍,更好的是處於3〜4〇岁1〇111丨11的範圍。 構成本發明的複合纖維的第2成分含有結晶性聚丙 烯,在不明顯有損效果的範圍内,可適宜使用丙烯.3_烯 烴共聚物的混合物、或熔體質量流動速率(MFR)或分子 量分佈(Mw/Mn)等物性不同的結晶性聚丙烯彼此的混合 物等。另外,視需要亦可調配其他熱塑性樹脂,或二氧化 鈦、碳酸鈣及氫氧化鎂等無機物,或各種添加劑(阻燃劑、 耐熱穩疋劑、抗氧化劑、耐候穩定劑、抗靜電劑、著色劑 等)。構成本發明的複合纖維的第2成分中,通常合適的是 ❹ 結晶性聚丙稀占至少7 5 wt%。 本發明的複合纖維中,含有乙烯.^_烯烴共聚物的第 1成分與含有結晶性聚丙烯的第2成分構成特定結構的並 列型截面。 在與纖維轴成直角的纖維截面中,含有乙烯.烯烴 共聚物的第1成分占纖維外周的55〜9〇%,含有結晶性聚 丙烯的第2成分占45〜10%。藉由含有特定的乙烯.烯 煙共聚物的第1成分占纖維外周的55%或55%以上,可進 12 200934897a copolymer of JUZ/^pn.UUC with a small amount (usually 2% by weight or less) of an α-olefin, such a Ziegler-Natta catalyst or a pentad metal catalyst. General purpose polypropylene obtained from metallocene catalyst. The crystalline polypropylene in the present invention is preferably a melting point of 150 to 165 ° C, preferably 155 to 165 ° C, and a melt mass flow rate (melt mass-flow rate ' ]\«^ = 230. (:, 21.2 N) is in the range of 〇.1 〜 ❹ 8 (^/1 〇 111 丨 11 , and more preferably in the range of 3 〇 4 〇 1 〇 111 丨 11 . The second component of the fiber contains crystalline polypropylene, and a mixture of propylene.3_olefin copolymer or melt mass flow rate (MFR) or molecular weight distribution (Mw/Mn) can be suitably used within a range in which the effect is not significantly impaired. a mixture of crystalline polypropylenes having different physical properties, etc. Further, other thermoplastic resins, or inorganic substances such as titanium oxide, calcium carbonate, and magnesium hydroxide, or various additives (flame retardants, heat-resistant stabilizers, or the like) may be blended as needed. In the second component constituting the conjugate fiber of the present invention, it is generally suitable that the fluorene crystalline polypropylene accounts for at least 75 wt%. In the composite fiber of the present invention The first component and the content of the ethylene-containing olefin copolymer The second component having the crystalline polypropylene constitutes a side-by-side cross section of a specific structure. The fiber component having a right angle to the fiber axis contains the first component of the ethylene-olefin copolymer in the range of 55 to 9 % by weight of the outer periphery of the fiber, and contains crystals. The second component of the polypropylene is 45 to 10%. The first component containing a specific ethylene olefinic copolymer accounts for 55% or more of the outer circumference of the fiber, and can enter 12 200934897

jpil.UUC ❹ ❹ 行100 C或100 c以下的熱處理加工;藉由含有結晶性聚丙 烯的第2成分占纖維外周的1〇%或1〇%以上,而使結晶性 聚丙烯連續地出現於纖維表面,可降低於纖維表面使用乙 烯·α_烯烴共聚物時的纖維間摩擦或對金屬摩擦、黏性, 紡絲性或進行梳棉加工時的其梳棉加工性變得良好。尤其 疋在與纖維軸成直角的纖維截面中,較好的是含有乙烯. α -烯烴共聚物的第1成分占纖維外周的6〇〜8〇%,含有結 晶性聚丙烯的第2成分占40〜20%。 本發明的複合纖維進而在與纖維軸成直角的纖維戴 面中,第1成分與第2成分的邊界線骑出向第丨成分側 彎曲為凸狀的轉。藉由具有該結構,與僅半月狀的兩種 成分接合而成的-般的並職面結構的複合纖維相比,第 1成分與第2成分的邊界_長度增加,㈣種成分間的 接合面積增大,而且採㈣丨成分包㈣2成分的結構, 藉此可抑制第2成分自該複合纖維上剝離。 尤其是在與纖維軸成直角的纖維截面中,當將描繪出 向第i成分侧彎曲為凸狀之曲線的第i成分與第2成分之 邊界線與纖維外周相交的兩個交點設為a與b,將通過將 連接該a與b的線段ab分為2等份的點e、且向與該線段 與第2成分侧的纖維外周相交的點 度的關係滿足炎〇.心之_的方式,上述邊 的1 成分側彎曲為⑽的結構。在滿足更好岐d〜、進而 13 200934897jpil.UUC ❹ ❹ Heat treatment at 100 C or less; in the case where the second component containing crystalline polypropylene accounts for 1% or more of the outer circumference of the fiber, the crystalline polypropylene is continuously present in The surface of the fiber can be reduced in the interfiber friction when the ethylene/α-olefin copolymer is used on the surface of the fiber, or the friction and adhesion to the metal, the spinnability, or the carding workability in the carding process. In particular, in the cross section of the fiber at right angles to the fiber axis, it is preferred that the first component containing the ethylene.α-olefin copolymer accounts for 6〇% to 8〇% of the outer periphery of the fiber, and the second component containing the crystalline polypropylene accounts for 40 to 20%. Further, in the conjugate fiber of the present invention, in the fiber surface at right angles to the fiber axis, the boundary line between the first component and the second component rides on the side of the second component to be convexly curved. By having such a structure, the boundary length of the first component and the second component is increased as compared with the composite fiber of the general coplanar structure in which only two components of the half moon are joined, and the bonding between the components is The area is increased, and the structure of the (four) bismuth component (four) component is obtained, whereby the peeling of the second component from the conjugate fiber can be suppressed. In particular, in the cross section of the fiber at right angles to the fiber axis, the intersection of the boundary line between the i-th component and the second component which curves the curve which is curved toward the i-th component side and the outer periphery of the fiber is set to a and b, by dividing the line segment a1 connecting the a and b into a point e of two equal parts, and satisfying the relationship between the point of intersection with the outer circumference of the fiber on the side of the line and the second component side. The one-component side of the above side is curved to have a structure of (10). In the satisfaction of better 岐d~, and then 13 200934897

^UZ/jpil.UUC 更好的疋cd^l.5ce、特別好的是cd^2ce的關係時複合 =的剝離性、及熱處理時或成形加工時的熱收縮性變 另外,在將描繪出向第i成分側彎曲為凸狀之曲線的 . 帛1成分與第2成分之邊界線看作第2成分的外周所描繪 =的®或橢圓之外周的—部分時,較好的是該邊界線的長 )g)超過應由第2成分所描緣出的圓或橢圓之總外周長 β由第2的二二更好的是大於等於6〇%的情況。尤其是應 ϋ-ί:: 的圓或橢圓之直徑或長抽的兩端存在 =複σ,’ \、’的與纖維轴成直角喊 成分和第2成分之邊界線與纖維= IS 點a、b連接的線段沾之長度為f>ab的關 發揮M u ^於f稷合纖維的截面中可形成對第1成分 ❹㈣峰㈣㈣分在㈣維軸成直 時形狀方面或纖維製造 而言:較好的是第工i成不=第2時成的強度與伸長率的平衡方面 更好的是_〇〜=的Γ率成/=則〜30/70的比率, 絲頭ίίη如合=可用使用先前公知的並列型複合纺 本專利tΓ本專利特開昭48-11417或日 製造。u2-74011中記载的並列型複合紡絲頭等來 200934897 為了使用該並列型複合紡絲頭來形成本發明的複合 纖維的截面雜,必職得含有乙烯·α_触共聚物的第 1成分與含有結晶絲丙烯的第2成分在祕時的流動性 (黏度等)的平衡,考細兩種成分的觸指數(μι)及 熔體質量流動速率⑽R)等,在製造纖維時的條 其進行調整。例如,針對含有乙婦.α•稀煙共聚物的第工 成分,測定19〇t:左右之温度下祕融時的流動 度)’根據炫融流動性(炫融黏度)的變動而選擇 造纖維的流動性(減)的溫度制,使之制纖 條件的擠出溫度,同樣對含有結晶性聚㈣的第2成八^ 2時3〇c=右第的5度定流動性(黏度)而選擇擠‘度 時於以第1成分的熔融流動性(熔融黏度) 的熔融流動性(熔融黏度)相比相對較大的方ΐ選探^ ====力擠出各成分,則於纖= Μ纖維周面的第1成分的比例相對提高。 雖然溶融時的流動性(黏度)的溫度依存性(’ =所使用的樹脂而不同,故不能一概而論,但關於匕 成刀的熔融指數(ΜΙ)與第2成分 (=的比率,當第i成分的請數(二 成刀的炫體f量流動速率(MFR)的比為15〜3 容易形成本發明的複合纖維的截面形狀 為1·8…的範圍。該比越高,越容易形= L2卜成因此第2成分占纖維外周的 Ρ使為相同擠出溫度、熔融黏度’亦可藉由改變樹 15 200934897^UZ/jpil.UUC is better 疋cd^l.5ce, particularly preferably in the relationship of cd^2ce, when the recombination of the composite = and the heat shrinkage during heat treatment or forming are changed, The i-th component side is curved into a convex curve. When the boundary line between the 帛1 component and the second component is regarded as the part of the outer circumference of the second component, or the outer circumference of the ellipse, it is preferable that the boundary line The length of the g) is greater than the total outer circumference β of the circle or ellipse to be traced by the second component, and the second or the second is preferably greater than or equal to 6〇%. In particular, the diameter of the circle or ellipse of ϋ-ί:: or both ends of the long pumping = compound σ, ' \, ' is a right angle with the fiber axis and the boundary between the second component and the fiber = IS point a The length of the b-joined line segment is f>ab, and the cross-section of the fiber can be formed in the cross section of the f-bonded fiber. The first component ❹(4) peak (four) (four) is divided into the (four) dimension axis in the form of straight shape or fiber manufacturing. It is better that the ratio of the strength to the elongation of the second work is not the same as the ratio of the elongation of the _〇~= to the ratio of ~=30/70, the silk head ίίη = It can be manufactured by using the previously known side-by-side type composite spinning patent, Japanese Patent Laid-Open No. 48-11417. The parallel type composite spinning head described in U2-74011, 200934897, in order to form the cross-section of the conjugate fiber of the present invention by using the side-by-side type composite spinning head, the first part containing the ethylene·α-contact copolymer The balance between the composition and the second component containing crystalline propylene in the secret flow (viscosity, etc.), the contact index (μι) of the two components, and the melt mass flow rate (10) R), etc. It is adjusted. For example, for the component containing the Epstein-Barley alpha-smoke copolymer, the fluidity at the temperature of 19 〇t: at the temperature of the melt is measured. 'Selected according to the change in the flow property (shadowing viscosity) The temperature at which the fluidity of the fiber is reduced (minus), and the extrusion temperature of the fiber-forming condition is also the same as the second degree of liquidity (viscosity) of the second octet containing the crystalline poly(tetra). When the degree of melt flow (melting viscosity) of the first component is relatively high, the melt fluidity (melt viscosity) of the first component is selected to be relatively large. The proportion of the first component on the fiber surface of the fiber is relatively increased. Although the temperature dependence (viscosity) at the time of melting differs depending on the resin used, it cannot be generalized, but the melting index (ΜΙ) of the 匕成刀 and the ratio of the second component (=, when i The ratio of the number of components (the ratio of the flow rate (MFR) of the shards of the two knives is 15 to 3. The cross-sectional shape of the conjugate fiber of the present invention is easily formed to be in the range of 1·8... The higher the ratio, the easier the shape is. = L2 卜成 Therefore the second component occupies the outer circumference of the fiber so that the same extrusion temperature, melt viscosity 'can also be changed by the tree 15 200934897

JU^/J>pil.UUC 對提高二=複, ❹JU^/J>pil.UUC is to improve two = complex, ❹

度或樹脂的吐出量以;.,::採所述選擇擠出溫 以提高織維製造時二::用定==纺:法。 Γ=纖維的表面塗佈處理劑。處理劑主要為= 劑,此外麵-步提高纖維表面 靜電 可,出:議酸鹽或其環氧乙燒加成物梨糖醇:: 聚魏等。絲尋體或 基本發明的複合纖維於跡C下熱處理5分鐘^的^ = =’較好的是小於等於3。%,_ 此處職的熱收縮率,是指將本發明的複合纖維製成 短纖維(staple fiber)❿投人至梳棉機中,將於梳棉出口 採取的纖_ (於纖維纏繞的狀態下成為片材者) 規定形狀後,於l〇〇°C下進行5分鐘熱處理,以百分率(°%) 表示處理前後的尺寸的不同(減少量)者。 於本發明中,該熱收縮率具體而言是指以如下方式辨 得的值:將本發明的複合纖維切割成3〇〜65 mm的任意^ 度而製成短纖維,然後將該短纖維投入至小型梳棉機 16 200934897 /^pn.uuc ❹ (miniature carding machine)中,製作單位面積重量為2〇〇 g/m的纖維網;接著使用250 mmx25〇 mm的紙型(paper pattern),於纖維的加工方向(MD)及與該加工方向成直 角的方向(CD)上’沿著紙型切割該纖維網,其後放置 1 〇分鐘’於即將進行熱處理之前啦該經_的纖維網的 MD長度’之後藉由循環熱風式娱箱於1〇〇力下進行 處理後再次败_長度,然後根據以下算 式求付該熱收縮率的值。 熱收縮率(%) = {(L。-L) /L。} χίοο L〇 :熱處理前的MD的長度 L:熱處理後的MD的長度 Ϊί值越小,不織布化時的纖維網的收縮越小,可進 ,從而可獲得質地良好的不織布。 合纖唯的加的熱收縮的取條件,對本發明的複件二處理條件、不織布化條件、使用法 行越穩定的加工 而且 ⑽前所㈣樹脂的組合所形成的並外 現出來^ί維’在製造纖維時的熱處理步驟中, 可發結構及該些樹脂構成的捲縮,其 列型截面 容易表 其結果 可發揮纖維的蓬鬆性提昇效 化的切割成所命且洛 ^ 尤其疋如用以進行不織布 維的自由度高維的集合體即纖維網般,若於纖 身的收縮。因:mr熱處理’則亦料產生纖維自 織布加工後會大二眉的狀態下蓬鬆的複合纖維在不 a縮而無法維持原本的蓬鬆性的情況 17 200934897 較多。另外,於纖維網中,為了使單位面積重量均 維網内的纖維的自由度存在分佈,該分佈程度 ,· ’ 異,因此於不織布化時的熱處理時,容易自自由度更古f 部分產生收縮。因此,更加容易收縮的部分使周邊的= 聚集成束喊為塊狀,_聚#成束錢_少 '八的 ❹ ❹ 單位面積重量下降,因此於不織布整體上單位面積重= 不均變得極為卿,難以獲㈣地均勻的不織布。、 相對於此’本發明的複合纖維無論是否 f分=列型截面結構,亦具有以如下方式配置的二开種 角的纖維截面中占纖維外周的55〜9〇%,進而 晶性聚丙烯㈣2成分;並域點為7Q〜削。c的乙稀有: 較好的是使用分子量分佈(Mw/Mn)為i 5〜 $度為0.87〜0.91 gW、且熔融指數⑽為1〇〜 型烯.α_烯烴共聚物,藉此可維持採用並列 ^面構_料潛在捲縮所引起的蓬鬆性提昇效果的 且可將熱處理加工時的收縮性抑制為可穩定地進 盯不織布化或成形加卫的範圍即小於等於5〇%。 特Ϊ樹脂構成與特定複合結構的本發明的複 二”囍可可5見出如此優異的收縮抑制機構,並不明 ===述特定的乙烯·㈣烴共聚物,將其與結 =人人敬進而製成具有特定的纖維截面形狀的纖 維人驚奇岐軸可抑觀縮,但另—方面,無法期 200934897The degree of discharge of the resin or the resin is selected as follows: ., :: The extrusion temperature is selected to increase the manufacturing of the weaving dimension. Γ = surface coating treatment of fibers. The treatment agent is mainly = agent, and this outer-step increases the surface static of the fiber. It can be: the acid salt or its epoxy Ethylene adduct, the pear sugar alcohol:: Wei Wei, etc. The composite fiber of the wire-seeking or basic invention is heat-treated at track C for 5 minutes ^^ =' is preferably less than or equal to 3. %, _ The heat shrinkage rate of the present invention means that the conjugate fiber of the present invention is made into a staple fiber and thrown into a carding machine, and the fiber taken at the card exit is _ In the case of a predetermined shape, after the shape is specified, heat treatment is performed for 5 minutes at 10 ° C, and the difference (decrease amount) between the dimensions before and after the treatment is expressed as a percentage (%). In the present invention, the heat shrinkage ratio specifically refers to a value which is obtained by cutting the composite fiber of the present invention into any degree of 3 〇 to 65 mm to form a short fiber, and then the short fiber. Put into a small carding machine 16 200934897 /^pn.uuc ❹ (miniature carding machine) to make a fiber web having a basis weight of 2〇〇g/m; then use a paper pattern of 250 mm x 25 〇 mm. Cutting the web along the paper in the machine direction (MD) and the direction (CD) at right angles to the machine direction, and then placing it for 1 〇 minutes before the heat treatment is about to be carried out. The length of the MD is then treated by a circulating hot air entertainment box and then _length again, and then the value of the heat shrinkage rate is calculated according to the following formula. Heat shrinkage rate (%) = {(L.-L) / L. } χίοο L〇 : Length of MD before heat treatment L: Length of MD after heat treatment The smaller the value of Ϊ, the smaller the shrinkage of the web at the time of non-woven, and the better the non-woven fabric with good texture can be obtained. The conditions for the heat shrinkage of the fiber-reinforced fiber are obtained by the combination of the processing conditions of the second part of the invention, the non-woven conditions, the more stable the processing, and the combination of the resin of (10) the former (four) resin. 'In the heat treatment step in the production of fibers, the expandable structure and the crimp of the resin are formed, and the tangent cross-section is easy to show, and the result is that the bulkiness of the fiber is improved and the cut is completed. It is used to form a collection of high-dimensionality of non-woven fabrics, that is, a fiber web, if it shrinks in the body. Because of the mr heat treatment, it is also expected that the bulky conjugate fiber in the state of the second eyebrow after the fiber is processed from the woven fabric will not be able to maintain the original bulkiness. Further, in the fiber web, in order to make the degree of freedom of the fibers in the mesh in the weight per unit area distributed, the degree of distribution is different, so that it is easy to generate a portion of the f from the heat treatment during the heat treatment at the time of non-woven fabricization. shrink. Therefore, the portion that is more easily contracted makes the surrounding = gathering bundle shout as a block, _ poly # into bundles _ less 'eight ❹ ❹ the weight per unit area decreases, so the unit area on the non-woven fabric is heavy = uneven Extremely clear, it is difficult to obtain (four) uniform non-woven fabric. In contrast to the 'composite fiber of the present invention, whether or not the f-minus=column-type cross-sectional structure, the fiber cross-section of the two-opening angle disposed in the following manner accounts for 55 to 9 % of the outer circumference of the fiber, and further the crystalline polypropylene (4) 2 components; the boundary point is 7Q~cut. Ethylene of c: It is preferred to use a molecular weight distribution (Mw/Mn) of i 5 to $degree 0.87 to 0.91 gW, and a melt index (10) of 1 〇~ type olefin. It is possible to suppress the shrinkage property by the potential crimping by the parallel surface structure, and to suppress the shrinkage property at the time of heat treatment processing so that the range which can be stably infiltrated or formed and cured is 5 〇% or less. The bismuth resin of the present invention having a specific composite structure and a specific composite structure exhibits such an excellent shrinkage suppression mechanism, and it is not known that the specific ethylene (tetra) hydrocarbon copolymer is described, and it is Furthermore, it is possible to make a fiber with a specific fiber cross-sectional shape, and it is surprising that the fiber axis can be suppressed, but on the other hand, it cannot be 200934897.

J\JL· / Jpll.UuC 待能夠獲得通常被認為是相反性能的蓬鬆性優異、質感良 好、並且100°c或100°C以下的低溫下的熱處理加工特性優 異的不織布。 ❹J\JL· / Jpll.UuC A non-woven fabric having excellent bulkiness, good texture, and excellent heat treatment processing characteristics at a low temperature of 100 ° C or less, which is generally considered to be the opposite performance. ❹

本發明的複合纖維的纖度(fineness)並無特別限定。 選擇考慮到構成複合纖維的成分的物性及製造時的步驟穩 定性、並且適於將該複合纖維加工為不織布或成形體的纖 度即可。例如,於直接接觸人的皮膚的化妝棉(c〇smetic puff)或藥劑塗佈片材等用途中,較理想地是於1〜5 dtex ,範圍内選擇’另外,於以印表機的墨g (inkcartridge) 等為代表的液體保持材用途中,合適的是丨〜⑺出⑶的範 f、’此外’於家顧芳香綱芳香芯之賴紐揮發材料 途中’合適的是1〜20 dtex的範圍。 或短定,可為長纖維 纖維的紗b/為纖料’其切度可根據該複合 經過㈣工法或用途而適當選擇。作為短纖維,於 二形時,較好的是設為如〜⑵麵,進 設為25〜75^梳棉通過性或纖維網的質地,較好的是 明的複合纖維=另外’於利用氣紡(也姻)法將本發 較好的是設為订不織布化的情形時,氣紡用短纖(chop) 巧 mm。 本發明的複人纏 、 纖維網或不織布,σ纖維為曰了使纖維束開纖而獲得蓬鬆的 捲縮類型可輪f好的是具有觸。峨予的捲縮數或 加工法或用途合纖維的纖度及切割長度,另外根據 、而適當選擇。例如,當以3.3〜· 19 200934897 ^υζ/Dpu.aoc i38〜45mm的複合纖維(短纖維)以梳棉 法製成纖_時’較好的是賦侦縮數U)〜25道/25 mm · J 口.3〜6.6 dtex的纖度將切割長度為3〜6随的複合纖 以氣紡法製成纖維網時,較好的是於捲 ^數5〜15道/25咖的範圍内賦予,縮的類型可例示鑛 齒(ngzag)形狀或螺旋(spiral)結構者。 ❹ 為了將本發明的複合纖維加I為不織布較 在形成纖_後進行誠㈣使其不織布 使該複合纖維通過梳棉二 使_;轉::=輸 =等’但並不限定於該些方法。當使用該些形 明顯損壞本發明的效果,則可混棉其他纖Ϊ。可、、1 =例如可舉出用以提高保水性的螺縈(咖 妒& Γ1 Gn)、用以使不織布更蓬鬆的以聚對苯二甲酸乙: 酉日為成分的中空纖維(hollowflber)等。 一 以該些纖維網形成法來形成所需的單位面積重署The fineness of the conjugate fiber of the present invention is not particularly limited. The physical properties of the components constituting the conjugate fiber and the step stability at the time of production may be selected, and the conjugate fiber may be processed into a fineness of a nonwoven fabric or a molded body. For example, in a use of a cotton pad (c〇smetic puff) or a drug-coated sheet that directly contacts a person's skin, it is preferable to select "in addition to the ink of the printer" within a range of 1 to 5 dtex. g (inkcartridge) and the like are representative of the liquid retaining material, and it is suitable to use 丨~(7) out (3) of the formula f, 'external' in the middle of the home fragrant aromatic core of the Lai New volatile material 'suitable is 1~20 dtex The scope. Or short-term, it can be a long fiber fiber yarn b / fiber material 'the degree of cut can be appropriately selected according to the compound (4) method or use. As the short fiber, in the case of a dichroic shape, it is preferably set to a surface of, for example, a ~(2) plane, and a texture of a card or a fiber web of 25 to 75, preferably a bright composite fiber = another 'utilization' The air-spinning (singularity) method is preferable to the case where the staple fiber is made into a non-woven fabric, and the air-spun staple fiber (chop) is skillfully mm. In the entangled, web or non-woven fabric of the present invention, the sigma fiber is a type of crimp which is obtained by opening the fiber bundle to obtain a fluffy type. The number of crimps or the fineness and the length of the cut of the processing method or the use of the fibers are appropriately selected depending on the type. For example, when the composite fiber (short fiber) of 3.3~· 19 200934897 ^υζ/Dpu.aoc i38~45mm is made into a fiber by the carding method, it is better to compensate the number of U)~25 channels/25 Mm · J port. 3 to 6.6 dtex fineness. When the composite fiber with a length of 3 to 6 is cut into a fiber web by air spinning, it is preferably given in the range of 5 to 15 channels/25 coffee. The type of shrinkage can be exemplified by a ngzag shape or a spiral structure. ❹ In order to add the composite fiber of the present invention to the non-woven fabric, it is not necessary to make the fiber _ after the formation of the fiber _ (4) so that the woven fiber is not woven, so that the conjugate fiber passes through the carding _; turn::====, but is not limited to these method. When these shapes are used to significantly impair the effects of the present invention, other fibers can be mixed. Yes, 1 =, for example, a screw (Curry & Γ1 Gn) for improving water retention, and a hollow fiber (Polyflber) which is made of polyethylene terephthalate for the purpose of making the nonwoven fabric more fluffy )Wait. The formation of the required unit area by the formation of the webs

Mn對纖軸進行熱處㈣使其不織布化 於進行熱處理前,使用藉由水流或 夺可 (spun.ee) ee epuneh)法’使強度提高或質感發生變化Γ 輕針i為熱處理法,可例示熱風黏接法、熱水黏接法、舳 法等方法。其中,在將本發明的複合纖維形二 維網後所進行的熱處理法較好的是熱風黏接法或熱 20 200934897Mn heats the fiber axis (4) so that it is not woven before heat treatment, and the strength is improved or the texture is changed by the water flow or the spe. ee ee epuneh method. The light needle i is a heat treatment method. Examples include hot air bonding method, hot water bonding method, and sputum method. Among them, the heat treatment method after the composite fiber-shaped two-dimensional net of the present invention is preferably hot air bonding or heat 20 200934897

jyj^L/^yiL.LiuC 法。 熱風黏接法是使經加熱的 ==成分軟化,,從而使纖維交= 精而有rJ:广減*辆城_躲般擠碎一定面 = 法,因此是適於提供本發明的課題 p逢氯且貝地、質感良好的不織布的黏接法。 舰是適於提供蓬鬆且《感良好的不織布 ❹Jyj^L/^yiL.LiuC method. The hot air bonding method softens the heated == component, so that the fiber cross = fine and has rJ: wide reduction * city _ hiding like a face = method, and thus is suitable for providing the subject of the present invention p The bonding method of non-woven fabrics with good chlorine and shellfish and good texture. The ship is suitable for providing fluffy and "feeling non-woven fabrics"

當以熱風黏接法對尤其是具有以兩種成 入Ϊ月形狀組合型並列截面的短纖維經切割 =,5纖_進行熱處理時,輸送帶上的纖維網的自 所^^ = ^與其他黏接法相比收縮容易變大,難以獲得 貝或質感良好的不織布。另一方面,本發明的複合纖維 由於因用以不織布化的熱處理所引起的收縮得到有效抑 制’故尤其適合於該熱風黏接法巾使用, 法而提供不僅維持本來所帶來的蓬鬆性此種優祕^ 質感優異的不織布。 '熱水黏接法是藉由使熱水或蒸氣通過纖維網之中而 使複合纖維的低熔點成分軟化、熔融,從而使纖維交織部 分黏接的方法。本發明的複合纖維,由於含有具有7〇艺〜 100C之熔點的乙烯·α•烯烴共聚物的第丨成分占纖維周 面的半以上’故可應用本來為ioo°c或1〇〇。〇以下的熱^ 理的熱水黏接法。該黏接法中所使用的媒體為熱水或蒸氣 此種比較便宜、無需特殊設備的媒體,藉由利用此種媒體 進行處理,可在進行不織布化的同時基本上洗去塗佈於本 21 200934897When the short fiber having the parallel cross-section of the two types of the shape of the moon into the shape is cut by the hot air bonding method, the heat treatment is performed on the fiber web on the conveyor belt. Other bonding methods tend to shrink more than shrinkage, and it is difficult to obtain a non-woven fabric having a good texture or a good texture. On the other hand, the conjugate fiber of the present invention is effectively inhibited by the shrinkage caused by the heat treatment for non-woven fabrication, so it is particularly suitable for use in the hot air bonding hood, and the method provides not only the maintenance of the original fluffiness. A special kind of non-woven fabric with excellent texture. The 'hot water bonding method is a method in which the low-melting component of the conjugate fiber is softened and melted by passing hot water or steam through the fiber web to bond the fiber interlaced portion. In the conjugate fiber of the present invention, since the ruthenium component of the ethylene·α• olefin copolymer having a melting point of from 7 Å to 100 C is more than half of the fiber surface, the original ioo°c or 〇〇 can be applied. 〇 The following hot water bonding method. The medium used in the bonding method is a medium which is relatively cheap and does not require special equipment such as hot water or steam. By using such a medium for processing, it can be substantially washed and applied while being non-woven. 200934897

I 發明的複合纖維的表面的處理劑。塗佈於纖維表面的處理 劑於複合纖維(短纖維及氣紡祕纖等)製造步驟中不可 或缺’但根據用途,在不織布化或成形加工之後會不需要、 或成為障礙。例如直接接觸食品的食品保護片材或包材或 托盤(tray)、含浸化妝品的化妝棉、用以將藥劑塗佈於患 部的棉棒(stiek) #。亦存在以安全的食品添加物或基= 此的成分來構成纖維表面的處理劑的方法、或者在形成不 織布或成形體後設置清洗步驟而洗去處理劑的方法,但即 便以對人體安全的成分來構成處理劑,亦並非沒有對化妝 品或藥劑的影響’為了保持製品的穩定性能,較理想的是 儘可能不於不織布或成形體上殘留處理劑。另外,在加工 為不織布或成形體後進一步經過清洗步驟,需要追加設 及時間,於成本方面不利。 认 因此,針對如上所述的用途,在能約以低成本高效地 提供蓬鬆、且處理劑幾乎不附著或處理劑的附著量經有效 ❹ 地減少至不會引起上述不良情況的程度的不織布或成形體 的方面,可採用熱水黏祕的本發明之複合纖維的工業音 義極大。最好的是使用本發明的複合纖維,藉由教水黏^ 法而進行錢布化、成形加玉’或者㈣時以熱風黏接法 進行熱處理而製成不織布的複合纖維,熱水黏接 行成形加工。 將本發明的複合纖維加工為不織布時的不織布 位面積重量可根據使用目的而適當選擇。例如,於食〇勺 材的用途中,較理想的是於2G〜5G咖2的内選= 22 200934897I The treatment agent for the surface of the composite fiber of the invention. The treatment agent applied to the surface of the fiber is indispensable in the production steps of the composite fiber (short fiber and air-spun fiber, etc.), but depending on the application, it may not be required or become an obstacle after the nonwoven fabric or the forming process. For example, a food protection sheet or a packaging material or a tray which directly contacts food, a cotton pad impregnated with cosmetics, and a cotton swab (stiek) # for applying the medicine to the affected part. There is also a method of forming a treatment agent for a fiber surface with a safe food additive or a component of the composition, or a method of setting a cleaning step to form a cleaning agent after forming a nonwoven fabric or a molded body, but even if it is safe for human body. The composition constitutes a treatment agent and does not have an effect on the cosmetic or the pharmaceutical agent. In order to maintain the stability of the product, it is preferred that the treatment agent remains as far as possible from the non-woven fabric or the molded body. Further, after the processing is performed into a non-woven fabric or a molded body, the cleaning step is further required, and additional time is required, which is disadvantageous in terms of cost. Therefore, for the use as described above, it is possible to efficiently provide a non-woven fabric which is bulky and can be efficiently disposed at a low cost, and the amount of adhesion of the treating agent hardly adheres or the treating agent is effectively reduced to such an extent that the above-mentioned adverse conditions are not caused. In terms of the molded body, the industrial sound of the composite fiber of the present invention which can be adhered by hot water is extremely large. It is preferable to use the composite fiber of the present invention to form a non-woven composite fiber by heat-sealing by heat-air bonding by means of a water-viscosing method, and to form a non-woven composite fiber by hot water bonding, and hot water bonding. Line forming processing. The non-woven fabric area weight when the conjugate fiber of the present invention is processed into a non-woven fabric can be appropriately selected depending on the purpose of use. For example, in the use of oyster spoons, it is desirable to select within 2G~5G coffee 2 = 22 200934897

jpu.uuC 於化妝棉或藥劑含浸片材等用途中,較理想的是於3〇〜 150 g/m2的範圍内選擇,另外,於藥劑塗佈用棉棒 中’較好的是50〜250 g/m2的範圍。 另外,將本發明的複合纖維加工為不織布時的不織布 的蓬鬆度是以比容積(specific volume)算出,容易獲得大 於等於20 cm3/g的蓬鬆度,亦可適宜獲得大於等於^jpu.uuC is preferably used in a range of 3 〇 to 150 g/m 2 in a cotton pad or a chemical impregnated sheet, and is preferably 50 to 250 in a cotton swab for drug application. The range of g/m2. Further, the bulkiness of the nonwoven fabric when the conjugate fiber of the present invention is processed into a non-woven fabric is calculated by a specific volume, and it is easy to obtain a bulkiness of 20 cm 3 /g or more, and it is also suitable to obtain a ratio of more than or equal to ^

❹ 在將本發明的複合纖維加工為不織布時,亦可根據目 的而於該錢布上積層其他錢布或纖維網、哉塑性薄 貼:例的透氣性薄臈、開孔薄膜或 開孔不織布貼合,或與由彈性體(dast〇mer)、 烯烴共聚物所構成的伸縮性不織布積層等。" 於本發明中,所謂「成形體」,是指a 合纖維,未_錢布化步㈣進行加王 加後 品’以及經過不織布化步驟而進行加 的加工 當未經過不織布化步驟而進行加工時,。品。 放入特定的模射,於維—, 「成形體」。當經過不織布。驟=理,藉此可獲得 明的複合纖維利用梳棉法或氣纺法等^ =時,可將本發 重量的纖維網,將該纖維網以孰風黏接需單位面積 的不織布重疊織 法或熱水輪_ 一體而 23 200934897 juz / jpu.aoc 本發明^複合纖維進行不織布化後,將不織布重憂 1所需的單位面積重#及厚度,或將該錢布切割並 :且^然後將所獲得者放人特料模具中,於此狀態下進 仃熱處理,獲得「成形體」。 使用本發明的複合纖維所獲得的「成形體」,亦可容 易地進行切觀「成形體」的—部分、或進 理等的2次加工。 丁”、、地 Φ❹ When the conjugate fiber of the present invention is processed into a non-woven fabric, other kraft cloth or fiber web or enamel plastic thin plaque may be laminated on the kraft cloth according to the purpose: a breathable thin enamel, an apertured film or a perforated non-woven fabric. It is bonded or laminated with a stretchable nonwoven fabric composed of an elastomer (dast mer) or an olefin copolymer. " In the present invention, the term "molded body" means a fiber, and the process of adding the product after the addition of the king and the step of the non-woven step is performed without the step of non-woven. When processing, Product. Put in a specific mold, in the dimension - "formed body". When not through the fabric. If the composite fiber is obtained by the carding method or the air-spinning method, the fiber web of the present weight can be woven by the woven fabric, and the non-woven fabric of the unit area is overlapped and woven. Method or hot water wheel _ integrated and 23 200934897 juz / jpu.aoc The invention ^ after the composite fiber is not woven, the non-woven fabric is seriously worried about the required unit area weight # and thickness, or the money cloth is cut and: and ^ Then, the obtained person is placed in a special mold, and heat treatment is performed in this state to obtain a "molded body". The "molded body" obtained by using the conjugate fiber of the present invention can be easily subjected to secondary processing such as "sectioning" or "processing". Ding", ground Φ

本發明的複合纖維可適宜祕化妝棉或藥劑塗佈片 ,、退熱片材(antiPyretie sheet)、食品托盤、減震材料 (cushioning material)、緩衝材料、家庭用芳香劑等的芯 材、加濕器等的保液材料、育苗片材(raising止⑽) 布(wiper)等用途。 [實施例] 其次藉由實施例與比較例來具體說明本發明,本發明 並不限定於以下實施例。而且,本說明書尤其是實施例與 比較例、以及以下表1〜3中所使用的術語的定義及測定方 法如下所述。 (1) 熔融指數 MI :基於 ASTM D-1238,於 19(TC、21 2 N 的條件下 進行測定。 而且,表中所示的數值是對樹脂進行測定的數值 位:g/min) (2) 密度 基於JIS K7112進行測定。 24 200934897 juz/Dpu.aoc 而且’表中所示的數值是對樹脂進行測定的數值。(單 位:g/cm3) (3) 分子量分佈(Mw/Mn) 分子量分佈為重量平均分子量與數量平均分子量的 比,是藉由凝膠滲透層析法(gel permeation chromatography)求得。使用 Waters 製造的「GPC-150C」 ❹The composite fiber of the present invention can be used as a core material for a cosmetic cotton or a drug coated sheet, an antiPyretie sheet, a food tray, a cushioning material, a cushioning material, a household fragrance, and the like. Liquid-repellent materials such as wetters, seedling sheets (raising), and the like. [Examples] Next, the present invention will be specifically described by way of Examples and Comparative Examples, but the present invention is not limited to the following Examples. Further, the definitions and measurement methods of the terms used in the present specification, particularly the examples and comparative examples, and the following Tables 1 to 3 are as follows. (1) Melt index MI: Measured under conditions of 19 (TC, 21 2 N based on ASTM D-1238. Moreover, the numerical values shown in the table are numerical values measured for the resin: g/min) (2 The density is measured based on JIS K7112. 24 200934897 juz/Dpu.aoc and the values shown in the table are the values measured for the resin. (Unit: g/cm3) (3) Molecular weight distribution (Mw/Mn) The molecular weight distribution is a ratio of the weight average molecular weight to the number average molecular weight, which is determined by gel permeation chromatography. "GPC-150C" made by Waters ❹

進行測定。(管柱:Tosoh製造的TSKgel GMH6-HT 7.5 cm I.D.x60 cm 1 根) 而且’表中的數值是對原料樹脂進行測定的值。 (4) 熔點 熔點表示樹脂熔融的溫度,是使用示差掃描熱量言 (DSC)進行測定。(單位:。€ ) 使用ΤΑ INSTRUMENTS製造的DSC「Q-l〇」進行頌 定。將樹脂切割成4.20〜4.80 mg的重量,將其填充至考 品盤(sample pan)中,並加以覆蓋。於A沖洗 内以~l〇°C/min的升溫速度自30。〇升溫至2〇〇乞,進淨 定’獲得熔_表。制表進行分析*求得糾峰值The measurement was carried out. (Tube: TSKgel GMH6-HT manufactured by Tosoh 7.5 cm I.D.x60 cm 1 piece) and the values in the table are values measured for the raw material resin. (4) Melting point The melting point indicates the temperature at which the resin is melted and is measured by differential scanning calorimetry (DSC). (Unit: €) Use the DSC "Q-l〇" manufactured by INSTRUMENTS to make the adjustment. The resin was cut into a weight of 4.20 to 4.80 mg, filled into a sample pan, and covered. In the A flushing, the heating rate is ~30 °C / min from 30. 〇 Warm up to 2 〇〇乞, enter the net to get the melt _ table. Tabulation analysis*

(5 )溶體質量流動速率(mfr) X 基於JIS K72H),於23(rc、21.2 N的條件下 解岐妓制冊料相定的值< (6)纖度、纖維徑 是由單位長度的重量 纖度、纖維控表不纖維的粗度, 真出。(單位:dtex ) 25 200934897(5) The mass flow rate of the solution (mfr) X is based on JIS K72H), and the value of the tantalum is determined at 23 (rc, 21.2 N). (6) The fineness and fiber diameter are determined by the unit length. The weight of the fiber, the fiber control table, the thickness of the fiber, the true. (Unit: dtex) 25 200934897

y i k场·^纖难《^徑0 度。 =厌+死为時,使用掃描型電子顯微 得的圖像中任意選擇100根纖維,測 由直徑的平均值與纖維的比重算出纖 © )第1成刀相對於纖維截面外周長的占有率等、 截面形狀觀察 π干矛 =合纖維以相對於長度方向成直角的方式加以切 ^藉由光學賴鏡或掃㈣電子紐鏡騎觀察並求 得.第1成分相對於與纖維轴成直角之纖維截面的纖維外 周長的佔有率(%);在與纖維軸成直角的纖維截面中,當 將描緣出向第1成分侧弯曲為凸狀之曲線的第1成分和第 2成分之邊界線與纖維外周相交的兩做點設為,將 通過將連接該a與b的線段ab分為2等份的點c、且向與 〇 該線段ab成直角的方向上延伸的直線與第i成分和第2 成^之邊界線相交的點設為d、與第2成分侧的纖維外周 相父的點設為e時,纖維cd的長度相對於線段ce的長度 的士(cd/ce);另外,將描繪出向第i成分侧彎曲為凸= 的第1成分與第2成分的邊界線看作第2成分的外周所描 繪出的圓或橢圓之外周的一部分時,該邊界線的長度 對於應由第2成分所描繪出的圓或橢圓之總外周長h的比 (g/h);進而,應由第2成分所描繪出的圓或橢圓之直徑 26 200934897 juz/jpii.aoc 或長轴的_存在賤複合纖_與纖雜成直角的 截面内時該直徑或長轴的長度[與線段ab的長度的長短^ 係0 使用NIKON製造的光學顯微鏡或日本電子㈣ f/7有限公㈣造的掃描型電子顯微鏡「簡_T22Q」進 冑自所獲得的圖像測定各成分露丨於纖維表面的部分的 長度,代入下式中而算出。而且,於纖維截面中第丨成分 與第2成分的區別可在將纖維以相對於長度方向成直角: 方式加以切割的狀態下進行熱處理而確認。例如,將切 後的纖維放置於l〇〇°C的烘箱乾燥器内,使第丨成分軟化、 熔融後,利用光學顯微鏡或掃描型電子顯微鏡進行觀察,' 確認纖維截面的哪一部分為第1成分。 ^ 第1成分的周面的長度(%) = (Li/L) χ100 L1 :第1成分的周面的長度 L:纖維截面的周面的全長 (8)熱收縮率 〇 熱收縮率是針對纖維網,表示熱處理前後的單位長度 的變化(減少率),是由變化量與單位長度的比算出。ς 位:%) 平 使用250 mmx250 mm的紙型,於纖維的加工方向 (MD)及與該加工方向成直角的方向(CD)上,分別沿 著該紙型對通過小型梳棉機而採取的纖維網200 g/m2進行 切割。放置10分鐘後,接著將經切割的纖維網置於牛皮 (kraft)紙(350 mmx700 mm)之上,測定MD的長度。 27 200934897 ^uz/^pix.aoc 其後,將牛皮紙對折而形成輕輕覆蓋纖維網之上的狀態, 於此狀態下放入SANYO製造的對流烘箱(循環埶風 中,於10(TC下進行5分鐘熱處理。處理結束後自'乾燥器 中取出,於室溫下放置冷卻5分鐘,再次測定MD的長度。 然後代入下式中而算出熱收縮率。y i k field · ^ fiber difficult "^ diameter 0 degrees. In the case of anaesthesia + death, 100 fibers are arbitrarily selected from the image obtained by scanning electron microscopy, and the average value of the diameter and the specific gravity of the fiber are measured. The fiber is occupied by the outer circumference of the first section. Rate, cross-sectional shape observation π dry spear = conjugate fiber is cut at right angles to the length direction. Obtained by optical ray mirror or sweep (four) electron beam mirror ride. The first component is relative to the fiber axis. The percentage (%) of the outer circumference of the fiber in the cross section of the fiber at right angles; and the first component and the second component in the cross section of the fiber at right angles to the fiber axis when the curve is bent to the first component side The two points at which the boundary line intersects the outer periphery of the fiber are set to be a line c which divides the line segment ab connecting the a and b into two equal parts and extends in a direction at right angles to the line segment ab and When the point at which the boundary between the i component and the second component intersects is d, and the point at which the outer edge of the fiber on the second component side is set to e, the length of the fiber cd is relative to the length of the segment ce (cd/ce) In addition, the first component and the second component which are bent to the i-th component side and convex = are drawn. When the boundary line of the division is regarded as a part of the outer circumference of the circle or ellipse drawn by the outer circumference of the second component, the ratio of the length of the boundary line to the total outer circumference h of the circle or ellipse to be drawn by the second component ( g/h); further, the diameter of the circle or ellipse depicted by the second component 26 200934897 juz/jpii.aoc or the long axis of the composite fiber _ is in the cross section at right angles to the fiber, or The length of the long axis [the length of the line segment ab ^ is 0. Using an optical microscope made by NIKON or a Japanese-made electronic (4) f/7 limited (4) scanning electron microscope "Jane_T22Q" The length of the portion of each component exposed on the surface of the fiber was measured and substituted into the following formula to calculate. Further, the difference between the second component and the second component in the fiber cross section can be confirmed by heat treatment in a state where the fiber is cut at a right angle to the longitudinal direction. For example, the cut fiber is placed in an oven drier at 10° C., and the second component is softened and melted, and then observed by an optical microscope or a scanning electron microscope to confirm which part of the fiber cross section is the first. ingredient. ^ The length of the circumferential surface of the first component (%) = (Li/L) χ100 L1 : the length L of the circumferential surface of the first component: the total length of the peripheral surface of the fiber cross section (8) The heat shrinkage ratio 〇 The heat shrinkage rate is The fiber web indicates the change in the unit length (reduction rate) before and after the heat treatment, and is calculated from the ratio of the amount of change to the unit length. ς Bit: %) Flat paper size of 250 mm x 250 mm, taken in the machine direction (MD) of the fiber and in the direction (CD) at right angles to the machine direction, respectively, taken along the paper type through the small card The web was cut at 200 g/m2. After standing for 10 minutes, the cut web was then placed on kraft paper (350 mm x 700 mm) and the length of the MD was determined. 27 200934897 ^uz/^pix.aoc Thereafter, the kraft paper is folded in half to form a state of lightly covering the top of the fiber web, and placed in a convection oven manufactured by SANYO in this state (circular hurricane, at 10 (TC) After heat treatment for 5 minutes, the sample was taken out from the 'dryer, and left to stand at room temperature for 5 minutes, and the length of MD was measured again. Then, the heat shrinkage rate was calculated by substituting into the following formula.

熱收縮率(%) = {(Lo-L) /Lq} χ1〇〇 L〇 :熱處理前的Md的長度 L.熱處理後的MD的長度 (9)單位面積重量 旦單位面積重量表示不織布及纖維網的每單位面積的 重里,疋由切割成一定面積的不織布或纖維網的重量算 出。(單位:g/m2) 將切割成250 mmx250 mm的不織布以a&D公司製 造的上皿電子天平「HF··」測定重量,將練值放大16 倍而算出單位面積重量。 (10)蓬鬆度(比容積) ,鬆度表示不織布的每單位體積的重量,是由單位面 積重量測定與厚朗絲算出。(單位:Cm3/g) 使用東洋精機製作所製造的「Digi-Thickness 於⑼(anVil)負荷為2 g/cm2、速度為2 mm/sec 下測定不織布的厚度,由該數值(腿)與單位面 積重置(g/m2)算出蓬 (11)質感 貝感疋對不織布的外觀質地、手㈣柔軟性、動性、 28 200934897 ^uz/^pir.aoc 膨脹等進行綜合判斷者。 藉由官能檢查員(paneler)的官能試驗進行判斷。以 「良好」、「普通」、「差」3階段的基準進行評價。 以下說明實施例1〜6及比較例1〜6,將該些的結果 匯總於表1〜3。 [實施例1]Heat shrinkage rate (%) = {(Lo-L) / Lq} χ1〇〇L〇: length of Md before heat treatment L. length of MD after heat treatment (9) unit area weight denier unit area weight means non-woven fabric and fiber The weight per unit area of the net is calculated from the weight of the non-woven fabric or web that is cut into a certain area. (Unit: g/m2) The weight of the non-woven fabric cut into 250 mm x 250 mm was measured by a weighing electronic balance "HF··" manufactured by a & D, and the weight per unit area was calculated by amplifying the exercise value by 16 times. (10) Bulkness (specific volume), the degree of looseness indicates the weight per unit volume of the non-woven fabric, and is calculated from the unit area weight and the thick ray. (Unit: Cm3/g) The thickness of the non-woven fabric was measured using the Digi-Thickness (2) (an Vil) load of 2 g/cm2 and the speed of 2 mm/sec. The value (leg) and unit area were measured by the Toyo Seiki Co., Ltd. Reset (g/m2) to calculate the texture of the poncho (11), the texture of the non-woven fabric, hand (four) softness, dynamics, 28 200934897 ^ uz / ^ pir. aoc expansion, etc. The panel test of the paneler was judged and evaluated on the basis of the three stages of "good", "normal" and "poor". Examples 1 to 6 and Comparative Examples 1 to 6 will be described below, and the results of the above are summarized in Tables 1 to 3. [Example 1]

❿ 第1成分為使用二茂金屬觸媒進行聚合而成的乙烯. (2-浠烴共聚物,烯烴為辛烯-1,在共聚物中含有1〇 mol%。該乙烯.α_稀烴共聚物的密度為〇 88〇,熔點為72 C,溶融指數(ΜΙ)為18g/l〇min,且分子量分佈(Mw/Mn) 為1.9。第2成分是熔體質量流動速率(MFR)為8岁1〇 min、且溶點為16〇。〇的結晶性聚丙烯。 一 A竣空陶樘戚为作為構成成分,使用並列型複合紡絲 頭,以第1成分/第2成分= 50/50的容積比,並且於第i ^上从刀Z風分=5〇/5〇的容積比,並且於第i rc:第2成分侧為赋的擠出溫度(設定溫 dtex的二=且 好。然後將所獲得的纖度為6.5 的加熱農 = 至長=Wnt)使用具有机的峨 捲= 的稷合纖維(短纖維)。 θ乃.2 #m) ^ (4) 溶以指數(MI)、分子量分佈(Mm/Mn)。 29 200934897 ju//^pii.aoc i 根據上述(4)、(5)的測定方法來測定熔 里流動速率(mfr)。將該些的結果示於表1 的構成成为的項目中。根據上述(6 複合纖維(短纖維)的纖維物性。將該些j Γϋ維截面的概略圖一併示於表1的絲質的項目 的制直角的方向的纖維截面中未發現成分間 進而,Cd/Ce=7.5,f>ab,且 g/h=0.80。 官许f 所獲得的複合纖維(短纖維)投入至500 mm 渦m棉機中’採取纖維網。梳棉步驟中的纖維通 纖維網’根據上述(8)的測定方法來測 .....'。將其結果示於表1的絲質的項目中。另外, ;50 g所獲得的複合纖維(短纖維)投入至500 _寬产 η ϋ㈣機巾’製錢_。紐使賴風循環式的熱 虫rough air)加工機,於設定温度為9 〇 加工時間為12咖的條件下對該織維= 根據上述(9)〜(⑴的測定方法,對所 =不織布的物性進行測定及評價。將該些的結“於表1 的不織布物性的項目中。 、表1 ,用有所得複合纖維(短纖維)的纖維網的執❿ The first component is ethylene obtained by polymerization using a metallocene catalyst. (2-anthraquinone copolymer, olefin is octene-1, and contains 1 〇mol% in the copolymer. The ethylene.α_lean hydrocarbon The copolymer has a density of 〇88〇, a melting point of 72 C, a melt index (ΜΙ) of 18 g/l〇min, and a molecular weight distribution (Mw/Mn) of 1.9. The second component is a melt mass flow rate (MFR) of 8 years old 1 〇 min, and the melting point is 16 〇. Crystallized polypropylene of 〇. A 竣 hollow ceramic 樘戚 is used as a constituent component, using a parallel type composite spinning head, with the first component / the second component = 50 /50 volume ratio, and the volume ratio from the knife Z wind division = 5 〇 / 5 第 on the i ^ ^, and on the i r rc: the second component side is the assigned extrusion temperature (two sets of the temperature dtex = Good. Then, the obtained fineness of 6.5 is heated = up to Wnt) using a twisted fiber (staple fiber) with a machine roll = θ is .2 #m) ^ (4) (MI), molecular weight distribution (Mm/Mn). 29 200934897 ju//^pii.aoc i The melt flow rate (mfr) is measured according to the measurement methods of (4) and (5) above. The results of these results are shown in the items of the composition of Table 1. According to the fiber properties of the above-mentioned (6 conjugate fiber (short fiber), a schematic view of the j-dimensional cross section is shown in the fiber cross section in the direction of the right angle of the silk item of Table 1, and no component is found. Cd/Ce=7.5, f>ab, and g/h=0.80. The composite fiber (short fiber) obtained by Guanfu f was put into a 500 mm vortex m cotton machine to take the fiber web. The fiber pass in the carding step The fiber web was measured according to the measurement method of the above (8). The results are shown in the silky item of Table 1. In addition, 50 g of the obtained conjugate fiber (short fiber) was put into 500 _ wide production η ϋ (four) scarf 'money _. New Zealand Lai wind circulation type hot insect rough air processing machine, at a set temperature of 9 〇 processing time is 12 coffee under the condition of the weaving dimension = according to the above ( 9) The measurement method of (1) is used to measure and evaluate the physical properties of the non-woven fabric. The knots are referred to in the item of non-woven fabric properties in Table 1. Table 1, using the obtained composite fiber (short fiber) Fiber web

:! 5:。的較低數值,故於利用熱風黏接法的 亦J 獲侍遙鬆、且質地及質感良好的不織布。 丌了 [實施例2] 30 200934897 ^uz/^pu.aoc mol%。該乙烯·α-稀烴共聚物的密度為〇 885,熔點為78 C,炼融指數(MI)為30g/i〇min,且分子量分佈(Mw/Mn) 為2.0。第2成分是熔體質量流動速率(MFR)為16 g/1〇 min '且熔點為160°C的結晶性聚丙烯。 以該些兩種成分作為構成成分,使用並列型複合紡絲 頭,以第1成分/第2成分= 50/50的容積比,且於第j成 分側為20(TC、第2成分侧為細。c的擠出溫度(設定溫度) ⑩=條件下進行舰紡絲。卷取時,使以山梨糖騎脂肪酸 二^基鱗_鹽的環氧乙烧加成物作為主成分的抗 電劑附者。紡絲性良好。然後將所獲得的纖度為1〇.2出饮 合長絲使用具備6Gt的加熱觀的加熱裝置延伸 獲广输;^捲縮賦予裝置賦予捲縮後,切割成38 _, 纖^ 故(纖維徑為31.7㈣的複合纖維(短 測定〜(4)的測定方法來 ❹針對第2成分,根攄上十)、分子量分佈(MW/Mn)。 點、熔體質量、t二()、(5)的測定方法來測定熔 的構成【=速率(MFR)。將該些的結果示於表1 測項Γ。根據上述⑷、⑺的測定方法來 的概略圖—併示於表1的轉皙的Β 二=:軸?角的方向的纖維截面中== 6.〇,f&gt;ab,w g所獲得的複合纖維(短纖維)投入至500 mm 31 200934897:! 5:. The lower value, so the use of hot air bonding method is also a non-woven fabric with a loose texture and good texture.丌 [Example 2] 30 200934897 ^uz/^pu.aoc mol%. The ethylene·α-dilute hydrocarbon copolymer had a density of 885 885, a melting point of 78 C, a smelting index (MI) of 30 g/μ〇min, and a molecular weight distribution (Mw/Mn) of 2.0. The second component is a crystalline polypropylene having a melt mass flow rate (MFR) of 16 g/1 〇 min ' and a melting point of 160 °C. In the parallel type composite spinning head, the two components are used as the constituent components, and the volume ratio of the first component/second component = 50/50 is 20, and the side of the j component is 20 (TC, the second component side is Fine. c. Extrusion temperature (set temperature) 10 = Ship spinning under conditions. When coiling, make anti-electricity with sorbose riding fatty acid bismuth salt-based ethylene oxide adduct as the main component Attachment. The spinning property is good. Then, the obtained fineness is 1〇. 2 The drinking and the filament are extended by the heating device with the heating view of 6Gt; the crimping imparting device is given the crimping and cutting </ br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br><br> The measurement method of the body mass, t(2), and (5) is used to measure the composition of the melt [= rate (MFR). The results of these tests are shown in Table 1. The outline of the measurement method according to (4) and (7) above. Figure - and shown in Table 1 of the transition Β 2 =: the cross section of the fiber in the direction of the angle == 6. 〇, f &gt; ab, wg obtained composite fiber ( Fiber) investment to 500 mm 31 200934897

i jpn.uuCi jpn.uuC

寬度的小型梳棉機中’採取纖維網。梳棉步驟中的纖 過性良好。針對該纖維網,根據上述(8)的測定方法.通 定熱收縮率。將其結果示於表1的絲質的項目Φ。 則 所獲得的複合纖維(短纖維)投入至500 mm寬产的 ^ 梳棉機中,製成纖維網,然後使用熱風循環式的=風力 機,於設定溫度為98°C、熱風風速為〇.8 m/see、加工 為12 sec的條件下對該些纖維網進行加工。根據上述&gt; B 〜(11)的測定方法,對所獲得的熱風不織布的物^ 測定及評價。將該些的結果示於表丨的不織布物性的項目 使用有所得複合纖維(短纖維)的纖維_熱 達到17%的較低触’故於仙減黏接法的加工中 獲得蓬鬆、且質地及質感良好的不織布。 [實施例3] 第1成分為使用二茂金屬觸媒進行聚合而成的乙 α-婦烴絲物’ α•烯烴為辛烯·卜在絲物中含有5 mol/0。該乙埽· α_烯烴共聚物的密度為〇 炫融指數⑽為3Gg/1Gmin,且分子量分佈為Μη98) :2.1 ° S 2成分是溶體質量流動速率(Mf幻為心 mm、且熔點為16〇°c的結晶性聚丙烯。 以,些兩種成分作為構成成分,使用並列型複合纺絲 八細成分/第2成分=45/55的容積比,且於第1成 〇&lt;:、第2成分側為26〇°C的擠出溫度(設定溫度) 的條件下進㈣融紡絲。卷取時,使以山梨糖騎脂肪酸 32 200934897In the small card of width, 'take the web.' The fiberiness in the carding step is good. The fiber web was subjected to the heat shrinkage rate according to the measurement method of the above (8). The results are shown in the silky item Φ of Table 1. Then, the obtained conjugate fiber (short fiber) is put into a carding machine of 500 mm wide production to form a fiber web, and then a hot air circulation type wind turbine is used, and the set temperature is 98 ° C, and the hot air wind speed is 〇 The webs were processed at .8 m/see and processed for 12 sec. According to the measurement method of the above &gt; B to (11), the obtained hot air non-woven fabric was measured and evaluated. The results of the results of the non-woven fabrics shown in the table are as follows: the fibers of the obtained conjugate fiber (short fiber) have a low touch of 17%, so that the fluffy and texture is obtained in the processing of the smear bonding method. And a non-woven fabric with good texture. [Example 3] The first component was an ethylene-glycolic hydrocarbon product obtained by polymerization using a metallocene catalyst. The α-olefin was octene-containing 5 mol/0 in the filament. The density of the acetamidine α-olefin copolymer is 〇Hybrid index (10) of 3 Gg/1 Gmin, and the molecular weight distribution is Μη98): 2.1 ° S 2 component is the mass flow rate of the solution (Mf is magical mm, and the melting point is Crystallinity polypropylene of 16 〇 °c. The two components are used as a constituent component, and the volume ratio of the side-by-side type composite spinning octagonal component / the second component = 45/55 is used, and the first composition is &lt;: The second component side is fed at a temperature of 26 ° C (set temperature) under the conditions of (four) melt spinning. When coiling, make sorbose riding fatty acid 32 200934897

JUZ/jpil.UW 醋及十二燒基鱗酸鉀鹽的環氧乙烧加成 然後將所獲得的纖度為 =:二使二有:的加熱輥的加熱裝置延伸 #得纖M 賦予捲縮後,切割成38咖, —(纖維徑為25 G㈣的複合纖維(短 ❹ ❹ 針對第1成分,根據上述⑴〜(4 Ϊ二點广融指數(MI)、分子量分佈(Mw/Mn二 動迷率(MFR)。將該些的結果示於表! 、⑺的測定方法來 的剝離。進而t 的纖維截面中未發現成分間 :】: 3.〇,f&gt;abL〇.7〇。 寬产的j型得的複合纖維(短纖維)投入至500職 過:良好。維採取纖維網。梳棉步驟中的纖維通 2維網’根據上述(8)的測定方法來測 =合目中。將-㈣姚*制上、 纖維)投入至500咖寬度的小型 ^於役網’紐使用熱風循環式的熱風加工 瓶速物♦、加工時間 〜(11)的射紐+纖維網進行加工。根據上述(9) 、、’對所獲得的熱風不織布的物性進行 33 200934897 測定及評價。將該些的結果示於表!的不織布物性的項目 中。 使用有所得複合纖維(短纖維)的纖維 達到28%的較低數值,故於利用熱風黏接法的加; 獲得蓬鬆、且質地及質感良好的不織布。 ' [實施例4] ❹ 以與實施例3相同的成分構成,進行相同條件的纺絲 與延伸’以捲縮賦予裝置賦予捲縮後’切割成5酿,择 得纖度為4.4dtex (纖維徑為25.〇㈣ ^ 紡用短纖)。 壤•难、孔 將200 g所獲得的複合纖維(氣紡用短纖) 有-個成對的成型頭(forminghead)的氣紡機 歲、 紡法製成纖維網。纖維自氣纺機中排出的排出性缺 後使用熱風循環式的熱風加工機,於設定溫度為: 風風速為0.38 m/sec、加工時間為14 : 風黏接加工。根據上述⑼〜⑻的測定;= 的熱風不織布的物性進行败及評價。賴些的結 表1的不織布物性的項目中。 σ ; ^所^的複合纖_氣紡法製成纖軸,麟風黏 工’結果可獲得蓬鬆、收縮受到抑制、且質地 及質感良好的不織布。 買 [比較例1] Μ + 成分為乙烯烯烴共聚物,為辛烯,在丘聚 3有2mol%。該乙烯·α-烯烴共聚物的密度為〇 91、二 34 200934897The epoxy Ethylene addition of JUZ/jpil.UW vinegar and the potassium sulphate potassium salt is then obtained. The obtained fineness is =: two is the same as: the heating device of the heating roller is extended. After that, cut into 38 coffee, - (Fiber diameter of 25 G (four) composite fiber (short ❹ ❹ for the first component, according to the above (1) ~ (4 Ϊ two point wide melting index (MI), molecular weight distribution (Mw / Mn two movement The rate of the results (MFR) is shown in Tables and (7). The peeling of the measurement method is not found in the fiber cross section of t::: 3.〇, f&gt;abL〇.7〇. The j-type composite fiber (short fiber) produced is put into the position of 500: good. The fiber is taken from the fiber. The fiber through the 2D mesh in the carding step is measured according to the measurement method of (8) above. Putting - (4) Yao* system, fiber) into a small 500-square-width 于 于 ' 'New hot air circulation type hot air processing bottle speed ♦, processing time ~ (11) injection + fiber mesh processing According to the above (9), and 'the physical properties of the obtained hot air non-woven fabrics are measured and evaluated 33 200934897. The results of these are shown in In the project of non-woven fabric properties, the fiber obtained by using the obtained composite fiber (short fiber) has a low value of 28%, so that it is added by the hot air bonding method; a non-woven fabric having a fluffy texture and a good texture is obtained. Example 4] ❹ The same composition as in Example 3 was carried out, and the spinning and stretching under the same conditions were carried out. After the crimping device was crimped, it was cut into 5 broths, and the fineness was 4.4 dtex (fiber diameter was 25). .〇(4)^Spun staple fiber). The composite fiber obtained from 200 g of the soil and the hole (the staple fiber for air-spinning) has a pair of forming heads of the forming head, and the fiber is made into a fiber. The fiber is discharged from the air-spinning machine and the hot air circulation type hot air processing machine is used. The set temperature is: wind speed is 0.38 m/sec, processing time is 14: wind bonding processing. According to the above (9)~ (8) Measurement; = The physical properties of the hot air non-woven fabric are defeated and evaluated. In the project of non-woven fabric properties of Table 1, σ; ^Comprehensive composite fiber_Air-spinning method for making fiber shaft, Linfeng bonded work' results Can get fluffy, shrinkage is inhibited, Non-woven fabric with good texture and texture. Buy [Comparative Example 1] Μ + The component is an ethylene olefin copolymer, which is octene, and has 2 mol% in the hill poly 3. The density of the ethylene·α-olefin copolymer is 〇91, II. 34 200934897

^&gt;KJ^ / ^pn.uuC =為M1GIC:融指數(MI)為3_min,且分子量 Ιΐ6ε/Γ〇 n 第2成分是熔體質量流動速率(MF10 以該些兩種成分作晶性聚丙烯。 頭,以第1成八t 構成 使用並列型複合紡絲 分侧為 c、第2成 於第1成 的條件下進贿融纺絲 疋溫度) ❹ ❹ 邊界線描繪出向第1成分侧彎曲為凸狀之:線 二卿脚鹽的脂肪酸醋及十 附著。鳴J ί 成物作為主成分的抗靜電劑 者人性良好。然後將所獲得的纖度為11 5 dtex的紡 :=: = ί Μ的,加熱裝置延伸至Μ 度為3.8 dtex (纖唯縮後’ 2成38 mm,獲得纖 針對第=二 成炫點、熔融指數⑽)、分子量分佈(Mw/Mn)。 點、熔體質i 上述(4)、(5)㈣定方絲測定溶 ^率(MFR)。將該些的結果示於表2 的構成成77的項目+。根據上述(6)、(7 測定所獲得的複合纖維(短纖維)的纖維物性。、將ί些的 結果與纖^面的概略圖一併示於表2的絲質的項目^。 進而;在纖維軸成直角的方向的纖維戴㊆中,d 3·5 ’ f&gt;ab ’ 且 g/h=〇 55。 將蘭g所獲得的複合纖維(短纖維)投入至腿 35 200934897^&gt;KJ^ / ^pn.uuC = M1GIC: Melt index (MI) is 3_min, and molecular weight Ιΐ6ε/Γ〇n The second component is the melt mass flow rate (MF10 is crystallized by these two components) Propylene. The head is composed of the first component, and the side-by-side type composite spinning side is c, and the second is formed under the condition of the first one. The boundary line is drawn to the first component side. Bending into a convex shape: fatty acid vinegar and ten attached to the line II. The antistatic agent which is the main component of J J ί is good in human nature. Then, the obtained fineness of 11 5 dtex is sputtered: =: = ί ,, and the heating device is extended to a twist of 3.8 dtex (after the fiber is shortened by '2 to 38 mm, the fiber is obtained for the second=29%, Melt index (10)), molecular weight distribution (Mw/Mn). Point, melt quality i The above (4), (5) (four) square wire was used to determine the dissolution rate (MFR). The results of these results are shown in item + of structure 77 in Table 2. The fiber properties of the conjugate fiber (short fiber) obtained by the above (6) and (7) are measured, and the results of the film are shown together with the outline of the fiber surface in the silk material of Table 2. Further; In the fiber wearing a direction in which the fiber axis is at right angles, d 3·5 ' f &gt; ab ' and g/h = 〇 55. The composite fiber (short fiber) obtained by the blue g is put into the leg 35 200934897

/ jpn.uuC ’採取纖維網。梳棉步驟中的纖維通 …所獲得的L:=:表,質的項 小型梳棉機中,製二峨維)投入至5GG mm寬度的 加工機,於,定、C'祠’然後使用熱風循環式的熱風 ^ 度為98°C、熱風風速為G.8〜卿、加工 蜜:八sec的條件下對該些纖維網進行加工,但因作為/ jpn.uuC ' Take the fiber web. The fiber in the carding step is obtained by using the L:=: table, the quality item of the small carding machine, and the machine is put into the processing machine of 5GG mm width, and then, C'祠' and then used. The hot air circulation type has a hot air temperature of 98 ° C, a hot air wind speed of G.8~qing, and processed honey: eight sec conditions to process the fiber webs, but

工、、田产烯辛烯]共聚物的熔點高,故於98°C的加 本點不會⑽,無法進行不織布化。如此, 記載要是纽點為1(^#方面與上述實施例3 者類㈣除此料基本上彻與該實施例3記載 轨欠勤垃、、進彳亍製造’所獲得者並非可進行在能夠採用 接法之程度的低溫下的不織布化處理或成形加工的 〇&gt;’維。因此預定的以低溫加工為前提的loot下纖維 網的收縮率的評價亦已經失去其測定的意義。 、’ [比較例2] 第1成分為乙烯· 烯烴共聚物,α-烯烴為丙烯與丁 烯自的含量於共聚物中為3 mol%及3 mol%。該乙烯· I烯烴共聚物的紐為0.897,熔點為收,溶融指數 (MI)為4 g/10 min,且分子量分佈(Mw/Mn)為2 〇。 第2成分是熔體質量流動速率(MFR)為8 g/1〇 min、且 熔點為16〇。(:的結晶性聚丙稀。 乂該些兩種成分作為構成成分,使用並列型複合紡絲 頭,以第1成分/第2成分= 50/50的容積比,且於第1成 36 200934897 ❷ =十二烧基磷酸鉀鹽的環氧乙烷加成物作】== 峨―劑附著’但確糊卷取的縣複合長料,產生少量 =。雖發現膠著,但將所獲得的纖度為9 8 dtex的纺絲 複δ長絲使用具有咐的加熱輥的加熱裝置延伸至! 7 ,、’以捲縮賦予裝置賦予捲縮後,切割成38賴,獲得纖 又為6.8 dtex(纖維僅為31 1以爪)的複合纖維(短纖維)。 針對第1成分,根據上述⑴〜⑷的測定方法來 :疋翁度、溶點、溶融指數(MI)、分子量分佈(Mw/Mn)。 對第2成;^ ’根據上述⑷、(5)的測定方法來測定溶 沾、熔體質讀動料(MFR)。將該些的結果示於表2 =成成分_目中。根據上述(6)、⑺的測定方法來 ^疋所獲4的複合纖維(域維)親_性。將該些的 :果與纖維截面的概略圖—併示於表2的絲質的項目中。 第1成刀的溶融指數(MI)低故導致在與纖維轴成直 给^方向的纖維截面中,第1成分與第2成分的邊界線描 1向第2成分侧彎曲為凸狀的曲線。因此,無法測定 c ce ’亦無法測定f、_。另外,發現成分間的剝離。 將100 g所獲得的複合纖維(短纖維)投入至500 mm 4的小型梳棉機中’採取纖賴。因纖維排出性產生不 #故k棉步驟中的纖維通過性不良。針對該纖維網,根 上述的測定方法測定熱收縮率。將該些的結果示於 2的、、糸貝的項目中。將50 g所獲得的複合纖維(短纖維) 37 200934897Since the melting point of the copolymer of the industrial and industrial octene olefins is high, the addition at 98 °C does not (10), and the nonwoven fabric cannot be formed. In this way, if the point is 1 (^# and the above-mentioned embodiment 3 (4), except that the material is substantially inconsistent with the description of the third embodiment, it is not possible to The non-woven treatment at the low temperature or the enthalpy of the forming process at the low temperature is used. Therefore, the evaluation of the shrinkage rate of the fiber under the loot which is premised on the low-temperature processing has lost its meaning of measurement. [Comparative Example 2] The first component is an ethylene/olefin copolymer, and the content of the α-olefin from propylene to butene is 3 mol% and 3 mol% in the copolymer. The bond of the ethylene·I olefin copolymer is 0.897. , melting point is acceptable, the melt index (MI) is 4 g/10 min, and the molecular weight distribution (Mw/Mn) is 2 〇. The second component is the melt mass flow rate (MFR) of 8 g / 1 〇 min, and The melting point is 16 〇. (: crystalline polypropylene. 乂 These two components are used as a constituent component, and a parallel type composite spinning head is used, and the volume ratio of the first component/second component = 50/50 is used. 1成36 200934897 ❷ = ethylene oxide adduct of dodecylphosphoric acid potassium salt as == 峨 剂 agent attachment However, it is true that the composite compound of the county is a small amount of =. Although it is found to be glued, the obtained spinning complex δ filament having a fineness of 98 dtex is extended to a heating device with a heating roller of 咐 to 7; After the crimping device is crimped, it is cut into 38 sheets, and a composite fiber (short fiber) having a fiber of 6.8 dtex (fiber is only 31 1 claw) is obtained. For the first component, according to the above (1) to (4) The measurement method is: 疋 度 degree, melting point, melting index (MI), molecular weight distribution (Mw / Mn). For the second formation; ^ ' according to the above (4), (5) measurement method to determine the dissolution, melt quality The material (MFR) was read. The results of the above were shown in Table 2 = component. The composite fiber (domain dimension) obtained by the above (6) and (7) was used. These are: a schematic view of the cross section of the fruit and the fiber - and are shown in the silk item of Table 2. The melting index (MI) of the first forming knife is low, resulting in a fiber cross section in the direction of the fiber axis. In the middle, the boundary line 1 of the first component and the second component is curved toward the second component side in a convex shape. Therefore, it is impossible to measure c ce ' It was not possible to measure f and _. In addition, peeling between the components was found. 100 g of the obtained conjugate fiber (short fiber) was put into a small card of 500 mm 4 to take the fiber. The fiber passability in the k-cotton step was poor. The heat shrinkage rate was measured for the fiber web by the above-described measurement method. The results of the above were shown in the item of mussels of 2, and 50 g of the obtained composite fiber. (short fiber) 37 200934897

/ ^pix.uuC 才又入至500 mm寬度的小型梳棉機中,製成纖維網然後 使用熱風循環柄熱風加卫機,於設定溫度為98°C、熱風 風速,0.8m/sec、加工時間為12sec的條件下對該些纖維 網,行加工’但收縮大’不織布強度低,無法獲得質地、 質感良好的不織布。使时所得複合纖_纖_的熱收 縮率高達55%。 [比較例3]/ ^pix.uuC is then inserted into a small card of 500 mm width, made into a fiber mesh and then hot air circulation handle hot air elevator, at a set temperature of 98 ° C, hot air wind speed, 0.8 m / sec, processing When the time was 12 sec, the webs were processed, but the shrinkage was large, and the non-woven fabric was low in strength, and a non-woven fabric having a good texture and texture could not be obtained. The heat shrinkage rate of the obtained composite fiber_fiber_ was as high as 55%. [Comparative Example 3]

第1成分為乙烯.α_烯烴共聚物,烯烴為丙烯,在 厂,物中含有15 m〇1%。該乙烯心稀烴共聚物的密度為 心3旦溶點為5『C ’熔融指數(MI)為21 g/l〇 min,且 刀佈(Mw/Mn)為2.0。第2成分是熔體質量流動 、、“(MFR)為16g/1〇min、且炫點為16〇。[的結晶性 丙稀。 以該些兩種成分作為構成成分,使用並列型複合 頭:第/成分/第2成分=50/50的容積比,且於第】成分 、第2成分侧為26(rc的擠出溫度(設定溫度) 紡絲。然而,卷取時’紡絲複合長絲產 妒二本;ί採進行延伸的紡絲複合長絲。關於該比 記載的纖維截面的示意圖是自膠著的複合紡 j長、社娜而進行觀絲獲得的。因第丨成分的溶融指 數(MI)相對於第2成分的熔體質量流動速率(MFR)而 ^意地較低,故在與纖維軸成直角的方向的纖維截面中, 土 η:與第2成分的邊界線為直線 合成分均為半月狀的複合截面。在與纖維軸成直角的方向 38 200934897The first component is an ethylene.α-olefin copolymer, and the olefin is propylene, and the plant contains 15 m〇1%. The density of the vinyl dilute copolymer was a core 3 denier of 5 "C" melt index (MI) of 21 g/l 〇 min and a knife cloth (Mw/Mn) of 2.0. The second component is a melt mass flow, "(MFR) is 16 g / 1 〇 min, and the bright point is 16 〇. [Crystal propylene. Using these two components as a constituent component, using a parallel type composite head : The volume ratio of the /component/second component=50/50, and 26 (the extrusion temperature (set temperature) of the rc component and the second component side are spun. However, when winding, the spinning composite Two filaments are produced; the spinning composite filaments are stretched. The schematic diagram of the fiber cross-sections of the ratio is obtained by the self-adhesive composite spinning, and the silk is obtained by the silk. Since the melt index (MI) is lower than the melt mass flow rate (MFR) of the second component, the boundary between the soil η: and the second component is in the fiber cross section in a direction perpendicular to the fiber axis. The linear composite is a half-moon composite cross section at a right angle to the fiber axis 38 200934897

/ ^pij..uuC 的織=:AC,0,且複合成分間發現剝離。 測定密声、心、根據上述⑴〜⑷的測定方法來 針對第。分,分子量分佈(Mw/Mn)。 的構成成=二速率(職)。將該些的結果示於表2 [比較例4]/ ^pij..uuC weave =: AC, 0, and peeling was found between the composite components. The measurement of the dense sound and the heart is carried out according to the measurement methods of the above (1) to (4). Points, molecular weight distribution (Mw / Mn). The composition is == two rate (job). The results of these are shown in Table 2 [Comparative Example 4]

OO

胸匕合有兩種樹脂而成者作為第1成分。其中一種 ㈣煙共聚物1·稀烴為丙烯,在共聚物中 該乙烯.心烯煙共聚物的密度為0.870,熔 點為75 C,㈣指數(ΜΙ)為丨g/1Qmin,且分子量分佈 MW/Mn)為1·9°另—種樹脂為丙:#·α·烯烴共聚物, 烴為乙馳了烯],該細.㈣含量在共聚物中 =1 mol/。。該丙烯.α_烯烴共聚物的熔點為128。〇,且 熔體^流動鱗(MFR)為16g/1Gmin。㈣兩種樹脂 以重量比為20/80的比例摻合。而且,表2中記載熔點更 =的樹脂即乙烯·丙烯共聚物的物性。第2成分是熔體質量 机動速率(MFR)為8g/l〇min、且溶點為16〇。〇的結晶性 聚丙烯。 以該些兩種成分作為構成成分,使用並列型複合纺絲 頭,以第1成分/第2成分= 50/50的容積比,且於第i成 分側為200 C、第2成分側為260°C的擠出溫度(設定溫度) 的條件下進行熔融紡絲,製造具有第丨成分與第2成分的 邊界線描繪出向第1成分侧彎曲為凸狀之曲線的纖維戴面 39 200934897The chest is combined with two kinds of resin as the first component. One of the (four) smoke copolymers 1 · a dilute hydrocarbon is propylene. In the copolymer, the density of the ethylene-ene olefin copolymer is 0.870, the melting point is 75 C, and the index (ΜΙ) is 丨g/1Qmin, and the molecular weight distribution is MW. /Mn) is 1·9° The other resin is C: #·α·olefin copolymer, the hydrocarbon is acetylene], and the content of the fine (4) is =1 mol/ in the copolymer. . The propylene.α-olefin copolymer has a melting point of 128. 〇, and the melt flow scale (MFR) is 16 g / 1 Gmin. (4) The two resins were blended in a weight ratio of 20/80. Further, in Table 2, the physical properties of the ethylene/propylene copolymer which is a resin having a higher melting point are described. The second component was a melt mass having a maneuvering rate (MFR) of 8 g/l 〇 min and a melting point of 16 Å. Crystallization of bismuth Polypropylene. The two-component composite spinneret is used as the constituent component, and the volume ratio of the first component/second component = 50/50 is 200 C on the i-th component side and 260 on the second component side. Melt-spinning was carried out under the conditions of an extrusion temperature (set temperature) of °C, and a fiber-lined surface in which a boundary line between the second component and the second component was drawn and curved toward the first component side was produced.

/ ^pn.uuC 、、、《構的複σ纖維。卷取時,使以山梨糖醇軒脂肪酸醋及十 二,基磷酸㈣崎氧乙餘成物作為域分的抗靜電劑 附著。纺絲性良好。然後將所獲得的纖度為9.7 dtex的紡 4複a長絲使肖具有6〇°c的加熱輥的力置延伸至2 6 倍、,以捲縮賦予裝置賦予捲縮後,切割成38 mm,獲得纖 度為4.4dtex(纖維徑為251 〃m)的複合纖維(短纖維)。 ❹ ❹ 針對第1成分,根據上述⑴〜⑷的測定方法來 測定密度、溶點、溶融指數(ΜΙ)、分子量分佈(Mw/Mn)。 針對第2成分’根據上述⑷、(5)的測定方法來測定溶 點、熔體質量流動速率(MFR)。將該些的結果示於表2 的構成成分的項目中。根據上述⑷、⑺的測定方法來 測定所獲得的複合纖維(短齡)的纖 結果與纖維截面的概略圖-併示於表2的絲質的=;的 而且,在與纖維軸成直角的方向的纖維載面 0.2,且 g/h&lt;〇.5。 — u叉Wtr、J饭S纖难I姐纖維)投入至 寬度的小型梳棉機中,採取纖維網。梳棉步驟中的纖維赶 過性良好。針對所獲得的纖維網,根據上述(8)的測定2 法來測定熱收_。將該些的結果祕表2的絲質的項g ί二=:斤獲得的複合纖維(短纖維)投入至500咖 寬度的小雜棉機中,製成纖維網,然後使用熱風 的熱風加工機’於設定温度為98〇C、熱風風迷為7 m/sec、加工時間為12 sec的條件下對該些纖維網办 工,但收縮大,無紐得質地、質感良好的不織布 200934897/ ^pn.uuC , , , "The complex σ fiber. At the time of coiling, an antistatic agent containing sorbitol sulfonate fatty acid vinegar and a bismuth phosphite (4) sulphur oxyethylene residue was attached as a domain. Spinnability is good. Then, the obtained spun 4 a-filament having a fineness of 9.7 dtex was used to extend the force of the heating roller having a diameter of 6 ° C to 26 times, and after being crimped by the crimping device, it was cut into 38 mm. A composite fiber (short fiber) having a fineness of 4.4 dtex (fiber diameter of 251 〃m) was obtained. ❹ ❹ For the first component, the density, the melting point, the melting index (ΜΙ), and the molecular weight distribution (Mw/Mn) were measured according to the measurement methods (1) to (4) above. The melting point and the melt mass flow rate (MFR) of the second component were measured according to the measurement methods of the above (4) and (5). The results of these are shown in the items of the constituent components of Table 2. According to the measurement methods of the above (4) and (7), the fiber results of the obtained conjugate fiber (short age) and the fiber cross-section are measured and shown in Table 2, and at a right angle to the fiber axis. The direction of the fiber loading surface is 0.2, and g/h &lt; 〇.5. — u fork Wtr, J rice S fiber difficult I sister fiber) into the small card of the width, take the fiber mesh. The fiber in the carding step is good in transit. The heat recovery _ was measured according to the measurement 2 method of the above (8) with respect to the obtained fiber web. The result of the results of the silky item g ί 2 =: the conjugate fiber obtained by the kg (short fiber) is put into a small coffee machine of 500 coffee width, made into a fiber web, and then processed by hot air. The machine's work on these fiber webs under the conditions of a set temperature of 98 〇C, a hot air fan of 7 m/sec, and a processing time of 12 sec, but the shrinkage is large, and the non-woven fabric with good texture and good texture is 200934897.

f ^pn.uuC 有所得複合纖維的纖維網的熱收縮率高達65%。 [比較例5] 使用摻合有兩種樹脂而成者作為第1成分。其中一種 樹脂為低密度聚乙烯。該低密度聚乙烯的密度為〇918, 熔點為105°C,熔融指數(MI)為24g/1〇 min,且分子量 分佈為7.0。另一種樹脂為乙烯_乙酸乙烯酯共聚物。乙酸 乙缔醋量為2G wt%,該乙烯乙酸乙_旨共聚物的密度為 0.939 ’熔點為92°C,熔融指數(MI)為2〇 g/1〇 min,且 分子置分佈(Mw/Mn)為5.0。將該兩種樹脂以重量比為 75/25的_摻合。而且,表3巾記㈣點更低的樹脂即 乙婦-乙酸乙_共聚物的物性。第2成分是熔體質量流動 速率(MFR)為8g/l〇min、且熔點為16〇〇c的結晶性聚 烯。 以該些兩種成分作為構成成分,使用並列型複合纺絲 頭’以第1成分/第2成分=50/50的容積比’且於 ❹ C、第2成分側為·。c的擠出溫度(設定溫度成) =件下進彳了賴_,製造具有第丨成分與第2成分的 邊界線描繪出向第i成分侧f曲為凸狀之 結= 纖維。卷取時,使以山梨糖醇軒二=: 環氧乙烧加成物作為主成分的抗靜電劑 附者。紡絲時產生較多斷線情況。然 劑 複合長絲使用具有為裝 置(伸至2.6倍’轉_予裝置_捲 ^ mm,獲得纖度為3.3 dtex (纖維徑為 刀。J成38 以》1)的複合纖 200934897 維(短纖維)。 針對第1成分,根據上述〜 、— 測定密度、溶點、溶融指數(MI)、分 的測定方法來 針對第2成分,根據上述(4)、( 量^刀佈(Mw/Mn)。 ❹ 點、熔體質量流動速率(MFR)。將蜂^疋方法來測定熔 的構成成分的項目中。根據上述(=f的結果示於表3 測定所獲得職合纖維(短^败方法來 結果與纖維截面的概略圖一併示於矣、'、、' 物性。將該些的 而且’在與纖維軸成直角的方向的的:質的項目中。 9.5,f〉ab,且 g/h=0.86。 I唯戴面中 ’ cd/ce = 將100 g所獲得的複合纖維(短 寬度的小型梳棉機中,採取纖維網。、=曼入至500 mm 生不均,故梳棉步驟中的纖維通過,纖維的排出中產 纖維網’根據上it (8)的測定方法來^二針對所獲得的 些的結果示於表3的絲質的項目中。將1、、、收縮率。將該 纖維(短纖維)投入至5〇〇 _ 沾50請獲得的複合 成纖維網,然:後使用熱風循環式棉機中’製 度為阶、熱風風速為G 8…财、加工=機,於設定溫 件下對該些纖維網進行加工,但 、㈢為12 sec的條 質感良好的不織布。 —縮大,無法獲得質地、 ,用有所得複合纖維的纖維網的 [比較例6] 、、收縮率回達60〇/〇。 以與比較例5相同的成分構成, 與延伸,以捲縮賦予裳置賦予捲縮後,件的纺絲 又丨刀割成5 mm,獲 42 200934897f ^pn.uuC The fiber web of the obtained composite fiber has a heat shrinkage rate of up to 65%. [Comparative Example 5] A mixture of two kinds of resins was used as the first component. One of the resins is low density polyethylene. The low density polyethylene had a density of 〇918, a melting point of 105 ° C, a melt index (MI) of 24 g / 1 〇 min, and a molecular weight distribution of 7.0. Another resin is an ethylene-vinyl acetate copolymer. The amount of ethyl acetate was 2 G wt%, the density of the ethylene acetate copolymer was 0.939 'melting point was 92 ° C, the melt index (MI) was 2 〇g / 1 〇 min, and the molecular distribution (Mw / Mn) is 5.0. The two resins were blended in a weight ratio of 75/25. Further, in Table 3, the lower limit of the resin (4) is the physical properties of the ethyl-acetate copolymer. The second component is a crystalline polyolefin having a melt mass flow rate (MFR) of 8 g/l 〇 min and a melting point of 16 〇〇c. The two components are used as the constituent components, and the parallel type composite spinning head is used in the volume ratio of the first component/second component = 50/50 and is on the side of the ❹ C and the second component. The extrusion temperature of c (the set temperature is) = the boundary line of the second component and the second component is produced, and the knot = fiber which is convex toward the i-th component side is drawn. When taking up, an antistatic agent containing sorbitol Xuanji =: Ethylene oxide blended adduct as a main component is attached. More wire breakage occurs during spinning. The compound composite filament is used as a device (extending to 2.6 times 'transfer_pre-device_roll^mm, obtaining a fineness of 3.3 dtex (fiber diameter is a knife. J into 38 to 1)) composite fiber 200934897 dimension (short fiber) For the first component, the second component is determined according to the measurement method of the density, the melting point, the melting index (MI), and the measurement according to the above-mentioned (4), (Mw/Mn). ❹ Point, melt mass flow rate (MFR). The bee method is used to determine the constituent components of the melt. According to the above (=f results are shown in Table 3, the obtained composite fibers are determined. The results are shown together with the outline of the fiber cross-section in the physical properties of 矣, ', and '. These are also in the qualitative direction of the fiber axis. 9.5, f>ab, and g /h=0.86. I only wear the surface 'cd/ce = 100g of the composite fiber obtained (in the short-width small card, take the fiber mesh., =Man into 500 mm, uneven, so comb The fiber in the cotton step passes, and the fiber is discharged from the middle fiber web' according to the measurement method of it (8). The results are shown in the silky item of Table 3. The shrinkage ratio is 1, and the fiber (short fiber) is put into a composite fiber web obtained by 5 〇〇 _ 50. In the hot air circulation type cotton machine, the system is a step, the hot air speed is G 8 ..., processing = machine, the fiber web is processed under the set temperature, but (3) is a non-woven fabric with good texture of 12 sec. When the texture was increased, the texture of the fiber web obtained with the obtained composite fiber was not obtained, and the shrinkage ratio was 60 〇/〇. The composition was the same as that of Comparative Example 5, and the film was stretched and given by crimping. After the skirt was given the curl, the spinning of the piece was cut into 5 mm and won 42 200934897

jpu.UOC ^i)3;3dtexc^ 有-所獲得的複合纖維(氣__)投入至具 網,纖^成型獅氣賴巾,_1紡法製成纖維 中=定的好C。紐使用熱風循 m/sec、Λ ^機、 度為98 C、熱風風速為0.38 ❹ ❹ 熱風14 ^的條件下對所獲得的纖維網進行 = ::,雖然可進行該_下的熱風黏接,繼 3中。…、法獲得質地、質感良好的不織布。將結果示於表 [實施例5] ㈣1!施例3中獲得的複合纖維(短纖維)以梳棉法製 該纖維網製成棒狀的纖維束。將製成纖維束 张制1、、充至以線徑為0.29 mm的20網目之金屬絲網 所^的^狀模具(1Gmmxl()mmx6()mm)中,於此狀態 ^用循環式的熱風加卫機,於設定溫度為攸、熱風風jpu.UOC ^i) 3; 3dtexc^ Yes - The obtained composite fiber (gas __) is put into the net, the fiber is formed into a lion gas, and the fiber is made into a fiber. The new fiber is subjected to hot air circulation m/sec, Λ^ machine, degree 98 C, hot air wind speed of 0.38 ❹ ❹ hot air 14 ^ under the condition of the obtained fiber web = ::, although the hot air bonding can be performed under the _ , following 3 in. ..., the law obtains a non-woven fabric with good texture and texture. The results are shown in the table. [Example 5] (IV) 1! The conjugate fiber (short fiber) obtained in Example 3 was formed into a rod-shaped fiber bundle by a carding method. The fiber bundle is made into 1, and is filled into a ^-shaped mold (1Gmmxl() mmx6() mm) of a 20 mesh wire mesh having a wire diameter of 0.29 mm, and in this state, a cyclic type is used. Hot air plus guard, set the temperature to 攸, hot wind

Um^sec、加工時間為128忧的條件下進行熱風黏接 σ工’獲*長方錄的晴成频。哺得的麟成形體 的減震性優異。 [實施例6] 使用實施例4中獲得的複合纖維(氣纺用短纖),以 氣纺法製成單位面積重量為5G g/m2__,使用循環 式的熱風加機,麟定温度為阶、熱風風速為Ο% m/sec加工%間為14 sec的條件下對該纖維網進行熱風黏 43 200934897Um^sec, the processing time is 128, and the hot air bonding is performed under the condition that the σ work is obtained. The lining body that is fed has excellent shock absorbing properties. [Example 6] Using the conjugate fiber (air-spun staple fiber) obtained in Example 4, the basis weight was 5 G g/m2__ by air spinning, and the circulating hot air machine was used. The hot air wind speed is 热% m/sec and the processing time is 14 sec. The hot air viscosity is applied to the fiber web 43 200934897

J\J^ / ^pn.uuC 接加工。將所獲得的熱風不織布填充至内徑為8 mm的玻 璃管中,於此狀態下直接放入沸水中,煮沸2分鐘。煮沸 後’使之冷卻,獲得圓柱狀的纖維成形體。所獲得的纖維 成形體的柔軟適度,纖維密度的不均較少,適於液體的保 液等。J\J^ / ^pn.uuC is processed. The obtained hot air non-woven fabric was filled in a glass tube having an inner diameter of 8 mm, and directly placed in boiling water in this state, and boiled for 2 minutes. After boiling, it was allowed to cool to obtain a cylindrical fibrous formed body. The obtained fiber molded body is soft and moderate, and has a small unevenness in fiber density, and is suitable for liquid retention of liquids and the like.

44 200934897 ^υζ/Dpn.aoc [表1]44 200934897 ^υζ/Dpn.aoc [Table 1]

實施例1 實施例2 實施例3 實施例4 構成 成分 第1 成 分 使用樹脂 乙烯·辛烯·1 共聚物 乙烯*辛稀-1 共聚物 乙烯·辛烯·1 共聚物 乙烯·辛烯-1 共聚物 密度(g/cm3) 0.880 0.885 0.902 0.902 熔點(°C) 72 78 98 98 熔融指數 (g/10 min) 18 30 30 30 分子量分佈 1.9 2.0 2.1 2.1 第2 成 分 使用樹脂 聚丙烯 聚丙稀 聚丙烯 聚丙烯 熔體質量流動 速率(g/10min) 8 16 16 16 熔點(°c) 160 160 160 160 紡絲 條件 擠出;1 (第 幾設定溫度(°c) 1成分/第2成分) 200/260 200/260 200/260 200/260 紡絲纖度(dtex) 6.5 10.2 10.0 10.0 延伸 條件 加熱裝置(加熱棍) 設定溫度(°C) 55 60 70 70 延伸倍率 1.7 1.7 2.6 2.6 絲質 纖度(dtex) 4.4 7.0 4.4 4.4 切割長度(mm) 38 38 38 5 纖維載面 © ③ ③ ③ 周面之長度 (第1成分)(%) 85 80 75 75 纖維網熱收縮率(%) 15 17 28 — 不織 布物 性 不織布化(加工溫度 設定為98°C ) 可 可 可 可 單位面積重量(g/m2) 50 50 50 50 比容積(cnrVg) 30 34 38 30 質感 良好 良好 良好 良好 45 200934897 ^υζ/^pii.aoc [表2]Example 1 Example 2 Example 3 Example 4 Component Component The first component used was a resin ethylene·octene·1 copolymer ethylene*octyl-1 copolymer ethylene·octene·1 copolymer ethylene·octene-1 copolymer Material density (g/cm3) 0.880 0.885 0.902 0.902 Melting point (°C) 72 78 98 98 Melt index (g/10 min) 18 30 30 30 Molecular weight distribution 1.9 2.0 2.1 2.1 The second component uses resin polypropylene polypropylene polypropylene Propylene melt mass flow rate (g/10min) 8 16 16 16 Melting point (°c) 160 160 160 160 Spinning condition extrusion; 1 (several set temperature (°c) 1 component/component 2) 200/260 200/260 200/260 200/260 Spinning fineness (dtex) 6.5 10.2 10.0 10.0 Extended condition heating device (heating rod) Setting temperature (°C) 55 60 70 70 Extension ratio 1.7 1.7 2.6 2.6 Silk denier (dtex) 4.4 7.0 4.4 4.4 Cutting length (mm) 38 38 38 5 Fiber surface © 3 3 3 Length of the circumference (Part 1) (%) 85 80 75 75 Web shrinkage (%) 15 17 28 — Non-woven fabric non-woven (Processing temperature is set to 98 ° C) Cocoa Weight per unit area (g/m2) 50 50 50 50 Specific volume (cnrVg) 30 34 38 30 Good texture Good Good Good 45 200934897 ^υζ/^pii.aoc [Table 2]

比較例1 比較例2 比較例3 比較例4 第 使用樹脂 ()内為混合 比率[wt%] 乙稀·辛烯 -1共聚物 乙稀,丙稀· 丁烯-1共聚 物 乙稀·丙稀 共聚物 乙烯·丙烯共聚物 (20) +丙稀乙稀· 丁烯-1共聚物(80) 1 密度(g/cm3) 0.913 0.897 0.863 0.870 構 成 成 分 成 熔點rc) 107 81 50 75 分 熔融指數 (g/10 min) 30 4 21 1 分子量分佈 3.0 2.0 2.0 1.9 第 2 成 分 使用樹脂 聚丙烯 聚丙烯 聚丙烯 聚丙烯 熔體質量流動 速率(g/10 min) 16 16 16 8 熔點(°C) 160 160 160 160 紡 絲 條 件 擠出機設定溫度 (°C) (第1成分/第2成 分) 200/260 220/260 220/260 200/260 纺絲纖度(dtex) 11.5 9.8 無法採取 9.7 延 伸 加熱裝置(加熱輥) 設定溫度(°C) 70 60 — 70 條 件 延伸倍率 3.3 1.7 — 2.6 纖度(dtex) 3.8 6.8 — 4.2 切割長度(mm) 38 38 — 38 絲 質 纖維截面 ③ ① 0 ① 周面之長度 (第1成分)(%) 70 40 50 55 纖維網熱收縮率 (%) 1 55 — 65 不 織 布 物 性 不織布化(加工溫度 設定為98°C ) 並不黏接, 無法採取 收縮大 — 收縮大 單位面積重量 (咖2) — — — — 比容積(cnrVg) — — — — 質感 — 差 — 差 46 200934897 [表3] 比較例5 比較例6 構成 成分 第1 成分 使用樹脂 Ο内為混合比率 fwt%l 乙烯.乙酸乙烯酯共聚物 (25)+低密度聚乙烯(75) 乙烯.乙酸乙烯酯共聚物 (25)+低密度聚乙烯(75) 密度(g/cm3)__ 0.940 0.940 熔點(°c) 92 92 熔融指數 (g/10 min) 20 20 分子量分佈 5.0 5.0 第2 成分 使用樹脂 t 聚丙烯 聚丙烯 熔體質量流動速 率(g/10min) 8 8 熔點(°c) 160 160 紡絲 條件 擠出相 (第1 1設定溫度(°C) 1 成分/第2成分) 200/260 200/260 紡絲缄度(dtex) 7.2 12 延伸 條件 加熱裝置(加熱輕) 設定溫度(°c) 70 70 延伸倍率 2.6 2.6 絲質 纖度(dtex) 3.5 3.5 切割長度(mm) 38 5 織維裁面 © ③ 周面之長度 (第1成分)(%) 90 90 纖維網熱收縮率(%) 60 — 不織 布物 性 L—- 不織布化 (加工溫度設定為98°C) 收縮大 收縮大 單位面積重量(g/m2) 一 — 比容積(cm3/g) — — 質感 差 差Comparative Example 1 Comparative Example 2 Comparative Example 3 Comparative Example 4 The resin () used was a mixing ratio [wt%] Ethylene·octene-1 copolymer ethylene, propylene·butene-1 copolymer ethylene·c Dilute copolymer ethylene·propylene copolymer (20) + propylene vinyl · butene-1 copolymer (80) 1 density (g/cm3) 0.913 0.897 0.863 0.870 constituents into melting point rc) 107 81 50 75 minute melt index (g/10 min) 30 4 21 1 Molecular weight distribution 3.0 2.0 2.0 1.9 The second component uses resin polypropylene polypropylene polypropylene polypropylene melt mass flow rate (g/10 min) 16 16 16 8 melting point (°C) 160 160 160 160 Spinning conditions Extruder set temperature (°C) (Part 1 / 2nd component) 200/260 220/260 220/260 200/260 Spinning fineness (dtex) 11.5 9.8 Cannot take 9.7 extension heating device (Heating roller) Setting temperature (°C) 70 60 — 70 Conditional extension ratio 3.3 1.7 — 2.6 Fineness (dtex) 3.8 6.8 — 4.2 Cutting length (mm) 38 38 — 38 Silk fiber section 3 1 0 1 Length of circumference (Part 1) (%) 70 40 50 55 Fiber web heat shrinkage rate ( %) 1 55 — 65 Non-woven fabric non-woven (processing temperature is set to 98 ° C) Does not stick, can not take large shrinkage - shrink large unit weight (coffee 2) — — — — specific volume (cnrVg) — — — — Texture — Poor — Poor 46 200934897 [Table 3] Comparative Example 5 Comparative Example 6 Component Component The first component used in the resin was a mixing ratio fwt%l ethylene. Vinyl acetate copolymer (25) + low density polyethylene (75) Ethylene. Vinyl acetate copolymer (25) + low density polyethylene (75) Density (g/cm3) __ 0.940 0.940 Melting point (°c) 92 92 Melt index (g/10 min) 20 20 Molecular weight distribution 5.0 5.0 2 Ingredients used resin t Polypropylene polypropylene Melt mass flow rate (g/10min) 8 8 Melting point (°c) 160 160 Spinning conditions Extrusion phase (1st set temperature (°C) 1 Component / 2nd component 200/260 200/260 Spinning twist (dtex) 7.2 12 Extended condition heating device (light heating) Setting temperature (°c) 70 70 Extension ratio 2.6 2.6 Silk denier (dtex) 3.5 3.5 Cutting length (mm) 38 5 Weaving dimension © 3 The length of the circumference (No. 1 component) (%) 90 90 Fiber web heat shrinkage rate (%) 60 - Non-woven fabric property L - Non-woven (processing temperature is set to 98 ° C) Shrinkage large shrinkage large basis weight (g/m2) I - specific volume (cm3/g) — — texture difference

[產業上之可利用性] 本發明的複合纖維是由含有具有特定性質的乙烯.α_ ^烴共聚物的第1成分與含有結晶性丙2成分構成 κΐϋπ/· 纖維具有低溫加工性,熱收縮率低, ' 或loot:以下的熱處理溫度下製造蓬鬆 47 200934897 ^υζ/^pn.aoc 質=炒質感良好的不織布及成形體而言較為有用。 本發明露如上,然其並非用以限定 本發明之料^ 領域巾具有料知識者,在不脫離 發明之银^圍内,當可作些許之更動與潤飾, ❹ 後附之申請專利範圍所界定者為準 概略Ξ。1為表示本發明的複合纖維的並列型截面 【主要元件符號說明】 無。 故本 的形狀的[Industrial Applicability] The conjugate fiber of the present invention is composed of a first component containing an ethylene.α_^ hydrocarbon copolymer having a specific property and a component containing a crystalline propylene 2 component, and has a low-temperature processability and heat shrinkage. The rate is low, ' or loot: the following heat treatment temperature is made of fluffy 47 200934897 ^υζ/^pn.aoc quality = non-woven fabric and molded body with good texture. The present invention is as described above, but it is not intended to limit the knowledge of the material of the present invention, and may be modified and retouched without departing from the silver of the invention. The definition is based on the outline. 1 is a side-by-side cross section showing the conjugate fiber of the present invention. [Description of main component symbols] None. The shape of the book

G 48G 48

Claims (1)

200934897 JU2/spit.a〇c 七、申請專利範圍: L一種複合纖維’其是由含有至少75 wt%的熔點為7〇 〜loop的乙烯.a •烯烴共聚物的第丨成分、與含有結晶性 聚丙烯的第2成分構成並列型截面而成,該複合纖維的特 徵在於:在與纖維軸成直角的纖維截面中,第1成分占纖 、維外周的55〜90%,第1成分與第2成分的邊界線描緣出 向第1成分侧彎曲為凸狀的曲線,並且第丨成分與第2成 分的面積比率(第1成分/第2成分)為70/30〜30/70的範 罾圍。 2·如申請專利範圍第1項所述之複合纖維,其中乙烯· a-烯煙共聚物的分子量分佈(Mw/Mn)為ι5〜2.5,密度 為0.87〜0.91 g/cm3,並且基於ASTMD_1238且於溫度為 190°C、負荷為21.2 N的條件下所測定的熔融指數(MI) 為 10〜35 g/10 min。 3. 如申請專利範圍第1項或第2項所述之複合纖維, 其中於100°C下進行5分鐘熱處理後的熱收縮率為小於等 Q 於 50%。 4. 一種不織布’其是對如申請專利範圍第1項至第3 項中任一項所述之複合纖維進行不織布化處理而獲得。 ’ 5.如申請專利範圍第4項所述之不織布,其中不織布 化處理為熱風黏接法或熱水黏接法。 6. —種成形體’其是使用如申請專利範圍第1項至第 3項中任一項所述之複合纖維而獲得。 7. —種成形體’其是使用如申請專利範圍第4項或第 49 200934897 5項所述之不織布而獲得。200934897 JU2/spit.a〇c VII. Patent application scope: L A composite fiber which is composed of a ruthenium component containing at least 75 wt% of ethylene. The second component of the polypropylene is formed into a side-by-side cross section, and the conjugate fiber is characterized in that the first component occupies 55 to 90% of the outer circumference of the fiber cross section at right angles to the fiber axis, and the first component and the first component are The boundary line of the second component is curved in a convex shape toward the first component side, and the area ratio (first component/second component) of the second component to the second component is 70/30 to 30/70. Wai. 2. The composite fiber according to claim 1, wherein the ethylene·a-olefinic copolymer has a molecular weight distribution (Mw/Mn) of ι 5 to 2.5, a density of 0.87 to 0.91 g/cm 3 , and is based on ASTM D_1238 The melt index (MI) measured under the conditions of a temperature of 190 ° C and a load of 21.2 N was 10 to 35 g/10 min. 3. The composite fiber according to claim 1 or 2, wherein the heat shrinkage rate after heat treatment at 100 ° C for 5 minutes is less than or equal to 50%. A non-woven fabric which is obtained by subjecting a conjugate fiber according to any one of claims 1 to 3 to a non-woven fabric. 5. The non-woven fabric of claim 4, wherein the non-woven fabric is a hot air bonding method or a hot water bonding method. 6. A molded body, which is obtained by using the conjugate fiber according to any one of claims 1 to 3. 7. A shaped body' obtained by using a non-woven fabric as described in claim 4 or 49 200934897. 5050
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