TW580527B - Stretchable fibers of polymers, spinnerets useful to form the fibers, and articles produced therefrom - Google Patents

Stretchable fibers of polymers, spinnerets useful to form the fibers, and articles produced therefrom Download PDF

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Publication number
TW580527B
TW580527B TW090124143A TW90124143A TW580527B TW 580527 B TW580527 B TW 580527B TW 090124143 A TW090124143 A TW 090124143A TW 90124143 A TW90124143 A TW 90124143A TW 580527 B TW580527 B TW 580527B
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Taiwan
Prior art keywords
polymer
spinneret
core
fiber
wing
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TW090124143A
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Chinese (zh)
Inventor
Garret Daniel Figuly
Anthony J Soroka
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Du Pont
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    • 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
    • D01F8/12Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyamide 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
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/253Formation of filaments, threads, or the like with a non-circular cross section; Spinnerette packs therefor
    • 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
    • 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
    • D01F8/14Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyester as constituent
    • 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
    • D01F8/16Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one other macromolecular compound obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds as constituent

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Multicomponent Fibers (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
  • Artificial Filaments (AREA)

Abstract

A stretchable synthetic polymer fiber comprising an axial core formed from an elastomeric polymer, and two or more wings attached to the core and formed from a non-elastomeric polymer, wherein preferably at least one of the wings is mechanically locked with the axial core. The fibers can be used to form garments, such as hosiery. A spinneret pack for producing such fibers is also provided.

Description

本發明係關於一種可伸展合成聚合物纖維 =性彈=物之轴芯及複數個包含熱塑性:、非::; 合物外!^徑向隔開之翼。翼聚合物或芯聚 著太二y Λ出土另一聚合物内’而改良翼對芯之附 月亦關於此種纖維之製法’及有用於形成纖維之 、、封裝。本發明關於由此纖維形成之物件,包括处 、衣物、及其類似物。 ^ 4希望賦予由合成纖維形成之許多產品,包括各種衣物, 諸如運動服及針織品可伸展性。如揭示於發證給之 國專利第4,861,660號之背景段落中,已知各種賦予合成長 柯伸展性《万法。在其中—種方法中,將纖維予以二或 三維蜷縮。在另一此種方法中,由彈性聚合物,例如,天 j或口成橡膠、或合成彈性體諸如聚胺甲酸酯彈性體,製 1可伸展長絲。此類型之可伸展長絲之缺點在於該橡膠或 聚胺甲酸酯彈性長絲之本身展現非常差之穿戴及針織加工 f與不良足染色性質。因此,聚胺甲酸酯彈性體長絲之橡 膠的缺點可經由將橡膠或彈性長絲覆蓋具有令人滿意之加 工性及染色牲質之另一類型長絲而避免。 然而’此種覆蓋彈性長絲具有相關的缺點。ishii嘗試經由 賦予由兩聚合物形成之長絲不對稱性,而克服此種缺點。 然而’此等纖維通常會有兩聚合物經常易在加工過程中彼 O:\74\74152-911018.DOa 4 -4- 580527 A7 B7 五、發明説明(2 ) 此脫離的嚴重缺陷。所產生之分裂纖維具有低斷裂韌度, 且會產生具有低於預期之透明性(sheerness)及導熱性的織 物。亦參見發證給Breen等人之美國專利第3,017,686號,其 揭示由兩不同非彈性聚合物所形成,且有此等缺點之纖維 〇 事實上,於發證給Tanner之美國專利第3,418,200號中知 曉在特定的條件下使芯聚合物突出至翼聚合物中實際上將 使由與芯及翼之突出部分不同之聚合物所形成之翼的部分 更易與突出部分分離。相對地,有時可能希望改良長絲中 之兩不同聚合物的附著,如揭示於美國專利第3,458,390號 ,其中使用一類型的機械鎖緊作用於將兩高模數、低彈性 之聚合物黏合在一起。然而,此種聚合物以及揭示於Breen 及Tanner中之聚合物由於其之低彈性而不具有供目前期望 之高伸展衣物用之適當的伸展及回復性質。 可利用揭示於美國專利第3,418,200號及美國專利第 5,344,297號中之噴絲板將包含兩聚合物之纖維抽絲。然而 ,當將多個聚合物流實質上在噴絲板之前結合於進給通道 中時,此等專利之噴絲板將出現聚合物的移動。此等問題 說明於聚合物科學期刊(Journal Of Polymer Science)[物理 版]第13(5)卷,863頁,1975,且其近來關於其他具有經設 計於自芯分裂之尖端之三葉形纖維之最新式的抽絲,而更 明確地示於國際纖維期刊(International Fiber Journal)(1998),第 13(5)卷,48 頁。 因此,仍有需要具有優異的伸展及回復,及在加工和使 O:\74\74152-9HOl8.DOa 4 - 5 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐) 用過程中保有其之動度之纖維及由其而得之 此種纖維及物件之便利的方法。亦有需要- 抽絲之喷絲板,其可消衫將多個聚合物流實質上在= 板孔口之雨結合於進給通道中時之聚合物移動的問題。、 發明概t 現經發現如兩聚合物之其中一者穿透另一聚合物,即一 或多個翼之至少-部分的翼聚合物突出至芯聚合物中,或 至少一邵分的芯聚合物突出至翼聚合物中,則可實質上地 降低或消除在可伸展之雙聚合物纖維内的分裂(:層貝”由 於預期(尤其係依照T_er之教授(在前))在應力之下θ,彈性 聚合物將會容易地變形,及拉出其與非彈性聚合物之互相 穿透的連接,因而此種行為係在意料之外。 根據此等發現’本發明提供一種可伸展合成聚合物纖維 ,其包括含熱塑性彈性聚合物之軸芯及複數個包含孰塑性 、非彈性聚合物之附著至芯之翼,其中翼聚合物或芯聚合 物足至少一者突出至另一聚合物内。在一具體實施例中, 軸芯包含一外部半徑Rl、一内部半徑h , &Ri/R2大於約 在另一具體實施例中,本發明提供一種可伸展合成聚合 物纖維,其包括含第一聚合物之軸芯及複數個包含第二聚 合物之附著至芯之翼,其中此纖維具有低於約i之脫層評比 及至少約2 0 %之退漿後伸展(after-b〇ii-〇ff stretch)。 此外,利用本發明之噴絲板封裝,可在噴絲板中之纖維 形成孔口的背側入口處,直接將多成份聚合物流計量至特 -6- O:\74\74I52-911018.DOO 4 本紙張尺度適用中國國家標準(CNS) A4規格(210X 297公釐) 580527 A7 B7 五、發明説明(4 ) 定點内。此可消除當將多個聚合物流實質上在噴絲板孔口 之前結合於進給通道中時之聚合物移動的問題。 因此,再根據本發明,提供一種熔融擠製複數個合成聚 合物以製造纖維之噴絲板封裝,其包括:包含可接受第一 聚合物熔體之第一組孔及可接受第二聚合物熔體之第二組 孔的計量板;與計量板對齊及接觸之噴絲板,此噴絲板具 有貫穿的毛細孔及具有低於噴絲板毛細孔長度之約6 0 %之 柱坑長度;及與噴絲板對齊及接觸,具有較毛細孔大之孔 之喷絲板支承板;其中此板經對齊,以致經供給至計量板 之複數個聚合物通過噴絲板及噴絲板支承板,而形成纖維。 圖示簡單說明 圖1係翼聚合物突出至芯中之本發明之纖維的橫剖面圖示。 圖2係芯聚合物突出至翼中之本發明之纖維的橫剖面圖示。 圖3係本發明之纖維之一具體實施例的橫剖面圖示,其中 突出聚合物,例如翼聚合物,如同牙根般地突出至被穿透 之聚合物,例如芯聚合物中。 圖4係本發明之纖維之一具體實施例的橫剖面圖示,其中 突出聚合物,例如芯聚合物,突出至被穿透之聚合物,例 如翼聚合物中,其中穿透聚合物如同栓槽。 圖5係本發明之纖維之一具體實施例的橫剖面圖示,其中 芯聚合物突出至翼聚合物中,且其包括遠端擴大的末端部 分及將末端部分結合至其餘之芯聚合物,而於其中形成至 少一頸縮部分的降低頸段。 圖6係本發明之纖維之一具體實施例的橫剖面圖示,其中 O:\74\74152-911018.DOa 4 本紙張尺度適用中國國家標準(CNS) A4規格(210X 297公釐)The present invention relates to an extensible synthetic polymer fiber = sexual elastic = core shaft core and a plurality of thermoplastically-containing, non-::; radially outer wings. The wing polymer or core is gathered in another polymer unearthed from Taiji y Λ, and the improvement of the wing-to-core attachment is also related to the production method of such fibers, and is used to form fibers. The present invention pertains to articles formed from such fibers, including articles, clothing, and the like. ^ 4 It is desirable to impart stretchability to many products formed from synthetic fibers, including various garments such as sportswear and knitwear. As disclosed in the background paragraph of the issued national patent No. 4,861,660, it is known that various kinds of extension properties are given to synthetic long ke "wanfa. In one of these methods, the fibers are shrunk in two or three dimensions. In another such method, stretchable filaments are made from an elastic polymer, for example, rubber or rubber, or a synthetic elastomer such as a polyurethane elastomer. The disadvantage of this type of stretchable filament is that the rubber or polyurethane elastic filament itself exhibits very poor wear and knitting processes and poor foot dyeing properties. Therefore, the disadvantages of the rubber of polyurethane elastomer filaments can be avoided by covering the rubber or elastic filament with another type of filament having satisfactory workability and dyeing properties. However, this type of covered elastic filament has related disadvantages. Ishii attempts to overcome this disadvantage by imparting asymmetry to the filaments formed by the two polymers. However, these fibers usually have two polymers, which are often susceptible to each other during processing. O: \ 74 \ 74152-911018.DOa 4 -4- 580527 A7 B7 V. Description of the invention (2) The serious defect of this separation. The resulting split fibers have low fracture toughness and produce fabrics with lower than expected sheerness and thermal conductivity. See also US Patent No. 3,017,686 issued to Breen et al., Which discloses fibers formed from two different non-elastic polymers and having these disadvantages. In fact, in US Patent No. 3,418,200 issued to Tanner It is known that protruding a core polymer into a wing polymer under certain conditions will actually make it easier to separate the wing portion from the protruding portion by a polymer different from the core and the protruding portion of the wing. In contrast, it may sometimes be desirable to improve the adhesion of two different polymers in a filament, as disclosed in US Patent No. 3,458,390, where a type of mechanical lock is used to bond two high modulus, low elastic polymers Together. However, such polymers, as well as the polymers disclosed in Breen and Tanner, do not have suitable stretching and restoring properties for the currently desired high stretch garments due to their low elasticity. The spinnerets disclosed in U.S. Patent No. 3,418,200 and U.S. Patent No. 5,344,297 can be used to spin fibers containing two polymers. However, when multiple polymer streams are incorporated into the feed channel substantially before the spinneret, polymer spin-off of these patented spinnerets will occur. These issues are described in Journal of Polymer Science [Physics Edition] Vol. 13 (5), p. 863, 1975, and more recently on other trilobal fibers with a tip designed to split from the core The latest type of spinning is more clearly shown in the International Fiber Journal (1998), Vol. 13 (5), p. 48. Therefore, there is still a need to have excellent stretch and recovery, and to process and make O: \ 74 \ 74152-9HOl8.DOa 4-5 This paper size applies to China National Standard (CNS) A4 (210 X 297 mm). A fiber that retains its dynamics in the process and a convenient method for such fibers and objects derived from it. There is also a need-a spinneret for spinning, which eliminates the problem of polymer movement when a plurality of polymer streams are substantially combined with rain in the orifice of the plate in the feed channel. The invention is now found that if one of the two polymers penetrates the other polymer, that is, at least a part of one or more wings of the wing polymer protrudes into the core polymer, or at least one point of the core The polymer protruding into the wing polymer can substantially reduce or eliminate the splitting in the stretchable bi-polymer fiber (: layer shell) due to expectations (especially according to Professor T_er (before)) in the stress. Below θ, the elastic polymer will easily deform and pull out its interpenetrating connection with the non-elastic polymer, so this behavior is unexpected. Based on these findings, the present invention provides a stretchable synthesis Polymer fiber comprising a core comprising a thermoplastic elastic polymer and a plurality of wings attached to the core comprising a plastic, non-elastic polymer, wherein at least one of the wing polymer or the core polymer protrudes to another polymer In a specific embodiment, the shaft core includes an outer radius R1 and an inner radius h, & Ri / R2 is greater than about 100%. In another embodiment, the present invention provides an extensible synthetic polymer fiber including: With The core of the first polymer and a plurality of wings attached to the core including the second polymer, wherein the fiber has a delamination ratio of less than about i and at least about 20% post-sizing stretch (after-b. ii-〇ff stretch). In addition, with the spinneret package of the present invention, the multi-component polymer flow can be metered directly to the special -6- O: \ at the backside entrance of the fiber-forming orifice in the spinneret. 74 \ 74I52-911018.DOO 4 This paper size applies to China National Standard (CNS) A4 (210X 297 mm) 580527 A7 B7 V. Description of the invention (4) Within the fixed point. This can eliminate the The problem of polymer movement when incorporated in the feed channel before the orifice of the spinneret. Therefore, according to the present invention, a spinneret package for melt-extruding a plurality of synthetic polymers to manufacture fibers is provided, which includes: A metering plate including a first set of holes that can accept a first polymer melt and a second set of holes that can accept a second polymer melt; a spinneret aligned and in contact with the metering plate, the spinneret having a through Capillary pores and those having a diameter less than about 60% of the pore length of the spinneret Pit length; and a spinneret support plate aligned with and in contact with the spinneret and having a larger capillary hole; wherein the plate is aligned so that a plurality of polymers supplied to the metering plate pass through the spinneret and the spinneret. The silk plate supports the plate to form fibers. The figure briefly illustrates the cross-sectional view of the fiber of the present invention in which the wing polymer protrudes into the core. Cross-section diagram. Figure 3 is a cross-section diagram of a specific embodiment of the fiber of the present invention, in which a protruding polymer, such as a wing polymer, protrudes like a tooth root to a penetrated polymer, such as a core polymer. Figure 4 is a cross-sectional view of a specific embodiment of the fiber of the present invention, in which a protruding polymer, such as a core polymer, protrudes into a penetrated polymer, such as a wing polymer, wherein the penetrating polymer Like a bolt groove. FIG. 5 is a cross-sectional view of a specific embodiment of the fiber of the present invention, in which the core polymer protrudes into the wing polymer, and includes a distal end enlarged end portion and the end portion is bonded to the remaining core polymer, A lowered neck section is formed in the at least one necked portion. Figure 6 is a cross-sectional illustration of a specific embodiment of the fiber of the present invention, where O: \ 74 \ 74152-911018.DOa 4 This paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X 297 mm)

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580527 A7 —___B7 五、發明説明(5 ) 芯包圍一或多個翼之一部分的側面,以致翼穿透芯。 圖7係有用於製造本發明之纖維之裝置的方法略圖。 圖8係可用於製造本發明之纖維之堆疊板噴絲板組合之側 立面的圖示。 圖8 A係與圖8所示之堆疊板喷絲板組合成9 〇。,及穿越圖 8之直線8 A - 8 A之孔口板A之平面圖的圖示。 圖8 B係與圖8所示之堆疊板喷絲板組合成9 〇。,及穿越圖 8之直線8B-8B之孔口板B之平面圖的圖示。 圖8C係與圖8所示之堆疊板噴絲板組合成9〇。,及穿越圖 8之直線8C-8C之孔口板C之平面圖的圖示。 圖9A顯示先前技藝噴絲板之橫剖面切開圖示。 圖9 B及9 C顯示本發明之兩噴絲板之橫剖面切開圖示。 圖1 0係可用於製造本發明之另一具體實施例纖維之堆疊 板噴絲板組合之側立面的圖示。 圖1 0 A、1 0 B及1 0 C分別顯示與圖1 〇之堆疊板喷絲板組 合成9 0。之噴絲板、分佈板、及計量板之另一具體實施例的 平面圖,其各可使用於本發明之噴絲板封裝組合中,以製 造本發明之另一具體實施例的纖維。 圖11A、11B及11C分別顯示與圖1〇之堆疊板喷絲板組合 成90°足噴絲板、分佈板、及計量板之另一具體實施例的平 面圖,其各可使用於本發明之噴絲板封裝組合中,以製造 本發明之另一具體實施例的纖維。 圖12係如實施例6所舉例之本發明之纖維的橫剖面圖示。 圖13係如實施例7所舉例之本發明之纖維的橫剖面圖示。580527 A7 —___ B7 V. Description of the Invention (5) The core surrounds the side of one part of one or more wings so that the wings penetrate the core. Fig. 7 is a schematic diagram of a method for manufacturing the fiber of the present invention. Figure 8 is an illustration of a side elevation of a stacked plate spinneret assembly that can be used to make the fibers of the present invention. Fig. 8 A is combined with the stacked plate spinneret shown in Fig. 8 to form 90. , And an illustration of a plan view of the orifice plate A across the straight line 8 A-8 A in FIG. 8. Figure 8B is combined with the stacked plate spinneret shown in Figure 8 to form 90. , And an illustration of a plan view of the orifice plate B passing through the straight line 8B-8B of FIG. 8. FIG. 8C is combined with the stacked plate spinneret shown in FIG. 8 to form 90. , And an illustration of a plan view of the orifice plate C passing through the straight line 8C-8C of FIG. 8. FIG. 9A shows a cross-sectional cut-away view of a prior art spinneret. 9B and 9C are cross-sectional cutaway views of two spinnerets of the present invention. Fig. 10 is an illustration of a side elevation of a stacked plate spinneret assembly that can be used to make fibers according to another embodiment of the present invention. Figs. 10 A, 10 B, and 10 C respectively show a combination of 90 with the spinneret of the stacked plate shown in Fig. 10. A plan view of another specific embodiment of the spinneret, the distribution plate, and the metering plate, each of which can be used in the spinneret packaging package of the present invention to manufacture the fiber of another specific embodiment of the present invention. 11A, 11B, and 11C are plan views showing another specific embodiment of a 90 ° foot spinneret, a distribution plate, and a metering plate combined with the stacked plate spinneret of FIG. 10, each of which can be used in the present invention. The spinneret package is used to fabricate fibers according to another embodiment of the present invention. FIG. 12 is a cross-sectional view of a fiber of the present invention as exemplified in Example 6. FIG. FIG. 13 is a cross-sectional view of a fiber of the present invention as exemplified in Example 7. FIG.

580527 A7580527 A7

五、發明説明( 7 物’各聚合物係為不同的屬類,例如 缔煙時,將其稱為「雙組成」纖維。如=;、、聚醋或聚 相當不同’則可使用相同屬類的聚合物,】《彈性特性 「雙成份」纖维。此種雙成份纖維亦係在本4 =維為 根據本發明,翼聚合物及芯聚合物 二—月<範圍卜 -聚合物内。圖i顯示翼聚合物突出至芯聚7物者突出至另 芯聚合物突出至翼聚合物内。芯及翼聚合 圖2 = 降低纖維分裂之方法完成。舉例來說,在 般:::=’穿透聚合物(例如翼聚合物)可如同牙根 奴地大出至被穿透之聚合物(例如芯聚合物)中,以致形成 複數個哭起(見圖3)。在另—具體實施例中,穿透聚合物( 例如芯聚合物)可突出至被穿透之聚合物(例如翼聚合物)中 ’其中穿透聚合物如同栓槽(見圖4)。检槽具有實質上均句 的直徑。纟又另一具體實施例中’至少_聚合物可具有單 :翼進入芯中或芯進入翼中之至少一突出部分,其包括遠 端擴大的末端部分及將末端部分結合至其餘之至少一聚合 物,而於其中形成至少一頸縮部分的降低頸段。圖5顯示芯 聚合物突出至各翼聚合物中,且其具有此一遠端擴大的末 端部分16及降低頸段18。將藉由此一擴大末端部分及降低 頸段而彼此附著之翼及芯稱為「機械鎖緊」。為容易製造 及使翼與芯之間有更有效的黏著,具有降低頸段之最後提 及的具體實施例通常為較佳。熟悉技藝人士可設想其他的 突出方法。舉例來說,如圖6所見,芯可包圍一或多個翼之 一部分的側面,以致翼穿透芯。 -10 - O:\74\74152-911018.DOC 4 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐) 580527 A7V. Description of the invention (7 substances 'Each polymer is a different genus, for example, when it is associated with tobacco, it is called a "double-composition" fiber. If = ;, polyacetate or poly is quite different', the same genus can be used Kind of polymer, "" bicomponent "fiber with elastic properties. This kind of bicomponent fiber is also based on this invention. According to the present invention, wing polymer and core polymer are two-month < range and polymer. Figure i shows that the wing polymer protrudes to the core polymer and the other core polymer protrudes to the wing polymer. The core and wing polymer Figure 2 = The method of reducing fiber splitting is completed. For example, in general :: : = 'Penetrating polymers (such as wing polymers) can grow out of the penetrating polymers (such as core polymers), so that multiple crying is formed (see Figure 3). In another— In a specific embodiment, a penetrating polymer (such as a core polymer) may protrude into a penetrating polymer (such as a wing polymer), where the penetrating polymer is like a plug groove (see FIG. 4). The diameter of the above sentence. In yet another specific embodiment, 'at least _ polymer may have a single: wings At least one protruding portion in the core or core into the wing, which includes a distally enlarged end portion and a lower neck portion that joins the end portion to the remaining at least one polymer to form at least one necked portion therein. Figure 5 It is shown that the core polymer protrudes into each wing polymer, and it has such a distally enlarged end portion 16 and a lowered neck section 18. The wings and cores attached to each other by this enlarged end portion and lowered neck section It is "mechanical locking." For ease of manufacture and more effective adhesion between the wing and the core, the last-mentioned specific embodiment with a lowered neck section is usually better. Those skilled in the art can envision other prominent methods. For example, as seen in Figure 6, the core may surround the side of one or more of the wings so that the wings penetrate the core. -10-O: \ 74 \ 74152-911018.DOC 4 This paper size applies Chinese national standards ( CNS) A4 size (210 X 297 mm) 580527 A7

本發明《纖維包括具有一外部半徑及一内部半徑之軸 ❹^別於圖⑴中之「^「^卜夕卜部半㈣ 2心 < 取外部部分外接之圓的半徑,及内部半徑係與翼之 取内部部分内切之[||的半徑。在本發明之纖維中, 般係大万;约1 · 2。R i /汉2係在約丨· 3至約2 . 〇之範圍内較佳。 杬脫層性在較低比下會衰退,及在較高比下,I中之高量 值的彈性聚合物(或芯中之非彈性聚合物)會使纖維之伸展 及回復減低。當芯在翼内形成栓槽時,Ri/R2接近2。相對 地,在翼或芯聚合物之其中一者並未突出至另一聚合物内 足纖維中,L接近r2,以致翼及芯未彼此穿透。在複數個 翼足情況中,一些翼中之聚合物穿透芯聚合物,同時其他 翼中 <聚合物被芯聚合物穿透,Ri&R2僅以對應於各翼之 對所決定,如圖2所說明,且各比ri/R2及riV:R2,一般係大 於約1.2,以在約ι·3至2· 〇之範圍内較佳。在另一具體實施 例中’一些翼可被芯聚合物穿透,而相鄰的翼則未被穿透 ’則〜及以2係以對被穿透翼之關係所決定;同樣地,當僅 有部分的芯被翼聚合物穿透時,R i及r2係以對穿透翼之關 係所決定。可對翼使用芯至翼、翼至芯、及無穿透之任何 組合,只要至少一翼穿透芯或被芯穿透即可。 本發明之纖維係繞其之縱軸扭轉,而無顯著的二或三維 蜷縮特性。.(在此種較高維的蜷縮中,纖維縱軸的本身呈鋸 齒或螺旋形態;此種纖維非為本發明)。本發明之纖維的特 徵可在於具有實質的螺旋拈及一維螺旋拈。「實質的螺旋 拈」包括完全環繞彈性芯通過之螺旋拈以及僅部分環繞芯 -11 - O:\74\74152-911018000 4 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐) 580527 A7According to the present invention, the "fiber includes an axis having an outer radius and an inner radius. ^ Is different from" ^ "in the figure. ^ 卜 夕 卜 部 半 ㈣ 2 center < takes the radius of the circle circumscribed by the outer part, and the inner radius is related to The radius of [|| inscribed in the inner part of the wing. In the fiber of the present invention, it is generally 10,000; about 1.2. Ri / Han 2 is in the range of about 丨 · 3 to about 2.0.杬 Delamination will decline at lower ratios, and at higher ratios, a high amount of elastic polymer (or non-elastic polymer in the core) in I will reduce fiber stretch and recovery When the core forms a bolt groove in the wing, Ri / R2 is close to 2. In contrast, one of the wing or core polymer does not protrude into the other polymer inner foot fiber, and L is close to r2, so that the wing and The cores do not penetrate each other. In the case of a plurality of wing feet, the polymer in some wings penetrates the core polymer, while the polymer in the other wings is penetrated by the core polymer, and Ri & R2 only corresponds to each wing. The pair is determined, as illustrated in Figure 2, and the ratios ri / R2 and riV: R2 are generally greater than about 1.2 so as to be in the range of about ι · 3 to 2 · 〇 Better. In another specific embodiment, 'some wings can be penetrated by the core polymer, while adjacent wings are not penetrated' is determined by the relationship of 2 series to the penetrated wings; also Ground, when only a part of the core is penetrated by the wing polymer, Ri and r2 are determined by the relationship of the penetrating wing. Any combination of core-to-wing, wing-to-core, and non-penetration can be used for the wing. As long as at least one wing penetrates or is penetrated by the core, the fiber of the present invention is twisted about its longitudinal axis without significant two- or three-dimensional shrinkage characteristics. (In such higher-dimensional shrinkage, the fiber The longitudinal axis itself is in a zigzag or spiral shape; such fibers are not the present invention). The fibers of the present invention may be characterized by having a substantial spiral tow and a one-dimensional spiral. The "essential spiral" includes passing completely around the elastic core. Spiral 拈 and only partially surround the core-11-O: \ 74 \ 74152-911018000 4 This paper size applies to China National Standard (CNS) A4 (210 X 297 mm) 580527 A7

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580527 A7 B7 五、發明説明(1〇 ) 研先期刊(Textile Research Journal),1967年 6 月,449 頁。 為達到最大的橫剖面徑向對稱,芯可具有實質上圓形或 規則的多邊形橫剖面,例如,如圖1及2所見。所謂「實質 上圓形」係指在纖維橫剖面之中心彼此9 〇。相交之兩軸之長 度的比不大於約1.2:1。相對於美國專利第4,861,66〇號之芯 ’使用實質上圓形或規則多邊形之芯可保護彈性體使不與 輥、導件等等接觸,如稍後參照翼之數目所說明。可將複 數個翼環繞芯以任何期望的方式設置,例如,如圖1及2所 描繪之不連續地設置,即翼聚合物並未於芯上形成連續的 飾邊,或相鄰的翼於芯表面相會,例如,如美國專例第 3,418,200號之圖4及5所說明。設若可維持實質的徑向對稱 ,則翼可為相同或不同的尺寸。此外,再次設若可維持實 負上的徑向幾何及聚合物組合物對稱,則各翼可為與其他 翼不同之聚合物。然而,為簡化製造及使徑向對稱性之達 成谷易,翼為大約相同的尺寸,且由相同的聚合物或聚合 物之摻混物製成較佳。為容易製造起見,翼不連續地環繞 芯亦較佳。 雖然纖維橫剖面就尺寸、聚合物及環繞芯之角度間隔而 T實質上為對稱,但應明瞭在任何的抽絲方法中一般會由 於諸如不均勻驟冷或有瑕疵的聚合物熔體流動或有瑕=的 抽絲孔口的.因素,而存在與完全對稱的微小變異。應明瞭 汉右此種變異之程度並不足以減損本發明之目的,諸如經 由一維螺旋拈而提供期望伸展及回復之纖維,同時使二2 三維蜷縮減至最小,則其係可容許。換言之,並非要故意 〇:\74\74152-9ll〇18.D〇a -13- 11 五、發明説明( 知,、准做成如同美國專利第4,861,660號般之不對稱。 、—異自其所黏附 < 芯向外突出’且形成至少部分環繞芯之 、夂數個累旋A其係於有效的加熱之後。當纖維經伸展時 累旋之節距可增加。本發明之纖維具有複數個翼, 以3 8個較佳,5或6個更佳。所使用之翼的數目可視纖維之 :他特徵及其之製造和使用條件而定。舉例來說,當製造 早絲,尤其係在較高牵伸比及纖維張力下時,可使用5或6 個翼在此情況,翼的間隔可夠頻繁地環繞芯,以致可保 護彈性使不與輥、導件、及其類似物接觸,因此而較使用 較少翼《情況不易斷裂、包輥、及磨損。較高牽伸比及纖 維張力的作用係要將纖維更緊密地壓向輕及導件,因此而 使翼伸展及使彈性芯與輕或導件接觸;因此,在高牵伸比 及纖維張力下多於兩翼較佳。在單絲中,關於容易製造及 降低芯接觸之最適組合,五或六個翼通常為較佳。♦須要 多纖維紗時,由於在彈性芯與輥或導件之間的接觸能性 因其他纖維之存在而降低,故可使用少至二或三個翼。 雖然為容易製造起見,翼較佳係不連續地環繞芯,但芯 可在其之外表面上在翼接觸芯的點之間 : 之勒。鞘之厚度可在纖維芯之最大半徑之約0 5%至== 的,圍内。鞘可經由在芯與翼聚合物之間提供更多接觸點 而#助翼心黏著至芯’此係當雙組成纖維中之聚合物並未 彼此艮好黏著時之特別有用的特徵。鞘亦可降低在朴. 、導件、及其類似物之間的磨蚀接觸,尤其係 ^ 少數的翼時。 ^八$ O:\74\74152-9U018.DOa 4 · 14 , 本紙張尺度適用t s S家標準(CNS) A4規格(21〇Χ297公爱)580527 A7 B7 V. Description of the Invention (10) Textile Research Journal, June 1967, 449 pages. To achieve maximum cross-section radial symmetry, the core may have a substantially circular or regular polygonal cross-section, as seen in Figs. The so-called "substantially circular" refers to each other at the center of the cross section of the fiber. The ratio of the lengths of the intersecting two axes is not greater than about 1.2: 1. In contrast to the core of U.S. Patent No. 4,861,66 ', the use of a substantially circular or regular polygonal core protects the elastomer from contact with rollers, guides, etc., as described later with reference to the number of wings. The plurality of wings can be arranged around the core in any desired manner, for example, as discontinuously arranged as depicted in Figures 1 and 2, that is, the wing polymer does not form a continuous trim on the core, or adjacent wings are The core surfaces meet, for example, as illustrated in Figures 4 and 5 of US Patent No. 3,418,200. Provided that substantial radial symmetry can be maintained, the wings can be the same or different sizes. In addition, once again, if the radial geometry in the negative direction and the polymer composition symmetry can be maintained, each wing may be a polymer different from the other wing. However, to simplify manufacturing and achieve radial symmetry, the wings are approximately the same size and are preferably made from the same polymer or polymer blend. For ease of manufacture, it is also preferred that the wings discontinuously surround the core. Although the cross section of the fiber is essentially symmetrical in terms of size, polymer, and angular spacing around the core, it should be understood that in any spinning method, due to, for example, uneven quenching or defective polymer melt flow or Defective = the factor of the drawing orifice, and there is a slight variation with perfect symmetry. It should be understood that the extent of this variation of Han You is not sufficient to detract from the purpose of the present invention, such as providing a desired stretch and recovery of fibers through a one-dimensional spiral crest, while minimizing two-dimensional and three-dimensional crimping. In other words, it is not intentional 〇: \ 74 \ 74152-9ll〇18.D〇a -13- 11 V. Description of the invention (knowledge, quasi-made as asymmetric as US Patent No. 4,861,660. ——Different From the core to which it is attached < protruding outwardly, and forming at least partly surrounding the core, a plurality of tired spins A are formed after effective heating. When the fiber is stretched, the pitch of the tired spins can be increased. The fiber of the present invention It has multiple wings, preferably 38, 5 or 6. The number of wings used depends on the characteristics of the fiber: its characteristics and the conditions of its manufacture and use. For example, when manufacturing early filaments, Especially under higher draft ratio and fiber tension, 5 or 6 wings can be used. In this case, the spacing of the wings can frequently surround the core, so that the elasticity can be protected from the rollers, guides, and the like. It is less likely to break, rolls, and wear than when it is in contact with materials. The effect of higher draft ratio and fiber tension is to press the fibers more tightly towards the light and guide, thus extending the wings. And bringing the elastic core into contact with the light or guide; therefore, at high draft ratios and fiber tension More than two wings are preferred. In a monofilament, five or six wings are usually better for the most suitable combination for easy manufacturing and reduced core contact. ♦ When multi-fiber yarn is required, it is because between the elastic core and the roller or guide The contact performance of the fiber is reduced due to the presence of other fibers, so as few as two or three wings can be used. Although the wings preferably discontinuously surround the core for ease of manufacture, the core can be placed on its outer surface Between the points where the wings touch the core: The thickness of the sheath can be within the range of about 0 5% to == of the maximum radius of the fiber core. The sheath can provide more contact points between the core and the wing polymer The #help wing heart adheres to the core 'is a particularly useful feature when the polymers in the bicomponent fibers are not well adhered to each other. The sheath can also be lowered between Pak, guides, and the like. Abrasive contact, especially when there are a few wings. ^ Eight $ O: \ 74 \ 74152-9U018.DOa 4 · 14, This paper size is applicable to ts S home standard (CNS) A4 specification (21〇 × 297 public love)

β、t發明《多翼橫剖面之芯及/或翼可為實心,或包括空心 或二隙典型上,芯及翼皆為實心。此外,翼可具有任何 形狀、’諸如卵形H、或S-形狀(參見,例如圖4)。 :用《翼形狀的例子見於美國專利第4,3 85,866號。T、c、 /狀如先㈤所說明,其可幫助保護彈性芯使不與導件及 幸昆接觸。 、I改’交全體翼聚合物對芯聚合物之重量比,以賦予性質 足期望的混合,例如,來自芯之期望彈性及其他性質諸如 來自翼永口物之低黏性。舉例來說,可使用約1 〇 / 9 〇至約 70/3 0,以約3〇/70至約4〇/6〇較佳之翼對芯之重量比。關 於在纖維不需使用伴紗之用途(例如針織品)中之高耐用性 結合高伸展,約3 5/65至約5〇/5〇之翼/芯重量比為較佳。 為在芯及翼之間有最佳的黏著,典型上,總纖維重量之約5 重!百分比至約3 〇重量百分比可為穿透芯之非彈性聚合物 ’或穿透翼之彈性芯聚合物。 如丽所指,本發明之纖維的芯可由任何熱塑性彈性聚合 物形成。有用之彈性體的例子包括熱塑性聚胺甲酸酯、熱 塑性聚酯彈性體、熱塑性聚烯烴、熱塑性聚酯醯胺彈性體 及熱塑性聚醚酯醯胺彈性體。 有用之熱塑性聚胺甲酸酯芯彈性體包括由聚合二元醇、 二異氰酸酯.、及至少一二元醇或二胺增鏈劑所製備得者。 由於利用二元醇增鏈劑製得之聚胺甲酸酯較使用二胺增鏈 劑所製得者具有較低之熔點,因而二元醇増鏈劑為較佳。 有用於製備彈性聚胺甲酸酯之聚合二元醇包括聚醚二元醇 O:\74\74152-911018.DOO 4 .15. 本紙張尺度適财g g家標準(CNS) A4規格(210 X 297公釐) '' ----— ---- —_B7 五、 永@旨一元醇、聚碳酸g旨二元醇及其之共聚物。此種二元 醇之例子包括聚(伸乙基醚)二元醇、聚(四亞甲基醚)二元醇 、聚(四亞甲基-共-2 -甲基四亞甲基醚)二元醇、聚(伸乙基· 共-己二酸1,4 -丁二酯)二元醇、聚(伸乙基-共-己二酸丨,2_ 丙二醋)二元醇、聚(六亞甲基-共-己二酸2,2 -二甲基- i,3_ 丙二酯)、聚(己二酸3 -甲基-1,5-戊二酯)二元醇、聚(壬酸 甲基-1,5 -戊二酯)二元醇、聚(十二酸2,2 -二甲基q,3· 丙二酯)二元醇、聚(戊烷· 1,5 -碳酸酯)二元醇、及聚(己烷_ 1,6 -碳酸酯)二元醇。有用的二異氰酸酯包括異氰酸基· 4-[(4 -異氰酸苯基)甲基]苯、異氰酸基_2-[(4 -異氰酸苯 基)甲基]苯、異佛爾酮二異氰酸酯、1,6 -己烷二異氰酸酉旨 、2,2-雙(4-異氰酸苯基)丙烷、丨〆-雙(對異氰酸基-α,α_ 二甲芊基)苯、1,1,_亞甲基雙(4-異氰酸基環己烷)、及二異 氰酸2,4-甲苯二酯。有用的二元醇增鏈劑包括乙二醇、 1,3-丙二醇、;ι,4-丁二醇、2,2-二甲基-L3-丙二醇、二乙 二醇、及其之混合物。較佳的聚合二元醇為聚(四亞甲基醚 )二元醇、聚(四亞甲基-共-2-甲基四亞甲基醚)二元醇、聚( 伸乙基-共-己二酸1,4 -丁二g旨)二元醇、及聚(十二酸2,2· 二曱基-1,3 -丙二酯)二元醇。1-異氰酸基·4-[(4 -異氰酸苯 基)甲基]苯為較佳的異氰酸酯。較佳的二元醇增鏈劑為 1,3·丙一醇及1,4 -丁二醇。可加入單官能鏈終止劑諸如卜 丁醇及其類似物,以控制聚合物之分子量。 有用的熱塑性聚酯彈性體包括由聚醚二元醇與低分子量 二元醇,例如,低於約250之分子量,及二羧酸或其之二元 -16- O:\74\74152-911018.DOa 4 本纸張尺度適用中國國家標準(CNS) Α4規格(210 X 297公釐) 580527 A7Beta and t inventions "The core and / or wings of a multi-wing cross section may be solid, or include hollow or two-gap. Typically, the core and wings are solid. Further, the wings may have any shape, such as an oval H, or S-shape (see, e.g., Figure 4). : An example of the shape of a wing is found in U.S. Patent No. 4,3,85,866. The T, c, / shape, as explained above, can help protect the elastic core from contact with the guide and Xing Kun. The weight ratio of the entire wing polymer to the core polymer is altered to impart properties that are adequately mixed, for example, the desired elasticity from the core and other properties such as low viscosity from the wing mouthpiece. For example, a weight ratio of about 10/90 to about 70/3, preferably about 30/70 to about 40/60, a wing to core may be used. Regarding high durability in applications where fibers are not required to accompany yarns (such as knitwear) combined with high stretch, a wing / core weight ratio of about 3 5/65 to about 50/50 is better. For the best adhesion between the core and the wings, typically, the total fiber weight is about 5 weights! The percentage to about 30% by weight can be a non-elastic polymer that penetrates the core 'or an elastic core polymer that penetrates the wings. The core of the fiber of the present invention may be formed from any thermoplastic elastomeric polymer, as Rey points out. Examples of useful elastomers include thermoplastic polyurethanes, thermoplastic polyester elastomers, thermoplastic polyolefins, thermoplastic polyester amide elastomers, and thermoplastic polyether ester amine elastomers. Useful thermoplastic polyurethane core elastomers include those prepared from polymerized diols, diisocyanates, and at least one diol or diamine chain extender. Since the polyurethane obtained by using a diol chain extender has a lower melting point than that obtained by using a diamine chain extender, a diol chain extender is preferred. Polymer diols useful in the preparation of elastic polyurethanes include polyether diols O: \ 74 \ 74152-911018.DOO 4 .15. This paper is compliant with the CNS A4 specification (210 X 297 mm) '' ---------------- B7 V. Wing @ 旨 一 元 醇, polycarbonate g 碳酸 diol and copolymers thereof. Examples of such diols include poly (ethylene ether) diols, poly (tetramethylene ether) diols, poly (tetramethylene-co-2-methyltetramethylene ether) Glycols, poly (ethylene-co-adipic acid 1,4-butyrate) glycols, poly (ethylene-co-adipic acid 丨, 2_ malonic acid) glycols, poly (Hexamethylene-co-adipate 2,2-dimethyl-i, 3-propanediol), poly (3-methyl-1,5-pentane adipate) glycol, poly (Nonanoic acid methyl-1,5-pentane ester) glycol, poly (dodecanoic acid 2,2-dimethyl q, 3 · propylene glycol) glycol, poly (pentane · 1.5 -Carbonate) diol and poly (hexane-1,6-carbonate) diol. Useful diisocyanates include isocyanate4-[(4-isocyanophenyl) methyl] benzene, isocyanato_2-[(4-isocyanatophenyl) methyl] benzene, iso Furone diisocyanate, 1,6-hexanediisocyanate, 2,2-bis (4-isocyanatophenyl) propane, 〆-bis (p-isocyanato-α, α_ di Formamyl) benzene, 1,1, -methylenebis (4-isocyanatocyclohexane), and 2,4-toluene diisocyanate. Useful glycol chain extenders include ethylene glycol, 1,3-propanediol, ι, 4-butanediol, 2,2-dimethyl-L3-propanediol, diethylene glycol, and mixtures thereof. Preferred polymeric diols are poly (tetramethylene ether) diols, poly (tetramethylene-co-2-methyltetramethylene ether) diols, poly (ethylene-co- -Adipic acid 1,4-butanedi g) glycol and poly (dodecanoic acid 2,2 · difluorenyl-1,3-propanediol) glycol. 1-isocyanate · 4-[(4-isocyanatophenyl) methyl] benzene is a preferred isocyanate. Preferred glycol chain extenders are 1,3-propanediol and 1,4-butanediol. Monofunctional chain terminators such as butanol and the like may be added to control the molecular weight of the polymer. Useful thermoplastic polyester elastomers include polyether diols and low molecular weight diols, for example, molecular weights below about 250, and dicarboxylic acids or their binary -16- O: \ 74 \ 74152-911018 .DOa 4 This paper is sized for China National Standard (CNS) A4 (210 X 297 mm) 580527 A7

酉。曰例如,對酞酸或對酞酸二甲酯之反應所製得之聚醚酷 、,用的聚醚二7C醇包括聚(伸乙基醚)二元醇、聚(四亞甲 基醚)二元醇、聚(四亞甲基_共」·甲基四亞甲基醚)二元醇[ 何生自四氯咬喃與3 ·甲基四氣峡喃之共聚合作用]及聚(伸 乙基-共-四亞甲基醚)二元醇。有用的低分子量二元醇包括 =一醇、1,3-丙二醇丁二醇、2,2_ 二甲基“,3-丙二 醇及其 < 混合物;1,3-丙二醇及154_ 丁二醇為較佳。有 用的二羧酸包括對酞酸,其視需要可具有少量的異酞酸, 及其之二兀酯(例如,<20莫耳百分比)。 —可使用於製造本發明之纖維之芯之有用的熱塑性聚酯醯 月女彈性體包括說明於美國專利第3,偏,975號中者。舉例來 說可將此種彈性體製備成具有經由使乙二醇、丨,2_丙二 醇、\,3-丙二醇、丁二醇、2,2-二甲基{3-丙二醇Γ I %戊二醇、I6·己二醇、M0-癸二醇、1,4-二(甲醇)環 己烷一乙一醇、或三乙二醇與丙二酸、琥珀酸、戊二酸 己一酸2 -甲基己二酸、3 -甲基己二酸、3,4 -二甲基己 二酸、庚二酸、辛二酸、壬二酸、癸二酸、或十二烷二酸 或其之酉曰反應而製得之聚酯片段。此種聚酯醯胺中之聚 醯胺片段的例子包括經由六亞甲二胺或十二亞甲二胺與對 酞酸、草酸、己二酸、或癸二酸之反應,及經由己内醯胺 之開環聚合作用所製備得者。 亦可使用熱塑性聚㈣酿胺彈性體,諸如說明於美國專 利第4,230,838號中者’製造纖維芯。此種彈性體可經由, 例如,經由自低分子量(例如’約3〇〇至約15,〇〇〇)聚己内醯unitary. For example, polyethers prepared by the reaction of terephthalic acid or dimethyl terephthalate, the polyether di 7C alcohols used include poly (ethylene ether) diols, poly (tetramethylene ether) ) Glycols, poly (tetramethylene_co "· methyltetramethylene ether) diols [He Shengzi's copolymerization of tetrachlorosulfan and 3.methyltetrahydroxan] and poly (Ethylene-co-tetramethylene ether) glycol. Useful low-molecular-weight diols include monool, 1,3-propanediol butanediol, 2,2-dimethyl ", 3-propanediol, and < mixtures thereof; 1,3-propanediol and 154_butanediol are Useful dicarboxylic acids include terephthalic acid, which may have a small amount of isophthalic acid, if necessary, and its bis-ester (e.g., < 20 mole percent).-Can be used to make the fibers of the present invention Useful thermoplastic polyester core elastomers for cores include those described in U.S. Patent No. 3, 975. Such elastomers can be prepared, for example, with ethylene glycol, 2-propanediol , \, 3-propanediol, butanediol, 2,2-dimethyl {3-propanediol Γ 1% pentanediol, I6 · hexanediol, MO-decanediol, 1,4-di (methanol) ring Hexane-ethylene glycol, or triethylene glycol with malonic acid, succinic acid, glutaric acid, adipic acid, 2-methyl adipate, 3-methyl adipic acid, 3,4-dimethyl adipate Polyester fragments prepared by the reaction of acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, or dodecanedioic acid, or any of them. Polyamide fragments in this polyester amide. Examples include Prepared by the reaction of hexamethylenediamine or dodecamethylenediamine with terephthalic acid, oxalic acid, adipic acid, or sebacic acid, and by ring-opening polymerization of caprolactam. Thermoplastics can also be used Polyurethane elastomers, such as those described in U.S. Patent No. 4,230,838, make fiber cores. Such elastomers can be passed, for example, from a low molecular weight (e.g., 'about 300 to about 15,000) Polycaprolactam

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580527 五、發明説明( 15 :二聚庚内驢胺、聚癸内醯胺、聚十 =卜聚⑴-胺基十二酸)、聚(己二酸己二= 壬一酸己二酯)、聚ΓΡ μ 日’水1 禾(癸一馼己二酯)、聚(十一酸 水(十二酸己二酯)、聚(二 -曰 、己二齡、I △ 馱壬一酴)或其類似物及琥珀酸 辛二酸、壬二酸、癸二酸、十一烷 酸、對酞 而製備製備二__胺預聚物 =仔。然後可使預聚物與經基封端聚趟’例如聚(四亞 :基二_、聚(四亞甲基冬2_甲基四亞甲基醚)二元 物反應。 水(狎乙基醚)一兀醇、或其類似 如前所指,翼可由任何非彈性、或硬的聚合物形成。此 種水口物之例子包括非彈性聚酯、聚酿胺、及聚缔煙。 有用之熱塑性非彈性翼聚酯包括聚(對酞酸乙二酯)(「 2G-T」)及其共聚物、聚(對酞酸丙二酯从「丁」)、聚 對酞酸丁二酯(「4G_T」)、及聚(2,6-莕二甲酸乙二酯)、 聚(對酞酸1,4-伸環己基二亞甲酯)、聚(乳交酯)、聚(壬二 酸乙一知)、永[2,7 -莕二甲酸乙二酯]、聚(羥乙酸)、聚(琥 珀酸乙二酯)、聚(α,α •二甲基丙内酯)、聚(對羥基苯甲酸 酉曰)、聚(氧苯甲酸乙二酯)、聚(異酞酸乙二酯)、聚(對酞酸 丁二酯)、聚(對酞酸己二酯)、聚(對酞酸癸二酯)、聚(1,4_ 裱己烷二亞甲基對酞酸酯)(反式)、聚(丨,5 _莕二甲酸乙二 酯)' 聚(2,6·莕二甲酸乙二酯)、聚(丨,扣亞環己基二亞甲 基對酞酸酯)(順式)、及聚(丨,4 ·亞環己基二亞甲基對酞酸 酯)(反式)。 裝 訂 線 O:\74\74152-9U018.DOa 4 -18 - 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐) 580527 A7580527 V. Description of the invention (15: Dipolyheptamylamine, polydecanedilamine, polydeca = polyammonium-aminododecanoic acid), poly (adipate adipate = adipic acid adipate) , Poly Γ μ μ '' water 1 He (decane hexamethylene adipate), poly (undecanoic acid water (hexadecyl lauryl adipate), poly (di-y, hexamethylene, I △ 驮 酴 驮 酴 酴) Or its analogues and succinate suberic acid, azelaic acid, sebacic acid, undecanoic acid, terephthalic acid to prepare di_amine prepolymers = zi. Then the prepolymers can be polymerized with end caps For example, the reaction of poly (tetramethylene: diphenyl), poly (tetramethylene winter 2-methyltetramethylene ether) binary reaction. Water (fluorethyl ether) monool, or similar as before As mentioned, the wings may be formed from any non-elastic, or rigid polymer. Examples of such spouts include non-elastic polyesters, polyamines, and poly-smoke. Useful thermoplastic non-elastic wing polyesters include poly (terephthalate) (Ethylene glycol) ("2G-T") and its copolymers, poly (propylene terephthalate from "butyl"), polybutylene terephthalate ("4G_T"), and poly (2,6 -Ethylene dicarboxylate), poly (terephthalic acid 1 , 4-cyclohexyl dimethylene), poly (lactide), poly (ethylene azelate), yong [2,7-acetonium dicarboxylate], poly (glycolic acid), poly (amber Acid ethylene glycol ester), poly (α, α • dimethylpropiolactone), poly (paraben), poly (ethylene oxybenzoate), poly (ethylene isophthalate), Poly (butylene terephthalate), poly (hexane terephthalate), poly (sebacate terephthalate), poly (1,4_ hexane dimethylene terephthalate) (trans ), Poly (丨, 5 _ ethylene dicarboxylate) 'poly (2,6 · ethylene dicarboxylate), poly (丨, cyclohexylene dimethylene terephthalate) (cis ), And poly (丨, 4 · cyclohexylenedimethylene terephthalate) (trans). Binding line O: \ 74 \ 74152-9U018.DOa 4 -18-This paper size applies to Chinese national standards ( CNS) A4 size (210 X 297 mm) 580527 A7

=的非彈性聚醋包括聚(恤乙二醋)、聚(對 一酉曰)、及聚(對酉太酸以· 丁二酉旨)及其之共聚物。當使 當=熔點之聚料如聚(fm酸乙L可將共單體加 入至聚酯中,以致其可於降低溫度下抽絲。此種共單心 包括具4·12㈣原子之直鏈、環狀、及分支鏈脂族二^ 例如戊一馱)’除對酞酸之外,且具有8 - 1 2個碳原子之芳族 二羧酸(例如異酞酸);具3-8個碳原子之直鏈、環狀、及分 支鏈脂族二元醇(例如丨,3·丙二醇、丨,2•丙二醇、丨,4-丁2 醇、及2,2_二甲基-1,3 -丙二醇);及具4-10個碳原子之脂 族及芳脂族醚二元醇(例如氫醌雙(2_羥乙基)醚)。共單體 可以在約0 · 5至1 5莫耳百分比之範圍内之量值存在於共聚酯 中異欧、戊一 、己二酸、1,3 -丙二醇、及ι,4 -丁二 醇由於可容易地於市面購得,且價廉,因而其為聚(對酞酸 乙二酯)之較佳共單體。 翼聚醋亦可包含少量的其他共單體,其限制條件為此種 共單體不會對纖維性質具有不利的影響。此種其他共單體 包括,例如,在約〇 · 2至5莫耳百分比之範圍内之量值的5 _ 磺酸異酞酸鈉。可加入非常少量,例如,以總成份計約〇1 重量百分比至約0.5重量百分比之三官能共單體,例如,偏 苯三甲酸,以控制黏度。 有用的熱塑性非彈性翼聚醯胺包括聚(六亞甲基己二醯胺 )(耐綸6,6);聚己内醯胺(耐綸6);聚庚醯胺(耐綸7);耐 論10;聚(12 -十二内醯胺)(耐綸12);聚四亞甲基己二醯 胺(耐綸4,6);聚六亞曱基癸二醯胺(耐綸6,10);聚(六亞 O:\74\74152-911018.DOC\ 4 -19- 本纸張尺度適用中國國家標準(CNS) A4規格(210X 297公釐)The non-elastic poly (vinyl acetate) includes poly (ethylene glycol diacetate), poly (polyethylene terephthalate), and poly (polyethylene terephthalate), and copolymers thereof. Dangdang = melting point polymers such as poly (fm ethyl acetate) can add comonomers to polyesters, so that they can be drawn at reduced temperatures. Such co-monomers include straight chains with 4 · 12㈣ atoms , Cyclic, and branched chain aliphatic di ^^ such as pentamidine) 'Aromatic dicarboxylic acids (eg isophthalic acid) other than terephthalic acid and having 8-12 carbon atoms; with 3-8 Linear, cyclic, and branched aliphatic diols of one carbon atom (for example, 3, propanediol, 2 propanediol, 4 butane-2 alcohol, and 2,2-dimethyl-1 , 3-propanediol); and aliphatic and araliphatic ether diols having 4 to 10 carbon atoms (such as hydroquinone bis (2-hydroxyethyl) ether). The co-monomer may be present in the copolyester in amounts ranging from about 0.5 to 15 mole percent. Isoou, glutaric, adipic acid, 1,3-propanediol, and ι, 4-butane Alcohols are readily available on the market and are inexpensive, making them a preferred comonomer of poly (ethylene terephthalate). Wing polyacetate may also contain small amounts of other comonomers, with the limitation that such comonomers do not adversely affect fiber properties. Such other comonomers include, for example, sodium 5-sulfoisophthalate in an amount in the range of about 0.2 to 5 mole percent. Trifunctional co-monomers, such as trimellitic acid, can be added in very small amounts, for example, from about 0.01 weight percent to about 0.5 weight percent based on total ingredients to control viscosity. Useful thermoplastic non-elastic wing polyamines include poly (hexamethylenehexamethylene diamine) (Nylon 6,6); polycaprolactam (Nylon 6); polyheptylamine (Nylon 7); Nairon 10; Poly (12-dodecylamine) (Nylon 12); Polytetramethylenehexamethylene diamine (Nylon 4,6); Polyhexamethylene sebacamide (Nylon 6) , 10); poly (Liuya O: \ 74 \ 74152-911018.DOC \ 4 -19- This paper size applies to China National Standard (CNS) A4 specification (210X 297 mm)

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線 580527 A7 ______B7 五、發明説明(17 ) 甲基十二si胺)(耐綸6,12);十二亞甲二胺及正十二烷二酸 之聚醯胺(耐綸12,12)、衍生自雙(4-胺基環己基)甲烷及十 二烷二酸之PACM- 1 2聚醯胺、3 0 %異酞酸六亞甲二銨及 70 %己二酸六亞甲二銨之共聚醯胺、至高3〇 %之雙(對醯胺 基環己基)亞甲基、及對g太故及己内醴胺之共聚醯胺、聚 (4·胺基丁酸)(耐綸4)、聚(8-胺基辛酸)(耐綸8)、聚(七亞 甲基庚二醯胺)(耐綸7,7)、聚(八亞甲基辛二醯胺)(耐紛 8,8)、聚(九亞甲基壬二醯胺)(耐綸9,9)、聚(十亞甲基壬 二醯胺)(耐綸1〇,9)、聚(十亞甲基癸二醯胺)(耐綸1〇,1〇) 、聚[雙(4 -胺環己基)甲烷-1,1 〇 ·癸烷二碳醯胺]、聚(間二 甲苯己二醯胺)、聚(對二甲苯癸二醯胺)、聚(2,2,2-三甲 基π亞甲基庚二醯胺)、聚(六氫吡畊癸二酸胺)、聚(1 1 _胺 基十一酸)(耐綸11)、聚六亞甲基異酞醯胺、聚六亞甲基對 酞醯胺、及聚(9-胺基壬酸)(耐綸9)聚己醯胺。亦可使用共 聚醯胺,例如,聚(六亞甲基-共_2•甲基五亞甲己二醯胺) ,其中六亞甲基基團可以全體二胺衍生基團之約75_9〇莫耳 百分比存在。 有用的聚晞烴包括聚丙埽、μ乙缔、聚甲基戊燒及乙婦 或丙烯之一者以上與其他不飽和單體之共聚物及三元聚合 物。舉例來說’包含非彈性聚丙埽翼及彈性聚丙#芯之^ 維係在本發明之範圍内;此種纖維為雙成份纖維。 彈性及非彈性聚合物之組合可包括聚醚醢胺,例如,聚 ㈣酿胺彈性芯與聚酿胺翼及聚趟酉旨彈性芯與聚黯翼。舉 例來說,翼聚合物可包括耐紛6,6、及其之共聚 如, O:\74\74152-9UOl8.DOO 4 -20- 580527Line 580527 A7 ______B7 V. Description of the invention (17) Methyl dodecyl siamine (Nylon 6,12); Dodecane diamine and polymethyleneamine of n-dodecane diacid (Nylon 12, 12) , PACM-12 polyamide derived from bis (4-aminocyclohexyl) methane and dodecanedioic acid, 30% hexamethylenediammonium isophthalate and 70% hexamethylenediammonium adipate Copolyamide, up to 30% of bis (p-amidocyclohexyl) methylene, and copolyamide of g Taicao and caprolactam, poly (4.aminobutyric acid) (Nylon 4), poly (8-aminooctanoic acid) (Nylon 8), poly (heptamethyleneheptamidamide) (Nylon 7,7), poly (octamethyleneoctanediamine) (resistant to 8,8), poly (nonmethylenenonamide) (Nylon 9,9), poly (decamethylenenonamide) (Nylon 10,9), poly (decamethylene Sebacamide) (Nylon 10,10), poly [bis (4-aminecyclohexyl) methane-1,1.10-decanedicarbamide], poly (m-xylylenediamine) , Poly (p-xylylenesecandiamine), poly (2,2,2-trimethylπmethyleneheptanediamine), poly (hexahydropyridine sebacate), poly (1 1 _ Amine Undecanoic acid) (nylon 11), polyhexamethylene isophthalic Amides, polyhexamethylene terephthalate Amides, and poly (9-amino nonanoic acid) (nylon 9) Amides polycaprolactam. Copolyamide can also be used, for example, poly (hexamethylene-co_2methylmethylpentanehexamethylene diamine), in which the hexamethylene group can be about 75-9 mol of the total diamine-derived group. Ear percentage is present. Useful polyalkylene hydrocarbons include copolymers and terpolymers of one or more of polypropylene, mu ethylene, polymethylpentane, and ethyl or propylene with other unsaturated monomers. By way of example, it is within the scope of the present invention to include a non-elastic polypropylene wing and an elastic polypropylene core; such fibers are bicomponent fibers. The combination of elastic and non-elastic polymers may include polyetheramide, for example, polyamine elastomer cores and polyamine wings, and polyammonium elastomer cores and polyhex wings. For example, wing polymers can include resistant 6,6, and copolymers thereof, such as O: \ 74 \ 74152-9UOl8.DOO 4 -20- 580527

聚(六亞甲基-共-2-甲基五亞甲己二醯胺),其中六亞甲基 基團係以約8 0莫耳百分比存在,其視需要可與約1 %直至約 1 5重量百分比之耐綸_丨2混合,及芯聚合物可包括彈性片段 聚醚酯醯胺。「片段聚醚酯醯胺」係指具有共價鍵結(藉由 酯基團)至硬片段(短鏈聚醯胺)之軟片段(長鏈聚醚)的聚合 物。類似的定義對應於片段聚醚酯、片段聚胺甲酸酯、及 其類似物。耐綸12可改良翼對芯的黏著,尤其係當芯係以 購自Atofina之PEBAXtm 3533SN為主材料時。另一較佳的 翼聚合物可包括選自聚(對酞酸乙二酯)及其共聚物、聚(對 酞酸丙二酯)、及聚(對酞酸丁二酯)之群的非彈性聚酯;適 5配合其使用之彈性芯可包括包含選自聚(四亞甲基醚)二 元醇及氷(四亞曱基-共-2-甲基四亞甲基_)二元醇之群之 聚醚二元醇與對酞酸或對酞酸二甲酯及選自丨,3•丙二醇及 1,4-丁二醇之群之低分子量二元醇之反應產物的聚醚酯。 亦可將彈性聚醚酯芯與非彈性聚醯胺翼配合使用,尤其 係當使用如說明於文中他處之黏著促進添加劑時。舉例來 說此纖維之翼可選自(a)聚(六亞甲基己二酿胺)及其與 2-甲基五亞甲二胺之共聚物及(b)聚己内醯胺之群,及此一 纖維之芯可選自(a)聚醚酯醯胺及(b)聚(四亞甲基酸)二元 醇或聚(四亞甲基-共-2-甲基四亞甲基醚)二元醇與對酞酸 或對酞酸二甲酯及選自丨,3·丙二醇及丨,4_丁二醇之群之二 元醇之反應產物之群。 技藝中知曉製造前述聚合物之方法,且其可包括使用技 蟄中所知曉之催化劑、輔催化劑、及鏈支化劑。 O:\74\74152-91 l〇18.D〇a -21 - 580527Poly (hexamethylene-co-2-methylpentamethylene hexamethylene diamine), in which the hexamethylene group is present at about 80 mole percent, which can be from about 1% up to about 1 if necessary 5 weight percent of nylon 2 blends, and the core polymer may include elastomeric polyetheresteramide. "Fragmented polyetheresteramide" means a polymer having a covalent bond (via an ester group) to a soft segment (long-chain polyether) of a hard segment (short-chain polyamine). Similar definitions correspond to fragmented polyetheresters, fragmented polyurethanes, and the like. Nylon 12 improves the adhesion of the wings to the core, especially when the core is based on PEBAXtm 3533SN purchased from Atofina. Another preferred wing polymer may include a non-selective group selected from the group consisting of poly (ethylene terephthalate) and its copolymers, poly (propylene terephthalate), and poly (butylene terephthalate). Elastic polyester; suitable elastic core for use with it may include a binary selected from poly (tetramethylene ether) glycol and ice (tetramethylene-co-2-methyltetramethylene) Polyether diol of a group of alcohols and a polyether of a reaction product of terephthalic acid or dimethyl terephthalate and a low molecular weight diol selected from the group of 3,3-propanediol and 1,4-butanediol ester. It is also possible to use an elastic polyetherester core with a non-elastic polyamide wing, especially when using an adhesion promoting additive as described elsewhere in the text. For example, the wing of this fiber may be selected from (a) poly (hexamethylenehexamethylenediamine) and its copolymer with 2-methylpentamethylenediamine and (b) a group of polycaprolactam And the core of this fiber may be selected from (a) polyetheresteramide and (b) poly (tetramethylene acid) diol or poly (tetramethylene-co-2-methyltetramethylene) A group of reaction products of a dihydric alcohol with terephthalic acid or dimethyl terephthalate and a diol selected from the group consisting of 丨, 3 · propylene glycol and 丨, 4-butanediol. Methods for making the aforementioned polymers are known in the art, and may include the use of catalysts, cocatalysts, and chain branching agents known in the art. O: \ 74 \ 74152-91 l〇18.D〇a -21-580527

—當纖維被伸展及鬆弛時,芯之高彈性使其可吸收其被附 著翼扭轉所產生的壓縮力、扭力及伸展力。如兩聚合物之 附耆太弱的話,此等力將會造成其之脫層。本發明視需要 可使用翼及芯聚合物之機械鎖緊作用於增進附著,及進一 步使當纖維加工及使用時之脫層減至最小。芯及翼之間的 黏合可經由選擇翼及芯組合物及/或對任一或兩聚合物使用 黏著促進添加劑,而再進一步增進。可於各翼或僅於一些 翼中使用黏著促進劑。因此,個別的翼可對芯具有不同的 脫層程度,例如,可故意使一些翼脫層。此種添加劑之一 例子為例如,以總翼聚合物計為5重量百分比之耐綸12,即 聚(12-十二内醯胺),亦稱為r 12」或「N12」,其可於市 面購自Atofina之Riisan®「ΑΜΝΟ」。此外,可使用順丁 缔二酸酐衍生物(例如,Bynel® CXA 一杜邦公司(Ε· I. du Pont de Nemours and Company)之註冊商標,或L〇tader@ · 購自AtoHna之乙婦/丙晞酸酯/順丁烯二酸酐三元聚合物)於 改進聚醚-醯胺彈性,以改良其對聚醯胺之黏著。 另一例子為可將熱塑性可溶可熔(n〇v〇lac)樹脂,例如具 有在約400至約5000之範圍内之數目平均分子量的 HRJ12700(Schenectady International),加至彈性(共)聚醚 酷芯,以改良其對(共)聚醯胺翼之黏著。可溶可熔樹脂之 量應在1-20重量百分比之範圍内,更佳的範圍為2-1〇重量 百分比。有用於此之可溶可熔樹脂的例子包括,但不限於 ,紛-甲酸、間私二紛-曱駿、對丁紛-甲酸、對乙紛·甲駿、 對己酚-甲醛、對丙酚-甲醛、對戊酚-甲醛、對辛酚-曱醛、 O:\74\74152*9 U 018.DOQ 4 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐) -22- 580527 A7 B7-When the fiber is stretched and relaxed, the high elasticity of the core allows it to absorb the compressive, torsional and stretching forces produced by the twist of the attached wings. If the adhesion of the two polymers is too weak, these forces will cause their delamination. According to the present invention, mechanical locking of wings and core polymers can be used to improve adhesion and further minimize delamination during fiber processing and use. The adhesion between the core and the wings can be further enhanced by selecting the wing and core composition and / or using adhesion promoting additives to either or both of the polymers. Adhesion promoters can be used on each wing or only on some wings. Thus, individual wings may have different degrees of delamination from the core, for example, some wings may be deliberately delaminated. An example of such an additive is, for example, 5 weight percent nylon 12 based on total wing polymer, namely poly (12-dodecylamine), also known as r 12 "or" N12 ", which can be used in Riisan® "ΑΜΝΟ" is commercially available from Atofina. In addition, a maleic anhydride derivative (for example, a registered trademark of Bynel® CXA-Du Pont de Nemours and Company) or Lotader @ · Otome / C from AtoHna can be used Triester / maleic anhydride terpolymer) is used to improve the elasticity of polyether-amidamine to improve its adhesion to polyamidamine. Another example is the addition of a thermoplastic soluble and soluble (novolac) resin, such as HRJ12700 (Schenectady International), which has a number average molecular weight in the range of about 400 to about 5000, to an elastic (co) polyether. Cool core to improve its adhesion to (co) polyamide wings. The amount of soluble and fusible resin should be in the range of 1-20 weight percent, and more preferably in the range of 2-10 weight percent. Examples of soluble and fusible resins used for this include, but are not limited to, phenol-formic acid, saccharine-peptone, p-butyl phenol-formic acid, p-ethyl benzoate, p-methyl phenol, formaldehyde, p-propyl Phenol-formaldehyde, p-pentol-formaldehyde, p-octylphenol-acetaldehyde, O: \ 74 \ 74152 * 9 U 018.DOQ 4 This paper size applies to China National Standard (CNS) A4 (210 X 297 mm)- 22- 580527 A7 B7

對庚酚-曱醛、對壬酚-甲醛、雙酚A -甲醛、羥萘甲醛及松 香(尤其係經部分順丁晞二酸化之松香)之烷基·(諸如第三 基-)酚改質酯(諸如異戊四醇酯)。參見1999年8月27曰提出 申請之經許可之美國專利中請案序勤9/384,6()5之關於提供 在共聚酯彈性與聚醯胺之間之改良黏著之技術的例子。 、亦可將利用順丁晞二酸纤(「M A」)官能化之聚醋使用作 為黏著促進添加劑。例如,可根據JM· BhaUacharya,聚 合物國際(Polymer lnternati〇nal) (2〇〇〇年8月),49:8 , 860-866頁(將其以引用的方式併入本文中),於雙螺桿擠製 機中經由自由基接枝利用MA將聚(對酞酸丁二酯「pB 丁」 )耳能化,J.M· Bhattacharya亦記述將數重量百分比之生成 之PBT-g-MA使用作為聚(對酞酸丁二酯)與耐綸66及聚(對 酞酸乙二酯)與耐綸6 6之二元摻混物的相容劑。舉例來說, 可使用此一添加劑於將(共)聚醯胺翼更緊密地黏著至本發 明之纖維之(共)聚醚酯芯。 使用於本發明之聚合物及生成之纖維、紗、及物件可包 括習知之添加劑,其係在聚合方法中加入或加至形成之聚 合物或物件,且其可促進聚合物或纖維性質之改良。此等 添=劑之例子包括抗靜電劑、抗氧化劑、抗微生物劑、防 火^、术料、光安定劑、聚合催化劑及助劑、黏著促進劑 、褪光劑諸如二氧化鈦、消光劑、及有機磷酸鹽。 其他可在’例如,抽絲及/或拉伸方法中塗布於纖維上之 添加劑包括抗靜電劑、光滑劑、黏著促進劑、親水劑、抗 氧化劑、抗微生物劑、防火劑、潤滑劑、及其之組合。此 O:\74\74152.911018.DOC\ -23- A7 B7 五、發明説明(21 ^卜,此等額外之^劑可在如技藝巾所知曉之方法的各個 步驟中加入。 雖然上述說明著眼於當纖維具有實質上徑向對稱之橫剖 :時《優點,然通常希望此種對稱性於本發明之下列具體 實施態樣中為不需要者: (a) 可伸展合成聚合物纖維具有低於約丨之脫層評比及至 少約2 0 %之退漿後收縮率。 (b) 可伸展合成聚合物纖維具有至少約2〇%之退漿後收縮 率,且其需要低於約1G%之伸展以實f上地將纖維拉直; (c) 可伸展合成聚合物纖_包括含彈性聚合物纟軸芯及複 數個附著至芯之含非彈性聚合物之翼,其中芯在其之外表 面上在翼接觸芯的點之間包括非彈性聚合物之鞘; ⑷可伸展合成聚合物纖維包括含彈性聚合物之軸芯及複 數個附著至芯之含非彈性聚合物之翼,其中芯具有實質上 圓形或規則的多邊形橫剖面;或 (Ο可伸展合成聚合物纖維包括含彈性聚合物之軸芯及複 數個附著至芯之含非彈性聚合物之翼,其中至少一個翼具 有T、C、或s形狀。 本發明之纖維可為連續長絲(複絲紗或單絲)或定長短纖維 (包括,例如,絲束或細紗)的形態。本發明之拉伸纖維可 具有自約1 .5至約60之每根纖維的丹尼值(denier)(約丨7_ 67分德士(dtex))。具有聚醯胺翼之本發明之完全拉伸纖維 典J上具有約1.5至3.0克/分德士之韌度,及具有聚酯翼之 4、准為約1 - 2 · 5克/分德士,其係視翼/芯比而定。最終纖維 O:\74\74I52.9UOl8.DOa 4Alkyl- (such as tertiary-) phenol modification of p-heptanol-acetaldehyde, p-nonol-formaldehyde, bisphenol A-formaldehyde, hydroxynaphthaldehyde, and rosin (especially partially rosinated by rosin). Esters (such as isopentaerythritol esters). See, for example, a patent application filed on August 27, 1999, in U.S. Patent Application Serial No. 9 / 384,6 () 5 for an example of a technique for providing improved adhesion between copolyester elasticity and polyamide. 2. Polyvinyl functionalized with maleic acid fiber ("MA") can also be used as an adhesion promoter. For example, according to JM · BhaUacharya, Polymer International (August 2000), 49: 8, 860-866 (incorporated herein by reference), both In a screw extruder, poly (butylene terephthalate "pB butyl") is ear-enhanced by MA via free-radical grafting. JM · Bhattacharya also described using PBT-g-MA produced as a polymer in a percentage by weight. Compatibility with binary blends of (butyl phthalate) and nylon 66 and poly (ethylene terephthalate) and nylon 6 6. For example, this additive can be used to more closely adhere the (co) polyamide wings to the (co) polyetherester core of the fibers of the present invention. The polymers used in the present invention and the resulting fibers, yarns, and articles may include conventional additives that are added to or added to the polymer or article formed during the polymerization process, and that can promote the improvement of polymer or fiber properties . Examples of such additives include antistatic agents, antioxidants, antimicrobial agents, fire retardants, materials, light stabilizers, polymerization catalysts and auxiliaries, adhesion promoters, matting agents such as titanium dioxide, matting agents, and organic Phosphate. Other additives that may be applied to the fibers in the drawing and / or drawing process include antistatic agents, smoothing agents, adhesion promoters, hydrophilic agents, antioxidants, antimicrobial agents, fire retardants, lubricants, and Its combination. This O: \ 74 \ 74152.911018.DOC \ -23- A7 B7 V. Description of the invention (21 ^ Bu, these additional agents can be added in each step of the method as known in the art towel. Although the above description focuses on When the fiber has a substantially radial symmetrical cross-section: "Advantage, but it is generally desirable that this symmetry is not needed in the following specific embodiments of the present invention: (a) Extensible synthetic polymer fibers have Delamination ratio of about 丨 and shrinkage after desizing of at least about 20%. (B) The stretchable synthetic polymer fiber has a shrinkage after desizing of at least about 20%, and it needs to be less than about 1G%. Stretching to straighten the fiber; (c) Extensible synthetic polymer fiber-including an elastic polymer-containing spool core and a plurality of non-elastic polymer-containing wings attached to the core, with the core outside of it The surface includes a sheath of non-elastic polymer between the points where the wings contact the core; 伸展 The stretchable synthetic polymer fiber includes a shaft core containing an elastic polymer and a plurality of non-elastic polymer-containing wings attached to the core, where the core Have a substantially circular or regular polygonal cross section; or (〇 The stretch synthetic polymer fiber includes an elastic polymer-containing shaft core and a plurality of non-elastic polymer-containing wings attached to the core, at least one of which has a T, C, or s shape. The fibers of the present invention may be continuous filaments (Multifilament yarn or monofilament) or fixed-length staple fibers (including, for example, tows or spun yarns). The drawn fibers of the present invention may have a denier value per fiber from about 1.5 to about 60 ( denier) (about 7-7 67 dtex). The fully drawn fiber code J of the present invention having a polyamide wing has a tenacity of about 1.5 to 3.0 g / dtex and a polyester wing No.4 The standard is about 1-2.5 g / dtex, which depends on the wing / core ratio. The final fiber O: \ 74 \ 74I52.9UOl8.DOa 4

580527 22 五、發明説明( 可具有至少約20%之退聚後伸展。為 成之織物中具有較大的伸展 * H維製 45%之退漿後伸展。 減維可具有至少約 當製造包含複數根纖維之紗時,此纖料為 纖維數及任何期望的dpf’且各纖維之彈 二:: 之比可不同。複絲紗可包含複數根不同纖維,例如,= 剛根纖維。此外,包含本發明之纖維㈣可 自2至 每根纖維的線性密度’且亦可包括不為本發明;纖維 可使用本發明之合成聚合物纖維,利用已知之方式勺 Π用Si經向針織、緯向(包括圓形)針織、或:織: ’十減’形成織物。此種織物具有優異的伸展及回復力。此 = = 纺織品及織物,諸如椅套’及衣物(包括亞麻 U針D ’以形成衣物之全部或—部分,包括窄幅布 。經發現使用本發明之纖維及紗製得之服裝,諸如針織品 ’及織物光滑、質輕 '且非常均勻(「無打毛」),且具有 良好的伸展及回復性質。 此外,根據本發明,提供一種將連續聚合物纖維抽絲之 溶融抽絲方法1參照圖7說明此方法,圖7係可使用於製 造本發明之纖維之裝置的略圖。然而,應明瞭亦可使用其 他裝置。本發明之方法包括使包含彈性聚合物之熔體通過 噴j板,而形成複數個包括含彈性聚合物之軸芯及複數個 附著至芯且包含非彈性聚合物之翼的可伸展合成聚合纖維 。參照圖7,將未示於圖中之熱塑性硬聚合物供給於2〇引入 土抽絲封裝組合3 〇,及將未示於圖中之熱塑性彈性聚合物 O:\74\74152-9n018.DOa -25- 580527 A7 B7 五、發明説明( 23 供給於22引入至抽絲封裝組合30。可使用前凝結或後凝結 嘴絲板封裝。可將兩聚合物自具有經設計成可產生期望橫 剖面之孔口之堆疊板噴絲板組合35擠製成為未拉伸長 。本發明之方法更包括於長絲離開噴絲板之毛細孔後,以 任何已知之方式使其騾冷,而使長絲冷卻,例如利用在圖了 之50的冷空氣。可使用任何適當的驟冷方法,諸如橫向流 動的空氣或徑向流動的空氣^ 、 視需要可使用任何已知之技術,在如圖7所示之處理劑塗 布機60,以處理劑,諸如視需要可具有硬脂酸鎂之矽酮油 ,處理長絲。然後於驟冷之後將此等長絲拉伸,以致其展 現至少約20%之退漿後伸展。可於至少一拉伸步驟中將長 絲拉伸,例如在概略示於圖7之進給輥8〇(其可在15〇至 1000米/分鐘下操作)與牵引輥90之間,以形成拉伸長絲1〇〇 。可將拉伸步驟與抽絲結合,而製造完全拉伸紗,或如須 要部分取向紗,則在分裂方法中在抽絲與拉伸之間有所延 遲。亦可在將長絲捲起成為經紗的過程中完成拉伸;熟悉 技藝人士將其稱之為「拉伸整經(draw warping)」。可賦予 長絲任何期望的拉伸比(除了會經由使長絲斷裂而干擾加工 者外),例如,可利用約3·〇至4 ·5倍之牽伸比製造完全取向 紗,及利用約1.2-3.0倍之牵伸比製造部分取向紗。在此, 牵伸比係奪引輥90的外圍速度除以進給輥8〇的外圍速度。 可在約15-10〇。(:下進行拉伸,典型上係約15-4〇。〇。 視需要可將拉伸長絲1〇〇部分鬆弛,例如,利用在圖7之 11 〇的蒸氣。可在抽絲過程中進行任何量的熱鬆弛。鬆弛作580527 22 V. Description of the invention (can have at least about 20% stretch after depolymerization. There is a large stretch in the finished fabric * H dimension stretch 45% after desizing stretch. Dimension reduction can have at least about when manufacturing includes In the case of a yarn of a plurality of fibers, the fiber material is the number of fibers and any desired dpf 'and the ratio of the elastic two of each fiber :: may be different. The multifilament yarn may include a plurality of different fibers, for example, = rigid fiber. In addition Including the fiber of the present invention, it can be from 2 to the linear density of each fiber 'and can also include the present invention; the fiber can use the synthetic polymer fiber of the present invention, using a known method to knit Si warp, Weft (including circular) knitting, or: Weaving: 'ten minus' to form a fabric. This fabric has excellent stretch and restoring force. This = = textiles and fabrics such as seat covers' and clothing (including linen U needles) D 'to form all or part of the garment, including narrow fabrics. Garments made using the fibers and yarns of the present invention, such as knitwear, and fabrics were found to be smooth and lightweight' and very uniform ("no fuzzing" ), And has a good extension In addition, according to the present invention, there is provided a melt-spinning method 1 for spinning continuous polymer fibers. This method will be described with reference to FIG. 7, which is a schematic view of an apparatus that can be used to manufacture the fibers of the present invention. However, It should be understood that other devices can also be used. The method of the present invention includes passing a melt containing an elastic polymer through a spray plate to form a plurality of shaft cores including an elastic polymer and a plurality of cores attached to the core and containing a non-elastic polymer. The stretchable synthetic polymer fiber of the wing. Referring to FIG. 7, a thermoplastic hard polymer (not shown in the figure) is supplied to 20, a silk-drawing encapsulation combination 3 is introduced, and a thermoplastic elastic polymer (not shown) is provided. : \ 74 \ 74152-9n018.DOa -25- 580527 A7 B7 V. Description of the invention (23 supplied to 22 introduced into the drawing package 30. It can be packaged with front condensation or rear condensation nozzle silk plate. Two polymers can be The stacked plate spinneret assembly 35 having orifices designed to produce the desired cross-section is extruded into an unstretched length. The method of the present invention further comprises, after the filament leaves the orifice of the spinneret, any known square Let it chill and cool the filaments, for example with cold air as shown in Figure 50. Any suitable quenching method may be used, such as laterally flowing air or radially flowing air ^, and any In a known technique, filaments are treated with a treating agent such as a silicone oil which may have magnesium stearate if necessary, in a treating agent coating machine 60 as shown in FIG. 7. Then, the filaments are drawn after quenching. So that it exhibits at least about 20% stretch after desizing. The filaments can be stretched in at least one stretching step, such as in the feed roller 80 (shown in FIG. 7 which can be between 15 and 1000 meters) / Minute operation) and traction roller 90 to form a drawn filament 100. The drawing step can be combined with drawing to make a fully drawn yarn, or if a partially oriented yarn is required, the splitting method There is a delay between drawing and stretching. It can also be stretched during the process of winding the filaments into warp yarns; those skilled in the art will call it "draw warping." The filament can be given any desired draw ratio (except that it will interfere with the processor by breaking the filament), for example, a fully oriented yarn can be made with a draft ratio of about 3.0 to 4.5 times, and about A draft ratio of 1.2 to 3.0 times is used to make a partially oriented yarn. Here, the draft ratio is the peripheral speed of the take-up roller 90 divided by the peripheral speed of the feed roller 80. Available at about 15-10. (: The drawing is carried out below, typically about 15-4. 0. The drawn filament can be partially relaxed if necessary, for example, using the steam of 1 10 in Fig. 7. It can be used during the drawing process. Perform any amount of thermal relaxation.

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580527 A7 -----------^________ 五、發明説明(24 ) 用愈大,則長絲愈有彈性,且在下游的操作中將產生較少 的收縮率。於經如下所述之鬆弛後之經拉伸的最終纖維可 具有至少約20%之退漿後伸展。以在將拉伸長絲捲起之前 之其長度計,將剛抽絲得之長絲熱鬆弛約1-3 5%較佳,以 致可將其以典型的硬紗操縱。 然後可經由在圖7中之收捲機130以每分鐘2〇〇至約35〇〇米 ,及至高每分鐘4000米之速度收捲,而收集經驟冷、拉伸 及視需要經鬆弛的長絲。或如將多根纖維抽絲及驟冷, 則可將纖維聚集,視需要經交織,然後再例如,在至高每 分鐘4000米下,收捲於收捲機13〇,例如在每分鐘約2〇〇至 約3500米之範圍内。單絲或複絲紗可以相同的方式收捲於 圖7中 < 收捲機13〇。當複絲經抽絲及驟冷時,可如技藝中 在收捲之前將長絲聚集及視需要交織。 可於拉伸之後的任何時刻,將雙組成長絲乾或濕熱處理 同時疋全鬆弛,以產生期望的伸展及回復性質。此種鬆 弛作用可於長絲製造過程中完成,例如在前述的鬆弛步驟 中,或於將長絲合併成紗或織物之後,例如在煮煉、染色 、及其類似步驟中。纖維或紗形態之熱處理可使用孰輕或 熱箱,或於例如,射流網增量⑽都㈣她㈣步驟中進 行。此種鬆弛熱處理可於纖維呈紗或織物形 佳,以致在該時刻之前,可將其如 了』心引J將其如问非彈性纖維般之加工 :然而,若須要’可在將其捲起成為高伸展纖維之前,將 ,、熱處理及完全鬆弛。為於最終織物中得到較大均勻度, 可將纖維均勾地熱處理及鬆他。熱處理/鬆他溫度當加熱介 O:\74\74I52-9HOI8.DOO 4 本紙張I度通财s s家標準(CNS) A4規格(210^^jy 580527 A7580527 A7 ----------- ^ ________ V. Description of the Invention (24) The larger the use, the more elastic the filament will be, and it will produce less shrinkage in downstream operations. The final fiber drawn after relaxation as described below may have a desizing stretch of at least about 20%. Based on the length of the drawn filament before it is wound up, it is better to thermally relax the filament just drawn to about 1-3 5%, so that it can be manipulated with a typical hard yarn. Then, it can be wound up through the winder 130 in FIG. 7 at a speed of 2000 to about 35,000 meters per minute, and up to 4,000 meters per minute, to collect the quenched, stretched and relaxed as needed. Filament. Or if multiple fibers are drawn and quenched, the fibers can be aggregated and interlaced as needed, and then, for example, wound up at a winder 13 at a height of 4000 meters per minute, for example at about 2 per minute Within the range of 0 to about 3500 meters. Monofilament or multifilament yarns can be wound up in the same manner in Fig. 7 < winder 13o. When the multifilament is drawn and quenched, the filaments can be gathered and interlaced as necessary before winding. At any time after stretching, the bi-component filaments can be dried or wet-treated simultaneously and fully relaxed to produce the desired stretch and recovery properties. Such relaxation can be accomplished during the manufacturing of the filaments, for example during the aforementioned relaxation steps, or after the filaments are combined into yarn or fabric, for example during the scouring, dyeing, and the like steps. The heat treatment of the fiber or yarn form can be performed in a light or hot box, or in, for example, a spray screen increase step. This relaxation heat treatment can be done when the fiber is in the shape of a yarn or fabric, so that it can be treated before that moment. It can be processed like a non-elastic fiber: However, if you need to It will be heat treated and fully relaxed before becoming high stretch fiber. In order to obtain greater uniformity in the final fabric, the fibers can be heat treated and loosened. Heat treatment / Songta temperature as the heating medium O: \ 74 \ 74I52-9HOI8.DOO 4 This paper I degree of wealth s s home standard (CNS) A4 specifications (210 ^^ jy 580527 A7

質為乾燥空氣時,其可在約8〇t:至約12〇。〇之範圍内,當加 齡質為熱水時約為7代至約⑽。c,及當加熱介質為:過 大氣壓力之蒸氣(例如於熱壓釜中)時約為1〇rc至約 。較低的溫度會產生過少或不產生熱處理,及較高的溫度 會將彈性芯聚合物熔融。熱處理/鬆弛步驟一般可於數秒内 完成。When the quality is dry air, it can be from about 80 to about 120. In the range of 0, when the ageing quality is hot water, it is about 7 generations to about ⑽. c, and when the heating medium is: steam at atmospheric pressure (for example, in an autoclave), about 10rc to about. Lower temperatures will produce too little or no heat treatment, and higher temperatures will melt the elastic core polymer. The heat treatment / relaxation step is typically completed in seconds.

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如前所指,噴絲板毛細孔具有對應於如前所述之本發明 之纖維之期望橫剖面,或產生其他雙組成或雙成份纖纟=之 汉计。如技藝中所知曉,毛細孔或噴絲板鑽孔可利用任何 適當的方法切割,諸如利用雷射切割(如說明於美國專利第 5,168,143號)、鑽孔、電子放電機器加工(EDM)、及衝孔。 可使用雷射光束切割毛細孔口,以良好地控制本發明纖維 之橫剖面對稱性。噴絲板毛細孔之孔口可具有任何適當尺 寸,且可經切割成為連續(前凝結)或非連續(後凝結)。二經 由以可使聚合物在噴絲板面之下方凝結及形成本發明之多 翼橫剖面的形態鑽出小孔,而製得非連續的毛細孔。 舉例來說,可利用如圖8、8A、88及8〇所說明之前凝結 噴絲板封裝製造本發明之長絲。圖8顯示圖7所示之噴絲^ 組合堆疊板的側立面,其中聚合物之流動係在箭頭F的方向 。噴絲板組合中之第一板為包含聚合物熔體池之板1),且其 係為習知之設計。板D靜置於計量板C(其之橫剖面圖示於 圖8C)上,其依序再靜置於靜置在噴絲板A(其之橫剖面圖 示於圖8A)上之非必需之分佈板B(其之橫剖面圖示於圖8" 上,噴絲板A係由噴絲板組合支承板E所支承。計量板(:係 O:\74\74152-9I1018.DOa 4 - 28 -As mentioned before, the spinneret pores have the desired cross-section corresponding to the fibers of the present invention as previously described, or produce other bi-component or bi-component fibers =. As is known in the art, capillary or spinneret drilling can be cut by any suitable method, such as laser cutting (as described in U.S. Patent No. 5,168,143), drilling, electronic discharge machining ( EDM), and punching. Capillary apertures can be cut using a laser beam to better control the cross-sectional symmetry of the fibers of the present invention. The orifice of the spinneret pores can be of any suitable size and can be cut to be continuous (pre-condensation) or discontinuous (post-condensation). Secondly, non-continuous capillary pores are made by drilling small holes in a form that allows the polymer to condense below the spinneret surface and form the multi-wing cross section of the present invention. For example, the filaments of the present invention can be manufactured using a previously condensed spinneret package as illustrated in Figures 8, 8A, 88, and 80. FIG. 8 shows the side elevation of the spinneret ^ combined stacking plate shown in FIG. 7, where the polymer flow is in the direction of arrow F. FIG. The first plate in the spinneret combination is a plate 1) containing a polymer melt pool, and it is a conventional design. Plate D is statically placed on the metering plate C (the cross-sectional view of which is shown in FIG. 8C), and it is sequentially placed on the spinneret A (the cross-sectional view of which is shown in FIG. 8A). The distribution plate B (its cross-section is shown in Fig. 8), the spinneret A is supported by the spinneret combination support plate E. Metering plate (: Department O: \ 74 \ 74152-9I1018.DOa 4- 28-

580527 A7 一 —__ B7 五、發明説明(26 ) 與在計量板下方之分佈板B對齊及接觸,分佈板係在具有貫 穿之毛細孔,但無實質之柱坑之噴絲板A的上方,與其對齊 ,並與其接觸,噴絲板係與具有較毛細孔大之孔之噴絲板 支承板(E)對齊及接觸。其之排列方式係使得供給至計量板 C之聚合物可通過分佈板B、噴絲板A及噴絲板支承板E, 而形成纖維。使用為習知之板的熔體池板D於供給計量板。 聚合物熔體池板D及噴絲板組合支承板E夠厚及夠剛硬,以 致其可緊密地彼此相壓,因此而防止聚合物在喷絲板組合 之堆疊板之間洩漏。板A、B、及C夠薄,以致可利用雷射 光方法切割孔口。噴絲板支承板(E)中之孔係以,例如, 45。-60°張開,以致剛抽絲得之纖維不會觸及孔之邊緣較 佳。當須要聚合物之前凝結時,在形成纖維之前,使聚合 物彼此接觸(前凝結)低於約〇·30公分,一般係低於〇15公分 亦較佳,以致可於纖維中更準確地展現由計量板C、非必需 之分佈板D、及噴絲板設計E所設計的橫剖面形狀。亦可經 由如美國專利第5,168,143號所說明將孔切割通過板,而更 促進纖維橫剖面之更精確的界定,其中將來自固態雷射之 多模光束降低至主要為單模的光束(例如模式),及聚 焦至直低於1〇〇微米,及在金屬片材上方〇 2至〇 3毫米之 點。利用與雷射光束同軸流動之加壓流體,將所產生之溶 化金屬自金屬片材之下表面排出。可將自最上方之分佈板 的頂端至嘴絲板面的距離降至低於約〇 〇公分。 為製造具有任何數目之對稱設置翼聚合物部分之長絲, 在各板中使用相同數目之對稱設置的孔口。舉例來說,圖 O:\74\74152-9U018.DOa 4580527 A7 I -__ B7 V. Description of the invention (26) Align and contact the distribution plate B below the metering plate. The distribution plate is above the spinneret A, which has a capillary hole that penetrates, but no substantial pillar pit. Aligned with and in contact with it, the spinneret is aligned with and in contact with the spinneret support plate (E) with a larger capillary hole. The arrangement is such that the polymer supplied to the metering plate C can pass through the distribution plate B, the spinneret A, and the spinneret support plate E to form fibers. A melt cell plate D, which is a conventional plate, is used for the supply metering plate. The polymer melt pool plate D and the spinneret combination support plate E are thick and stiff enough so that they can be pressed against each other tightly, thus preventing the polymer from leaking between the stacked plates of the spinneret combination. The plates A, B, and C are thin enough that the aperture can be cut by the laser light method. The hole in the spinneret support plate (E) is, for example, 45. It is better to open at -60 ° so that the fiber just drawn will not touch the edge of the hole. When the polymer is required to coagulate before contacting the polymers (former coagulation) below about 0.30 cm before forming the fibers, generally less than 0.15 cm is also preferred, so that it can be more accurately displayed in the fibers The cross-sectional shape designed by the metering plate C, the optional distribution plate D, and the spinneret design E. A more precise definition of the fiber cross section can also be promoted by cutting the holes through the plate as described in U.S. Patent No. 5,168,143, in which the multi-mode beam from a solid-state laser is reduced to a predominantly single-mode beam ( (E.g. mode), and focus to a point below 100 microns, and 0.02 to 0.3 mm above the metal sheet. The generated molten metal is discharged from the lower surface of the metal sheet by using a pressurized fluid flowing coaxially with the laser beam. The distance from the top of the uppermost distribution plate to the surface of the mouth wire plate can be reduced to less than about 0.00 cm. To make filaments with any number of symmetrically arranged wing polymer portions, the same number of symmetrically arranged orifices are used in each plate. For example, Figure O: \ 74 \ 74152-9U018.DOa 4

580527580527

8A顯示與圖7之堆疊板形態成9〇。方向之噴絲板A的平面圖 。圖8A中足板A包括連接至中心圓形噴絲板孔 142之六個對 稱設置的翼噴絲板孔口 14〇。各翼孔口 14〇可具有不同的寬 度144及146。圖8B顯不具有在開口端152變尖細至將分佈 孔口連接至中心圓1156之非必需之狹縫154之分佈孔口 15〇 的互補分佈板B。圖8C顯示具有翼聚合物之計量毛細孔16〇 及〜水口物之中%计量毛細孔丨62之計量板c。聚合物熔體 池板D可為技藝中之任何習知的設計。噴絲板支承板£具有 夠大,及自新抽絲得之長絲之路徑張開(例如以45_6〇。張開 )’以致長絲不會觸及孔之側面的通孔,如圖7及8的側立面 所π。堆登板組合—板八至〇—係經排列成使芯聚合物自聚合 物熔體池板D流過計量板C之中心計量孔162及流過6個小的 毛細孔164,流過分佈板β之中心圓形毛細孔156,流過喷絲 板、、且a板Α之中〜圓形毛細孔丨42,及經由喷絲板支承板ε 中之大的張開孔流出。在此同時,翼聚合物自聚合物熔體 池板D流過計量板C之翼聚合物計量毛細孔16〇,流過分佈 板B足分佈孔口 15〇(其中如存在非必需的狹缝154,則兩聚 合物先彼此接觸),流過噴絲板A之翼聚合物孔口14〇,及最 終經由噴絲板組合支承板E中之孔流出。 可使用本發明之噴絲板封裝於熔融擠製複數個合成聚合 物,而產生纖維。在本發明之噴絲板封裝中,由於喷絲板 不具有實質的柱坑,因而可將聚合物直接供應至噴絲板毛 細孔内。所明供貫質的柱坑係指任何存在柱坑之長度(包括 任何連接複數個毛細孔之入口的凹處)係低於噴絲板毛細孔 O:\74\74152-911018.DOO 4 本紙張尺度適用中S g家標準(CNS) A4規格(210X2dv^)8A shows the shape of the stacked plate of FIG. 7 as 90. A plan view of the spinneret A of the direction. The foot plate A in FIG. 8A includes six symmetrically arranged wing spinneret orifices 14 connected to a central circular spinneret orifice 142. Each wing orifice 14 may have different widths 144 and 146. Fig. 8B shows a complementary distribution plate B having a distribution orifice 15 which is tapered at the open end 152 to a non-essential slit 154 connecting the distribution orifice to the center circle 1156. FIG. 8C shows the metering pores 16 with wing polymer and the metering plate c of% metering pores 62 in the spout. The polymer melt cell plate D may be of any conventional design in the art. The spinneret support plate is large enough, and the path of the filament obtained from the new drawing is opened (for example, at 45-60. Open) so that the filament does not touch the through hole on the side of the hole, as shown in Figure 7 and The side elevation of 8 is π. The stacking board assembly—plates eight to zero—are arranged so that the core polymer flows from the polymer melt pool plate D through the center measuring hole 162 of the metering plate C and the six small capillary holes 164, and then through the distribution plate. The center circular capillary hole 156 of β flows through the spinneret, and the circular capillary hole 42 in the a plate A, and flows out through the large opening hole in the spinneret support plate ε. At the same time, the wing polymer flows from the polymer melt pool plate D through the wing polymer metering pores 16 of the metering plate C, and through the distribution plate B foot distribution orifice 15o (where there is a non-essential slit 154, the two polymers first contact each other), flow through the polymer orifice 14 of the wing of the spinneret A, and finally flow out through the holes in the spinneret support plate E. The spinneret of the present invention can be used to encapsulate a plurality of synthetic polymers by melt extrusion to produce fibers. In the spinneret package of the present invention, since the spinneret does not have a substantial column pit, the polymer can be directly supplied into the capillary holes of the spinneret. The stated pits of the supply and delivery means any length of pits (including any recesses connecting the entrances of multiple pores) which are lower than the pores of the spinneret. O: \ 74 \ 74152-911018.DOO 4 copies Paper size applies to Chinese Standard (CNS) A4 specification (210X2dv ^)

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580527 A7580527 A7

之長^的60% ’及以低相4Q%較佳。見圖9A,其顯示先 前技蟄《噴絲板的橫剖面,及圖9b&c,其顯示本發明之 喷絲板的橫剖面。在噴絲板中之纖維形成孔口的背側入口 處’直接將多成份聚合物流計量至特定點内可消除—般去 將多個聚合物流實質上在噴絲板孔口之前結合於進給通: 中時之聚合物移動的問題。 可經由使用在具有通過板以連接槽之適當孔之單一板之 一或兩側上之凹槽,而有用地將兩板之功能結合為一。舉 例來說可在噴絲板之上游側切割出凹處、槽及凹陷(例如 利用放電機器加工),且其可作為分佈通道或淺而薄弱的柱 坑0 可利用本發明之噴絲板封裝製造各種包括二或多個聚合 物之纖維。舉例來說,亦可製造未於文中揭示及/或提出專 利申叫之其他雙組成纖維及雙成份纖維,其包括揭示於美 國專利第4,861,660號 '第3,458,390號 '及第3,671,379號中之 橫剖面。生成纖維之橫剖面可為,例如,並排、偏心鞘_芯 、同心鞘·芯、翼_及_芯、翼-及-鞘·及芯等等。此外,可使 用本發明之嘴絲板封裝於將可分裂或不可分裂之纖維抽絲 〇 可修改本發明之噴絲板封裝,以獲致不同的多翼纖維, 例如’經由對不同的期望翼數改變毛細孔腳之數目,改變 狹逢尺寸以改變製造不同之每根長絲丹尼值或紗數所需, 或不同合成聚合物之用途所需之幾何參數。舉例來說,圖 1 0之具體貫施例顯示用於製造如例舉於以下之實施例7之具 O:\74\74152-9ll0l8.DOa 4 本紙張尺度制A4規格(21〇χΈ6 -31 - 裝 訂60% of the length ^ and 4Q% of the low phase are preferred. Fig. 9A shows a cross section of a spinneret of the prior art, and Fig. 9b & c shows a cross section of a spinneret of the present invention. At the back side entrance of the fiber-forming orifice in the spinneret, the metering of the multi-component polymer stream to a specific point can be eliminated-generally, multiple polymer streams are essentially combined with the feed before the orifice of the spinneret. General: Problem of polymer movement in the middle age. The function of the two boards can be usefully combined into one by using grooves on one or both sides of a single board having suitable holes through which the board connects grooves. For example, recesses, grooves, and depressions can be cut on the upstream side of the spinneret (for example, using discharge machining), and they can be used as distribution channels or shallow and weak pillar pits. 0 The spinneret package of the present invention can be used for packaging. Manufactures a variety of fibers that include two or more polymers. For example, other bi-component fibers and bi-component fibers that are not disclosed and / or claimed in the text can also be manufactured, including those disclosed in US Patent Nos. 4,861,660, '3,458,390' and 3,671,379 In the cross section. The cross section of the generated fiber may be, for example, side-by-side, eccentric sheath_core, concentric sheath · core, wing_and_core, wing-and-sheath · and core, and the like. In addition, the mouthpiece of the present invention can be used for packaging splittable or indivisible fibers. The spinneret package of the present invention can be modified to obtain different multi-wing fibers, for example, 'through different desired number of wings. Change the number of capillary pores, change the size of each pin to change the geometrical parameters required to make different denier values or yarns per filament, or different synthetic polymer applications. For example, the specific embodiment shown in FIG. 10 is used to manufacture a tool O as exemplified in Example 7 below: \ 74 \ 74152-9ll0l8.DOa 4 This paper is made in A4 size (21〇χΈ6 -31 -Binding

580527 五、發明説明 有三翼之纖維之相當薄的噴絲板封裝。在圖i〇a中,噴絲 =為⑴015英吋(0.038公分)厚,且其具有利用揭示於文中之 雷射光万法機械加工通過不銹鋼之整個厚度的孔口,此孔 口呈各具有兩寬度(分別具有長度144及146),且繞對稱中 心隔開120度對稱設置之三直翼14〇的形態;在毛細孔口的 上方並供柱坑。各翼14〇自其之尖端至中心與對稱中心一致 之0.012英吋(〇_〇3〇公分)直徑之中心圓形噴絲板孔m之圓 周為0.040英吋(0102公分)長。接下來參照圖1〇B,〇 〇1〇英 吋(0.025公分)厚度之分佈板B係同軸對齊於噴絲板八上,以 致分佈板B之各別的翼孔口 ι5〇係與喷絲板a之翼ι4〇對齊; 分佈板B之各翼孔口 15〇自其之尖端至對稱中心為〇 1375英 付(0·349公分)。計量板c(圖10C)為0.010英吋(0.025公分) 厚’且其具有〇·〇25英吋(0.064公分)直徑之孔160、0.015英 吋(0.038公分)直徑之孔162、及〇 〇1〇英吋(〇 〇25公分)直徑 之中心孔164。板C係與分佈板Β對齊,以致在使用時,由 熔體池板D(見圖1〇)供給至孔16〇之翼聚合物及供給至分佈 板C之孔162及164之芯聚合物經板Β分佈至板Α而形成纖維 ’其中翼穿透芯。在噴絲板A中並無柱坑,且板a、B、及 C之結合厚度僅為約〇·〇35英吋(0.089公分)。 在另一噴絲板封裝組合具體實施例中,未使用噴絲板支 承板E (見圖8 )。此舉例說明於以下的實施例8。在圖11A, 喷絲板A為0.3125英吋(0.794公分)厚,且各抽絲孔口具有 0.100英吋(0.2 54公分)直徑柱坑及在柱坑底部之0.015英吋 (0.03 8公分)長的毛細孔。如圖11A所示,嘴絲板A中之各噴 O:\74\74152-911018.DOa 4 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐)580527 V. Description of the invention A relatively thin spinneret package with three wings of fiber. In Figure i0a, the spinneret is ⑴015 inches (0.038 cm) thick and has holes that are machined through the entire thickness of stainless steel using the laser light method disclosed in the text. This hole has two holes each Width (with lengths 144 and 146, respectively), and three straight wings 1440 symmetrically arranged 120 degrees apart around the center of symmetry; above the capillary orifice and for column pits. Each wing 14 has a center circular spinneret hole m having a diameter of 0.012 inch (0-30 cm) that is coincident with the center of symmetry, and the circumference of the hole m is 0.040 inch (0102 cm) long. Next, referring to FIG. 10B, the distribution plate B having a thickness of 100 inches (0.025 cm) is coaxially aligned on the spinneret eight, so that the respective wing openings of the distribution plate B50 and the spinneret The wings of plate a are aligned at 40 °; the openings of each wing of distribution plate B are from 0. 1375 inches (0.349 cm) from the tip to the center of symmetry. The metering plate c (FIG. 10C) is 0.010 inches (0.025 cm) thick 'and has holes 162 with a diameter of 0.025 inches (0.064 cm), holes 162 with a diameter of 0.015 inches (0.038 cm), and 〇〇. A center hole 164 with a diameter of 10 inches (025 cm). Plate C is aligned with distribution plate B so that, in use, the melt polymer plate D (see FIG. 10) is supplied to the wing polymer in hole 16 and the core polymer is supplied to holes 162 and 164 in distribution plate C. Fibers are distributed through plate B to plate A to form fibers where the wings penetrate the core. There are no pillar pits in the spinneret A, and the combined thickness of the plates a, B, and C is only about 0.035 inches (0.089 cm). In another embodiment of the spinneret package combination, the spinneret support plate E is not used (see Fig. 8). This example is illustrated in Example 8 below. In FIG. 11A, the spinneret A is 0.3125 inches (0.794 cm) thick, and each spinning orifice has a pillar diameter of 0.100 inches (0.2 54 cm) and a pitch of 0.015 inches (0.03 8 cm) at the bottom of the pillar. Long pores. As shown in FIG. 11A, each spray in the nozzle silk plate A: O: \ 74 \ 74152-911018.DOa 4 This paper size applies to the Chinese National Standard (CNS) A4 specification (210 X 297 mm)

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線 -32- 580527 A7 B7 五、發明説明( 30 絲板孔口具有六個直的翼孔口 170,其各具有通過對稱中心 之長軸中心線,且具有0.035英吋(0.089公分)之自其尖端至 中心圓孔172之圓周的長度。自各翼之尖端至0.015英吋 (0·03 8公分)之長度174為0.004英吋(0.010公分)寬;長度176 為〇·020英吋(0.051公分)長及0.0028英吋(0.007公分)寬。將 各翼之尖端於尖端之一半寬度處圓弧切割。分佈板B(見圖 ΠΒ)為0.015英吋(〇〇38公分)厚,且具有六翼孔口,此孔口 各係正中位於噴絲板A中之相對柱坑之上,且經定向成使板 B中之各翼孔口與板a之翼孔口對齊。板b中之各翼孔口 15〇 為0.060英吋(0.152公分)長及0.020英吋(0.051公分)寬,且 將其尖端弄圓至0.010英吋(〇·〇25公分)之半徑。板b中之中 心孔152的直徑為〇·100英吋(0·254公分)。計量板c(見圖 11C)亦為〇·〇ΐ5英吋(0.038公分)厚。在板c,孔160具有 0.008英吋(0.020公分)之直徑,且其距形成纖維之芯之板β 及Α之中心孔162之中心o.ioo英吋(0.254公分)。將非彈性 翼聚合物供給至板C中之孔160,並通過板B及A之翼孔口 ’而形成纖維之翼。翼及芯聚合物先於在噴絲板A面上方 0.328英吋(0.833公分)之分佈板B之上方接觸,由噴絲板A 擠製得直徑0.080英吋(0.203公分)之纖維。板c係與板B對 齊,以致板C之六個孔160係在板B之翼孔口 150之中心線的 上方。將板排列成使供給至板C之孔162的彈性芯聚合物通 過中心。 由以下的非限制性實施例說明本發明。使用以下的試驗 方法。 〇:\74\74I52-9I1018.D〇a 4 •33- ψ 裝 訂线 -32- 580527 A7 B7 V. Description of the invention (30 silk plate orifices have six straight wing orifices 170, each of which has a long axis centerline passing through the center of symmetry, and has a 0.035 inch (0.089 cm) The length from the tip to the circumference of the center circular hole 172. The length 174 from the tip of each wing to 0.015 inches (0.03 cm) is 0.004 inches (0.010 cm) wide; the length 176 is 0.020 inches (0.051) Cm) length and 0.0028 inch (0.007 cm) width. Cut the tip of each wing in an arc at one and a half width of the tip. Distribution plate B (see Figure Π) is 0.015 inches (〇38 cm) thick and has Six-wing orifices, each of which is centered over the opposite pillar pit in spinneret A, and is oriented so that each wing orifice in plate B is aligned with the wing orifice in plate a. Each wing orifice 15 is 0.060 inches (0.152 cm) long and 0.020 inches (0.051 cm) wide, with its tip rounded to a radius of 0.010 inches (0.025 cm). Center in plate b The diameter of the hole 152 is 0. 100 inches (0. 254 cm). The metering plate c (see FIG. 11C) is also 0. 5 inches (0.038 cm) ) Thick. In plate c, hole 160 has a diameter of 0.008 inches (0.020 cm), and it is o.ioo inches (0.254 cm) from the center of the plate β and the center hole 162 of the fiber forming the core of the fiber. The elastic wing polymer is supplied to the holes 160 in the plate C and forms the fiber wings through the wing orifices of the plates B and A. The wing and core polymer are 0.328 inches (0.833 cm) above the spinneret A surface ) On top of distribution plate B, and extruded from spinneret A to a fiber with a diameter of 0.080 inches (0.203 cm). Plate c is aligned with plate B so that six holes 160 of plate C are on the wings of plate B Above the center line of the orifice 150. The plate is arranged so that the elastic core polymer supplied to the hole 162 of plate C passes through the center. The invention is illustrated by the following non-limiting examples. The following test method is used. 〇: \ 74 \ 74I52-9I1018.D〇a 4 • 33- ψ binding

線 本紙張尺度適用中國國家標準(CNS) A4規格(210X 297公釐) 580527 A7 B7 五、發明説明(31 ) 試驗方法 於實施例1 · A、B、C、及D中製備得之纖維的伸展性質( 退漿後伸展、退漿後收縮率及退漿後伸展回復)係測定如下 。將5000丹尼值(5550分德士(dtex))之紗束收捲於54英忖 (13 7公分)之捲軸上。環圈紗束之兩側皆包含於總丹尼值内 。測量具有2克重物(長度CB)及具有1〇〇〇克重物(〇·2克/丹 尼值)(長度L B )之起始紗束長度。使紗束於9 5 水中處理 30分鐘(「退漿」),及測量具有2克重物(長度及具 有1000克重物(長度LA起始)之起始(退漿後)長度。於利用 1000克重物測量後,於30秒後(長度CA3G秒)及於2小時後(長 度CA2·!、#)測量具有2克重物之額外的長度。將退漿後收縮率 计算為100 X (LB-LA)/LB。將退漿後伸展百分比計算為1〇〇 X (LA-CA@30秒)/CA@3 0秒。將退漿後回復計算為1〇〇 χ (LA-CA〗小時)/(LA-CA起始)。 在2 0 %及3 5 %有效伸展下之無負荷力之試驗係進行如下 。製備退漿後之具有5000之總丹尼值(555()分德士)之雙組 成纖維紗束。環圈紗束之兩側皆包含於總丹尼值内。在2 i °C及65%相對濕度下使用英斯特朗(Instr〇n)拉伸試驗儀 (Canton,ΜA)。將紗束置於試驗儀的顆夾中,其間有3英忖 (7 6毫米)之間隙。使試驗儀循環通過三個伸展及鬆弛(負荷 及典負荷)循環,各負荷循環具有5〇〇克力(〇 2克每丹尼值) 之最大值,然後測定在第三次無負荷循環的力。對在第三 次無負荷循環之20%及3 5%有效伸展測定有效丹尼值(即在 試驗伸長率下之實際線性密度)。「2〇%及35%有效伸展」 -34- O:\74\74152-9 U018.DOa 4 本紙張尺度適用中國國家標準((:^3) Α4規格(21〇 χ 297公釐) 580527 A7 __________B7 五、發明説明(32 ) ^" — 係指紗束分別自在第三循環之5〇〇克力鬆弛2 〇 %及3 5 %。以 耄克母有效丹尼值(φ克/丹尼值)之單位記錄在2 〇 %及3 5 % 有效伸展下之無負荷力。 經由先將5000丹尼值(5550分德士)之紗束(紗束尺寸包括 生成環圈之兩側)收捲於1.25米之捲軸上,而測定翼自纖維 之芯的脫層。使紗束於熱壓釜中#1〇2t:蒸氣處理3〇分鐘。 自紗束選取2 0公分長度之個別纖維,並將其對摺一半。將 所產生之環圈之開口端的底部縛在一起,及將經縛起的環 圈垂直懸掛於鉤上。將丨克每丹尼值(對25丹尼值之環圈為 50克)之重物附加至環圈之底部(縛起)端。將重物提升至環 圈鬆弛的點,然後輕輕降低,以使環圈伸展及施加完全的 重量。於10個此種循環後,在放大下檢查環圈之脫層並評 定等級。將三樣品評定如下·· 0 =沿纖維沒有可見的翼/芯脫層 1 =於一或多個節點反轉觀察到輕微的脫層 2 =在纖維與其所懸掛之鉤摩擦處觀察到脫層 3 =邊際的脫層(在小環圈中,且僅於少數點) 4 =沿整個纖維之指示脫層的小環圈 5 =大的脫層(沿整個纖維之大環圈) 將二樣品的結果平均。 經由將兩圓重疊於纖維之橫剖面的顯微照片上,以致一 圓(RP與芯聚合物之概略的最外部範圍外接,及另一圓 (R2)與翼聚合物之概略的最内部範圍内切,而測量^及^。 實施例 O:\74\74152-911018.DOO 4 本纸張尺度適用中國國豕標準(CNS) A4規格(210X297公爱) -35- 580527The size of the thread paper is applicable to the Chinese National Standard (CNS) A4 specification (210X 297 mm) 580527 A7 B7 V. Description of the invention (31) The test method is based on the fibers prepared in Example 1 · A, B, C, and D. The elongation properties (extension after desizing, shrinkage after desizing, and extension recovery after desizing) were determined as follows. The 5,000-denier (5550 cent dtex) yarn bundle was wound on a reel of 54 inches (137 cm). Both sides of the loop yarn bundle are included in the total Denny value. The length of the initial yarn bundle having a weight of 2 g (length CB) and a weight of 1,000 g (0.2 g / denier) (length L B) was measured. Treat the yarn bundle in 9 5 water for 30 minutes ("desizing"), and measure the initial (after desizing) length with a weight of 2 grams (length and with 1000 grams of weight (starting from length LA)). After measuring 1000 grams of weight, measure the additional length with a weight of 2 grams after 30 seconds (length CA3G seconds) and after 2 hours (length CA2 · !, #). Calculate the shrinkage after desizing as 100 X (LB-LA) / LB. The extension percentage after desizing was calculated as 100X (LA-CA @ 30 seconds) / CA @ 30 seconds. The post-desizing response was calculated as 100 × (LA-CA 〗 Hours) / (La-CA start). The test of no load at 20% and 35% effective extension was performed as follows. After the desizing, a total denier value of 5000 (555 () points) was prepared. (Taxi) double-component fiber yarn bundle. Both sides of the loop yarn bundle are included in the total denim value. Instron tensile test at 2 i ° C and 65% relative humidity (Canton, MA). The yarn bundle is placed in the tester's clamp with a gap of 3 inches (76 mm). The tester is circulated through three stretching and relaxation (load and nodal load) cycles. Each load cycle There is a maximum value of 500 gram force (0.2 g per denier value), and then the force at the third no-load cycle is measured. It is effective for 20% and 3 5% effective extension measurement at the third no-load cycle Denny value (that is, the actual linear density under the test elongation). "20% and 35% effective stretch" -34- O: \ 74 \ 74152-9 U018.DOa 4 This paper size applies to Chinese national standards (( : ^ 3) Α4 size (21〇χ 297mm) 580527 A7 __________B7 V. Description of the invention (32) ^ " — It means that the yarn bundle will relax by 200% and 35% from 5000 grams of force in the third cycle respectively. %. Record the unloaded force at 20% and 35% effective elongation in units of effective denier value (耄 gram / denier value) of gram mother. By first setting 5000 denier value (5550 cents taxi) The yarn bundle (the size of the yarn bundle includes both sides of the generated loop) is wound on a reel of 1.25 meters, and the delamination of the wing from the core of the fiber is measured. The yarn bundle is placed in an autoclave # 1〇2t: steam treatment 30 minutes. Select individual fibers of 20 cm length from the yarn bundle and fold them in half. Tie the bottoms of the open ends of the loops together, and The tied loop is hung vertically on the hook. Attach a weight of 丨 gram per Denny (50g for a loop of 25 Denny) to the bottom (tied) end of the loop. Lift the weight To the point where the ring is loose, then lower it gently to stretch the ring and apply full weight. After 10 such cycles, check the delamination of the ring under magnification and rate it. Three samples are rated as follows: 0 = no wing / core delamination along the fiber 1 = slight delamination observed at one or more nodes inversion 2 = delamination observed at the friction between the fiber and the hook it hangs from 3 = marginal delamination (In small loops, and only to a few points) 4 = Small loops indicating delamination along the entire fiber 5 = Large delaminations (large loop along the entire fiber) Average the results of the two samples. By superimposing the two circles on the photomicrograph of the cross section of the fiber, one circle (the outermost range of the outline of the RP and the core polymer is circumscribed, and the other circle (R2) and the outline of the winged polymer are inscribed. And measure ^ and ^. Example O: \ 74 \ 74152-911018.DOO 4 This paper size applies to China National Standard (CNS) A4 specification (210X297 public love) -35- 580527

J施例1 各拉伸纖維具有26丹尼值(28·6分德士)之線性密度,且實 %上為徑向對稱。退漿後性質記述於表又。 复盘例1 · A (比車# ) 使用如圖7所說明之裝置及圖8之堆疊板噴絲板組合將锻 組成纖維抽絲。將形成纖維之芯的第一聚合物於2〇引入= 圖7中之抽絲過濾器封裝3〇❶芯聚合物為聚醚酿醯胺 (PEBAXW 3533SN,購自At〇fina),將其體積計量,以產 生佔各纖維之51重量百分比的芯。在圖7之22將熔融的耐 綸共聚物引入至抽絲過濾器封裝3〇。形成六個翼之共聚物 為聚(六亞甲基-共-2-甲基五亞甲己二醯胺),其中六亞甲 基基團係以二胺衍生基團之8〇莫耳百分比存在。並無翼被 芯的顯著穿透,或反之亦然(Ι^/ρ^=1 〇9)。 前凝結噴絲板封裝包括側立面如圖8所示之標示為A至£ 之堆疊板。使用如說明於美國專利第5,168,143號中之方法 ,將0.015英吋(0·038公分)厚之不銹鋼噴絲板a切割出環繞 對稱中心以60。對稱設置之六個翼的孔口。如圖所說^ ,各翼孔口 140為具有通過對稱中心之長軸中心線的平直孔 口’且其具有0.049英吋(0.124公分)之自尖端至半徑之原點 與對稱中心相同之中心圓形噴絲板孔142(直徑〇 〇12英叶 [0.030公分])之圓周的長度。在至噴絲板毛細孔之入口處並 無柱坑。自尖端至0.027英吋(0.069公分)之翼長度144為 0.0042英吋(0.0107公分)寬;其餘之〇·〇22英吋(〇〇56公分) 的長度146為0.0032英吋(0.0081公分)寬。將各翼之尖端於 -36- O:\74\74152-9110I8.DOC\ 4 本紙張尺度適用中國國家標準(CNS) Α4規格(210X297公釐) 580527 A7 _______B7 五、發明説明(34 ) 尖端之一半寬度處圓弧切割。將0.015英吋(0.038公分)厚度 之分佈板B(圖8B)與噴絲板A(圖8A)對齊,以致其之分佈孔 口與噴絲板A中之噴絲板孔口相配合。板b之六翼孔口 150 為0.094英吋(0.239公分)長及0.020英吋(0.051公分)寬,及 將其之翼尖端弄圓成其之一半寬度的半徑。如圖8B所說明 ,分佈板B之六翼孔口 150各變尖細至圓形(0.006英吋(〇.〇 15 公分)直徑)開口端,然後再以〇.〇13英吋(0.033公分)長度及 0.0018英吋(0.0046公分)長度之狹縫154延續至中心孔156。 此板中之中心孔156的直徑為0.0125英吋(0.032公分)。狹缝 154連接中心孔與各翼分佈孔口之末端。計量板c為〇.〇1〇英 吋(0.025公分)厚度(見圖8 C)。各計量孔係正中位於分佈板 B中之翼長軸中心線之上方或對稱中心之上方。中心計量孔 162及各翼160之一孔為0·010英忖(0025公分)直徑;孔160 之中心距孔162之中心0.120英吋(0.305公分)。對中心計量 孔供應來自習知之熔體池板D (見圖7 ),及形成最終纖維中 之芯元件之經過濾的熔融彈性聚合物。對板C之外部的六個 計量孔160供應來自熔體池板D,成為聚合物翼之非彈性聚 合物。噴絲板支承板Ε(再次見圖8)中之大孔(典型上為 0.1875英吋(0.4763公分)直徑)係與噴絲板a中之喷絲板孔 口對齊,並張開4 5。。噴絲板A、分佈板b、及計量板c被 熔體池板D·及噴絲板支承板E夾住;如圖8所示。典型上, 板£為0.2-0.5英吋(0.4-1.3公分)厚,及板1)為〇〇2_〇.〇3英 吋(0.05-0.08公分)厚。 因此,在喷絲板A中並無柱坑,且板a、B、及c之結合 O:\74\74152-911018.DOC\ 4 ' 37 - 本纸張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐)~ 580527 A7 B7 五、發明説明(35 厚度僅為約0.040英叶(0·102公分)。翼及芯聚合物先於分佈 板Β之正上方彼此接觸,以致其在形成纖維前之約公 分(0.038公分分佈板+ 0.038公分噴絲板)彼此前凝結。 利用空氣50之流動,使新抽絲的纖維4〇(見圖7)冷卻,以 使其固化,及於6 0塗布5重量百分比(以纖維重量計)之包括 石夕酮油及金屬硬脂酸鹽之處理劑。使纖維前進至在進給輥 8 0與牽引輥9 0之間的拉伸區,對各輥纏繞數圈。對於4 · 〇 之牽伸比,牽引輥90之速度為進給輥80之四倍(後者為每分 鐘3 5 0米)。然後於室11 〇中以6镑每平方英吋(〇 8 7仟帕斯卡 )之蒸氣處理長絲;以較牽·引輥對9 〇之速度低2 〇 %的速度操 作收捲機13 0,以使纖維部分(2 〇 %)鬆弛,而降低最終纖維 中之收縮率。將經拉伸及部分鬆弛之纖維丨2〇收捲於收捲機 130 ’且其具有26丹尼值(29分德士)之線性密度。 t施例1 ·ΒΓ比鲂、 貝貝上如同貫施例1.Α ’將具有六個聚(六亞甲基-共 甲基五亞甲己二醯胺)之翼(其中六亞甲基基團係以8〇莫耳 百分比存在)及PEBAXTM 3 533SN之芯的纖維抽絲,除了將5 重量百分比(以總翼聚合物重量計)之耐綸i 2 [聚(丨2 -十二内 酿胺),「N12」](購自Atofina之Rilsan® ΑΜΝΟ)加至翼聚 合物,以促進翼對芯的内聚作用。翼/芯重量比為48/5 2 , 及 Ri/R2 為 1.05。 實_施例1 . C Γ發明) 實質上如同實施例1 · A製備具有六個聚(六亞甲基-共-2 _ 甲基五亞曱己二醯胺)(20莫耳百分比之2 -甲基五亞甲基基 O:\74\74152-911018.DOQ 4 本紙張尺度適用中國國家標準(CNS) A4規格(210X 297公釐) -38-J Example 1 Each drawn fiber has a linear density of 26 deniers (28.6 decitex), and is substantially symmetrical in radial direction. The properties after desizing are described in the table. Rewinding example 1 · A (比 车 #) The device as illustrated in FIG. 7 and the stacked plate spinneret of FIG. 8 were used to spin the forged fibers. The first polymer that forms the core of the fiber is introduced at 20 = the spin filter package in Figure 7 is used. The core polymer is polyetheramine (PEBAXW 3533SN, purchased from Atomofina), and its volume is Measure to produce a 51 weight percent core for each fiber. The molten nylon copolymer is introduced into the spin-on filter package 30 at 22 of Figs. The copolymer forming the six wings is poly (hexamethylene-co-2-methylpentamethylenehexamethylene diamine), in which the hexamethylene group is 80 mole% of the diamine-derived group presence. No wings were significantly penetrated by the core, or vice versa (Ι ^ / ρ ^ = 1〇9). The front-condensation spinneret package includes stacked boards with side elevations, labeled A to £, as shown in Figure 8. Using the method described in U.S. Patent No. 5,168,143, a 0.015 inch (0.038 cm) thick stainless steel spinneret a was cut out around the center of symmetry to 60. The six wing orifices are arranged symmetrically. As shown in the figure ^, each wing orifice 140 is a straight orifice having a long axis centerline passing through the center of symmetry 'and has an origin of 0.049 inches (0.124 cm) from the tip to the radius the same as the center of symmetry The length of the circumference of the center circular spinneret hole 142 (the diameter is 012 inches [0.030 cm]). There are no pillar pits at the entrance to the capillary holes of the spinneret. The wing length 144 from the tip to 0.027 inches (0.069 cm) is 0.0042 inches (0.0107 cm) wide; the remaining 0.022 inches (0.056 cm) length 146 is 0.0032 inches (0.0081 cm) wide . Put the tip of each wing at -36- O: \ 74 \ 74152-9110I8.DOC \ 4 This paper size applies to Chinese National Standard (CNS) A4 specification (210X297 mm) 580527 A7 _______ B7 V. Description of the tip (34) Arc cut at half width. Align the distribution plate B (Fig. 8B) with the spinneret A (Fig. 8A) with a thickness of 0.015 inches (0.038 cm) so that the distribution orifices match the orifices in the spinneret A. The six-wing orifice 150 of plate b is 0.094 inches (0.239 cm) long and 0.020 inches (0.051 cm) wide, and the radius of its wing tips is rounded to one and a half widths. As illustrated in FIG. 8B, each of the six-wing apertures 150 of the distribution plate B is tapered to a round (0.006 inch (0.015 cm) diameter) open end, and then 0.013 inches (0.033 cm) ) Length and 0.0018 inch (0.0046 cm) length of slit 154 continues to the center hole 156. The center hole 156 in this plate has a diameter of 0.0125 inches (0.032 cm). The slit 154 connects the central hole and the end of each wing distribution opening. The metering plate c is 0.010 inches (0.025 cm) thick (see Figure 8C). Each measuring hole is located above the centerline of the long axis of the wing in the distribution plate B or above the center of symmetry. The central metering hole 162 and one of the holes of each wing 160 have a diameter of 0.010 inches (0025 cm); the center of the hole 160 is 0.120 inches (0.305 cm) from the center of the hole 162. The center metering hole is supplied from a conventional melt cell plate D (see Fig. 7) and a filtered molten elastic polymer forming a core element in the final fiber. Six metering holes 160 to the outside of plate C are supplied from the melt pool plate D, which becomes a non-elastic polymer of polymer wings. The large holes (typically 0.1875 inches (0.4763 cm) in diameter) in the spinneret support plate E (see Figure 8 again) are aligned with the spinneret orifices in spinneret a and open 4 5. . The spinneret A, distribution plate b, and metering plate c are sandwiched by the melt pool plate D · and the spinneret support plate E; as shown in FIG. 8. Typically, the plate is 0.2-0.5 inches (0.4-1.3 cm) thick, and the plate 1) is 0.02-0.03 inches (0.05-0.08 cm) thick. Therefore, there are no pillar pits in the spinneret A, and the combination of the plates a, B, and c is O: \ 74 \ 74152-911018.DOC \ 4 '37-This paper size applies to the Chinese National Standard (CNS) A4 Specifications (210 X 297 mm) ~ 580527 A7 B7 V. Description of the invention (35 thickness is only about 0.040 inches (0 · 102 cm). The wing and core polymer contact each other directly above the distribution plate B, so that Approximately centimeters before forming the fibers (0.038 cm distribution plate + 0.038 cm spinneret) are condensed before each other. Using the flow of air 50, the newly drawn fiber 40 (see Fig. 7) is cooled to solidify, and Apply 5 weight percent (based on the weight of the fiber) of the treatment agent including lithone oil and metal stearate at 60. The fiber is advanced to the drawing zone between the feed roller 80 and the pull roller 90. Wrap each roll several times. For a draft ratio of 4.0 °, the speed of the traction roll 90 is four times the speed of the feed roll 80 (the latter is 350 meters per minute). Then in the room 11 〇 for 6 pounds Steam treated filaments per square inch (0,87 Pascals); operating the winder 130 at a speed that is 20% lower than the speed of the draw-and-roller pair 90, In order to relax the fiber part (20%) and reduce the shrinkage rate in the final fiber. The drawn and partially relaxed fiber is wound up in a winder 130 'and has a 26 denier value (29 points) Tex) linear density. Example 1 · ΒΓ is higher than 鲂, as in Example 1.A 'on the babe will have six poly (hexamethylene-co-methylpentamethylene hexamethylene diamine) Wings (where hexamethylene groups are present at 80 mole percent) and fiber spinning of the core of PEBAXTM 3 533SN, except for 5 weight percent (based on total wing polymer weight) of nylon i 2 [poly (丨 2-Dodecalactam), "N12"] (Rilsan® AMINO purchased from Atofina) is added to the wing polymer to promote the cohesion of the wing to the core. The wing / core weight ratio is 48/5 2 , And Ri / R2 is 1.05. Example _ Example 1. C Γ invention) is substantially the same as in Example 1 · A prepared with six poly (hexamethylene-co-2 -methylpentamethylenehexamethylene diamine) ) (20 mol% 2-methylpentamethylene O: \ 74 \ 74152-911018.DOQ 4 This paper size applies to China National Standard (CNS) A4 (210X 297 mm) -38-

裝 訂Binding

580527 A7 B7 五、發明説明(36 ) 團,以二胺衍生基團計)之翼及PEBAXTM 3533SN芯(繞曲模 數2800 psi( 19,300仟帕斯卡))之纖維,除了計量板C具有另 一組孔164(如圖8C所示),各翼之一孔位在翼之中心線上, 各孔之直徑為0.005英吋(0.013公分),且距孔之對稱中心 0.0475英吋(0· 12 1公分)。對此等額外的孔及中心孔供給來 自共同熔體池之熔融聚合物,而形成芯及翼中的突出芯元 件。結果,有翼被芯聚合物的穿透(Ri/Rf 1 .6,由以類似 方式製備得之纖維的比估計),而將翼更佳地黏著至芯。纖 維橫剖面實質上如圖2所說明。 實施例1 . D (發明) 實質上如同實施例1 · C將纖維抽絲,但在翼中有5重量百 分比之耐綸1 2[聚(十二内醯胺)](Rilsan® ΑΜΝΟ)内聚添加 劑。纖維具有被芯聚合物穿透之翼部分(I^/Rfl .5),而 將翼更佳地黏著至芯。纖維橫剖面實質上如圖2所說明。 表1580527 A7 B7 V. Description of the invention (36) group, based on diamine-derived group) wings and PEBAXTM 3533SN core (2800 psi (19,300 仟 Pascal) modulus), except metering plate C has another group Hole 164 (as shown in Figure 8C), one of the wings is located on the centerline of the wing, the diameter of each hole is 0.005 inches (0.013 cm), and 0.0475 inches (0.112 cm) from the center of symmetry of the hole ). These additional holes and center holes are supplied with molten polymer from a common melt pool to form core and protruding core elements in the wings. As a result, the wings were penetrated by the core polymer (Ri / Rf 1.6, estimated from the ratio of fibers prepared in a similar manner), and the wings were better adhered to the core. The fiber cross section is substantially as illustrated in FIG. 2. Example 1. D (Invention) The fiber is essentially the same as in Example 1. · C, but there is 5 weight percent of nylon 1 2 [poly (dodecylamine)] (Rilsan® ΑΝΝ) in the wings Poly additives. The fiber has wing portions (I ^ / Rfl.5) penetrated by the core polymer, and the wings are better adhered to the core. The fiber cross section is substantially as illustrated in FIG. 2. Table 1

實施例1.A (比較) 實施例1.B (比較) 實施例l.C (發明) 實施例l.D (發明) Ri/R2 1.1 1.1 1.6 1.5 翼聚合物 6/MPMD 6/MPMD 6/MPMD 6/MPMD (80/20)-6 (80/20)-6+ 5wt% N12 (80/20)-6 (80/20)-6+ 5wt% N12 芯聚合物 PEBAX™ PEBAX™ PEBAX™ PEBAX™ 3533SN 3533SN 3533SN 3533SN 〇;\74\74l52-911018.D〇a 4 " 39 本纸银尺度適用中國國家標準(CNS) A4規格(210X297公釐) A7Example 1.A (comparative) Example 1.B (comparative) Example 1C (invention) Example 1D (invention) Ri / R2 1.1 1.1 1.6 1.5 Wing polymer 6 / MPMD 6 / MPMD 6 / MPMD 6 / MPMD (80/20) -6 (80/20) -6+ 5wt% N12 (80/20) -6 (80/20) -6+ 5wt% N12 core polymer PEBAX ™ PEBAX ™ PEBAX ™ PEBAX ™ 3533SN 3533SN 3533SN 3533SN 〇; \ 74 \ 74l52-911018.D〇a 4 " 39 The silver standard of this paper applies the Chinese National Standard (CNS) A4 specification (210X297 mm) A7

沸水處理後之可 苎復伸展%Elongation after boiling water treatment%

此等數據顯示纖維對於針織品及服裝應用非常良好。脫 層數據_ τπ有翼黏著至芯之纖維的優良性能。本發明之纖 維可具有低於約1 · 〇之脫層評比。此外,數據顯示在翼聚合 物中使用黏著添加劑諸如Nl2有利。 秀漿後收縮率% 脫層評比These data show that fibers are very good for knitwear and apparel applications. Delamination data_ τπ Excellent performance of fibers with wings attached to the core. The fibers of the present invention may have a delamination rating below about 1.0. In addition, the data show that the use of adhesion additives such as Nl2 in wing polymers is advantageous. Post-shrinkage shrinkage% delamination evaluation

免施例2 · A 貫質上如同實施例1D將本發明之三長絲雙組成紗抽絲, 但有以下足差異。各板具有五個以分開72。對稱設置之供翼 聚合物用之孔,以致各纖維具有五個翼。五個翼中之聚合 物為具有5重量百分比耐綸丨2添加劑之9 5重量百分比聚己 内醯胺(3.14以,慣例上係由1:|111>〇1^(1〇以“11所製備,及 自其所購得)。如表2· A所示改變翼/芯比。處理劑為椰子油 、第四胺、水、及非離子表面活性劑之混合物,其係以纖 維計2重量百分比塗布。進給輥速度為每分鐘42〇米,及使 拉伸纖維在捲起之前受到丨5 %的鬆弛。橫剖面實質上係如 圖2所示,為約i ·4 ,及拉伸纖維為23丹尼值(2 5分德 士)。 如前於退漿處理後測定不同翼芯比之紗的可回復伸展百 分比。 O:\74\74152-911018.D〇a 4 - 40 - 本紙張尺度適用中國國家標準(CNS) A4規格(210X297公釐) 五、發明説明(38Exemption Example 2 · A The three-filament bi-component yarn of the present invention is drawn in the same manner as in Example 1D, but with the following differences. Each plate has five to separate 72. The holes for the wing polymers are arranged symmetrically so that each fiber has five wings. The polymer in the five wings is 5 weight percent of nylon, 2 and 9 weight percent of polycaprolactam (3.14 to, conventionally, it is composed of 1: | 111 > 〇1 ^ (1〇 to "11 (Prepared and purchased from it). Change the wing / core ratio as shown in Table 2.A. The treatment agent is a mixture of coconut oil, fourth amine, water, and non-ionic surfactants, based on fiber 2 Coating by weight percentage. Feed roller speed is 4200 meters per minute, and the drawn fiber is subject to 5% relaxation before being rolled up. The cross section is substantially as shown in FIG. The elongation fiber is 23 denier (25 decitex). As before, the recoverable elongation percentage of yarns with different wing-to-core ratios is determined after desizing. O: \ 74 \ 74152-911018.D〇a 4-40 -This paper size applies to China National Standard (CNS) A4 specification (210X297 mm) V. Description of invention (38

-表 2 . A-Table 2. A

:2.A中之結果顯示當在實施例之纖維中翼,芯重量比低 ^ , 同的退漿後伸展,當未對本發明乏鏞 、,隹使用伴纖維時其為較佳。當對 4 以提高結合紗中之回復力時丄發月'誠維使用伴纖維 A 寺,再更低的翼/芯比通常為較佳 (例如約20/80至約4〇/6〇)。 仅住The results in: 2.A show that when the core weight of the fiber in the embodiment is low, the core weight ratio is the same, and it is stretched after desizing. It is better when the companion fiber is not used for the present invention. When paired with 4 to increase the recovery force in the bonded yarn, "Bai Fayue" uses the companion fiber A Temple, and a lower wing / core ratio is usually better (for example, about 20/80 to about 4/6/6) . Live only

t施例2.R 評估針織品耐用性、透明性及伸展成翼之總線性密度(丹 ί值1分德士)之函數。將實施例2.A之纖維針織成為針織 二°使用其他的纖維。改變纖維之總丹尼值及翼對芯體 男比 组砰疋人員主觀地評定針織品之a )以穿帶壽命為 基準的耐用性’ b)透明性美觀(相對於由經覆蓋5纖維之了丹 尼值(8分德士)耐輪6_6之i〇丹尼值乙似,彈性纖維以類 〇:\74\74Ι52-9ΐΙ〇ΐ8.〇〇α 4tExample 2.R As a function of the durability, transparency, and bus density of a wing that stretches into a wing (Dan value 1 cent taxi). The fiber of Example 2.A was knitted to a knit of 2 °, and other fibers were used. Change the total denier value of the fiber and the wing-to-core man-to-man ratio. The knitting staff subjectively evaluates a) the durability based on the belt wearing life 'b) the transparency and beauty (compared with In the case of the Denny value (8 points taxi), the i-6 value of the resistance wheel 6_6 is similar to that of the elastic fiber, and the elastic fiber is classified as 0: \ 74 \ 74Ι52-9ΐΙ〇ΐ8.〇〇α 4

似方式針織彳于之針織品的參考標準),及c)退漿後伸展百分 比西如耐用性超過7天則將其評定為合格;如透明性等於參 考栝準則將其評定為合格;及如伸展百分比係在4 0及i 2 0 % g且可防止鬆弛(bagginess)及針織品之「鬆垮(ride- down) 」’ 則將 其評定 為合袼 。 表 2 』 中之 打星號 ⑺及黑 體的數字係指示以三評定面積為基準,在定性上較佳之分 德士及翼對芯比。表之主體中之係各纖維之翼之分德士的 總和。 翼/芯 重量比 翼/芯 重量比 衣 翼/芯 重量比 翼/芯 重量比 翼/芯 重量比 翼/芯 重量比 總分德士 35/65 40/60 45/55 50/50 55/45 60/40 17 5.8 6.7 7.5 8.3 U ί M w/ 9.2 10.0 22 7.8 8,9 10.0 11.0* 12 2 13 3 28 9.7 11* 12.5* 13.9* 15.3 16 6 33 11.7* 13.3* 15.0* 16.6* 18.3 20.0 當總分德士增加至高於約3 3時,針織品之透明性降低。 當總分德士降至低於約22,及翼分德士總和降至低於約n 時’耐用性開始受害。當翼/芯重量比上升至高於約5〇/5〇 時,伸展百分比開始降低(如早先於實施例2A所示)。 由此試驗之結果,推論本發明之較佳的雙組成纖維可具 有在約2 2至3 3分德士之範圍内之總線性密度,至少約丨丨之 -42- O:\74\74152-911018.DOO 4 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公爱7 580527 A7 ____B7 ΪΓ、發明説明(40 ) ' "~" ~' 翼部分分德士總和,及在3 5 / 6 5及5 0 / 5 0之間之翼對芯重量 比。The reference standard for knitwear knitted in a similar manner), and c) the percentage of elongation after desizing. If the durability is more than 7 days, it is evaluated as qualified; if the transparency is equal to the reference standard, it is evaluated as qualified; and if The elongation percentage is between 40 and i 2 0% g, which can prevent bagginess and "ride-down" of knitted fabrics, which are evaluated as combined. The numbers in asterisk ⑺ and black body in Table 2 indicate that the three assessment areas are used as the basis, and the qualitatively better points are taxi and wing-to-core ratio. The body of the table is the sum of the taxis of each fiber wing. Wing / Core Weight Ratio Wing / Core Weight Ratio Clothing Wing / Core Weight Ratio Wing / Core Weight Ratio Wing / Core Weight Ratio Wing / Core Weight Ratio Total Taxi 35/65 40/60 45/55 50/50 55/45 60/40 17 5.8 6.7 7.5 8.3 U ί M w / 9.2 10.0 22 7.8 8,9 10.0 11.0 * 12 2 13 3 28 9.7 11 * 12.5 * 13.9 * 15.3 16 6 33 11.7 * 13.3 * 15.0 * 16.6 * 18.3 20.0 When it is higher than about 3, the transparency of the knitted fabric is reduced. When the total taxis drop below about 22 and the total wing taxis drop below about n, the durability begins to suffer. As the wing / core weight ratio rises above about 50/50, the percent stretch begins to decrease (as shown earlier in Example 2A). From the results of this test, it is inferred that the preferred bicomponent fiber of the present invention may have a bus density in the range of about 22 to 33 cents taxis, at least about -42- O: \ 74 \ 74152 -911018.DOO 4 This paper size is in accordance with Chinese National Standard (CNS) A4 specification (210 X 297 Public Love 7 580527 A7 ____B7 发明 Γ, Invention Description (40) '" ~ " ~' Wing portion is divided into taxis, and Wing to core weight ratio between 3 5/65 and 50/50.

實施例3 A 貫夤上如同實施例2 A之說明將本發明之雙組成纖維抽絲 ,除了塗布4重量百分比(以纖維之重量計)之聚矽氧烷基處 理劑(如說明於美國專利第4,999,120號)替代實施例2A之處 理劑’纖維在捲起之前鬆弛2 〇 %,且在鬆弛步驟中所使用 之蒸氣為3psi(20.7仟帕斯卡)。翼/芯/突出芯重量比為 3 8/5 3/9,及!^/!^為約L4。圖5係纖維之橫剖面顯微照片 ,此纖維為32丹尼值(36分德士,剛拉伸),且具有ι〇8% 之退水後伸展,2 4 %之退漿後收縮率,及9 2 %之退漿後回 復。 實施例3 . ft 於典型上對每程機械雙重覆蓋彈性纖維腿構造所設置之 商業機器上,由實施例3·Α之纖維將針織品胚料針織。機器 為MATEC HSE 4.5,其在大腿區域以约7〇〇 RpM針織,及 在腳踝以800 RPM針織,及設定為尺寸?。於約2分鐘内針 織一個腿胚料。將腿紗以硬紗之正常方式供給至機器;未 使用電子張力器。利用滾轉蒸氣加熱在大氣壓力下將原胚 布襪胚料處理30分鐘❶然後使用標準的工業自動熱壓釜捲 板設備將衣物在1〇2它下捲板4秒,隨後再在95χ:下乾燥3〇 秒。將捲板用的織物長度選擇成儘可能地小,同時將織物 維持於無敏狀態。使用標準的酸性染料將衣物在98。〇下染 色45分鐘,及使用相同尺寸的板及條件後捲板。 O:\74\74I52-911018.DOa 4 _____ -43- 紙張尺錢财0 S家標準—Example 3 A As described in Example 2 A, the bi-component fiber of the present invention is drawn, except that 4 weight percent (based on the weight of the fiber) of the polysiloxane treatment agent is applied (as described in the US patent). No. 4,999,120) The treatment agent of Example 2A, the fiber was relaxed by 20% before being rolled up, and the steam used in the relaxation step was 3 psi (20.7 仟 Pascal). The wing / core / protruding core weight ratio is 3 8/5 3/9, and! ^ /! ^ Is about L4. Figure 5 is a cross-section photomicrograph of a fiber. The fiber has a value of 32 denier (36 cents taxi, just stretched), and has a stretch of 8% after dehydration and a shrinkage of 24% after desizing. , And 92% of the return after desizing. Example 3. ft. On a commercial machine typically provided with a double-stranded elastic fiber leg structure for each mechanical pass, the knitted fabric blank was knitted from the fibers of Example 3.A. The machine is MATEC HSE 4.5, which is knitted at approximately 700 RpM in the thigh area, and 800 RPM in the ankle, and set to size? . Needle-knit a leg stock in about 2 minutes. The leg yarn was supplied to the machine in the normal way of hard yarn; no electronic tensioner was used. Tumble steam heating was used to treat the original sock stock material under atmospheric pressure for 30 minutes. Then, the standard industrial automatic autoclave coiling equipment was used to roll the fabric under the 102 for 4 seconds, and then at 95χ: Dry for 30 seconds. The length of the fabric for the roll sheet is selected to be as small as possible while maintaining the fabric in a non-sensitized state. Use standard acid dyes to keep the clothes at 98. The dyeing was carried out for 45 minutes, and the plate was rolled after using the same size plate and conditions. O: \ 74 \ 74I52-911018.DOa 4 _____ -43- Paper rule money 0 S home standard —

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線 580527 A7 ____ B7 五、發明説明(41 ) 生成之織物具有3.38X10 “瓦/公分之意料之外的高導 熱性。 使用如圖7所描述之纟置1用聚酉旨翼及聚醚酉旨芯製備根 據本發明之三長絲雙組成紗。纖維4 A之芯聚合物為 HYTREL@ 3078聚醚醋彈性體(杜邦公司之註冊商標;撓曲 模數4000 pSi(27,600仟帕斯卡))。實施例4 β及實施例斗c 之纖維的芯聚合物為實質上如美國專利第4,9〇6,721號之說 明製備得之具有聚(四亞甲基-共_2•甲基四亞甲醚)二元醇 軟片段及對酞酸丁二酯(4 G · 丁)硬片段之聚醚酯彈性體。加 入至共聚醚二兀醇中之3 -曱基四氫呋喃之量為9莫耳百分比 ,一元醇數目平均分子量為2750,及4G-T對共聚醚二元醇 之莫耳比為4.6:1。在表4,將此聚合物指示為r2MeP()4G :4G-T」。在實施例4A及4B之纖維中之翼聚合物為聚(對 酞酸丁二酯)(4G-T,Crastin® 6129;杜邦公司之註冊商標 ,撓曲模數350,〇〇〇 psi(2.4百萬仟帕斯卡)),及於纖維4c 中’其為聚(對酞酸丙二酯。3G_T係於雙容器方法 中’使用以聚合物計為6〇 ppm之鈦酸四異丙酯催化劑, Tyzor® TPT(杜邦公司之註冊商標),由丨,、丙二醇及對酞 酸二甲醋製備得。在轉酯化容器中在185艺下將熔融Dmt加 至3(3及催化劑,及將溫度提高至210°C,同時將甲醇移除 。將生成之中間體移至聚縮合容器,在此將壓力降至1亳巴 (10·2公斤/平方公分),及將溫度提高至255°C。當達到期望 的’溶體黏度時,將壓力提高,及將聚合物擠製、冷卻、及 O:\74\74152.911018.DOO 4 本纸張尺度適财®®X 297公釐) 580527 A7 B7 五、發明説明(42 ) 切割成粒料。使粒料於固態在於212 °C下操作之滾筒乾燥機 中進一步聚合至1.04分升/克(dl/g)之固有黏度。此實施例 之噴絲板封裝及各纖維的抽絲條件實質上與實施例2 A相同 ,除了在翼中沒有聚合物添加劑,翼為總纖維之4 0重量百 分比,塗布4重量百分比(以纖維計)之說明於實施例3 A之 處理劑,及在藉由3磅每平方英吋壓力(20.7仟帕斯卡)之蒸 氣捲起之前,使纖維鬆弛20%。纖維具有記述於表4之性質 表4 實施例4A 實施例4B 實施例4C 丹尼值(dtex) 25(27.5 dtex) 24(26 dtex) 27(30 dtex) 翼聚合物 4G-T 4G-T 3G-T 芯聚合物 HYTREL™ 2MeP04G:4G-T 2MeP04G:4G-T 3078 Ri/R2 1.6 1.6 1.6 沸水處理後之可 60 100 76 回復伸展% 退漿後收縮率% 10 12 12 退漿後回復% 85 94 89 無負荷力@20% 有效伸展 15 18 17 無負荷力@35% 3 5 1 有效伸展Wire 580527 A7 ____ B7 V. Description of the invention (41) The resulting fabric has an unexpectedly high thermal conductivity of 3.38X10 "Watts / cm. Use the poly-purpose wing and polyether as shown in Figure 7 The purpose is to prepare a three-filament bicomponent yarn according to the present invention. The core polymer of fiber 4 A is HYTREL @ 3078 polyether vinegar elastomer (registered trademark of DuPont; flexural modulus 4000 pSi (27,600 仟 pascal)). The core polymer of the fibers of Example 4 β and Example c is substantially poly (tetramethylene-co_2methyltetramethylene) prepared as described in US Pat. No. 4,906,721. Ether) Polyether ester elastomers with soft segments of diols and hard segments of butyl phthalate (4 G · butyl). The amount of 3-fluorenyltetrahydrofuran added to the copolyether diol is 9 mole percent The average molecular weight of the number of monohydric alcohols is 2750, and the molar ratio of 4G-T to copolyether glycol is 4.6: 1. In Table 4, this polymer is indicated as r2MeP () 4G: 4G-T ". The wing polymer in the fibers of Examples 4A and 4B was poly (butylene terephthalate) (4G-T, Crastin® 6129; a registered trademark of DuPont, with a flexural modulus of 350,000 psi (2.4 Millions of Pascals)), and in fiber 4c 'It is poly (propylene terephthalate. 3G_T in a two-container method' uses 60 ppm of tetraisopropyl titanate catalyst based on polymer, Tyzor® TPT (registered trademark of DuPont), prepared from Benzene, propylene glycol, and dimethyl terephthalate. In a transesterification vessel, the molten Dmt is added to 3 (3 and the catalyst, and the temperature is increased). Raise to 210 ° C while removing methanol. Move the resulting intermediate to a polycondensation vessel, reduce the pressure to 1 bar (10.2 kg / cm²), and increase the temperature to 255 ° C. When the desired 'solution viscosity is reached, increase the pressure, and extrude, cool, and polymer: O: \ 74 \ 74152.911018.DOO 4 This paper is suitable for standard paper ® X 297 mm) 580527 A7 B7 V. Description of the invention (42) Cutting into pellets. The pellets are further polymerized in a drum dryer operating at 212 ° C in a solid state to Intrinsic viscosity of 1.04 dL / g (dl / g). The spinneret packaging and fiber drawing conditions of this embodiment are substantially the same as those of Example 2 A, except that there is no polymer additive in the wing, and the wing is the total 40% by weight of fiber, coated with 4% by weight (in terms of fiber) as described in Example 3A, and before being rolled up by steam at a pressure of 3 pounds per square inch (20.7 仟 Pascal), The fiber is 20% slack. The fibers have the properties described in Table 4. Table 4 Example 4A Example 4B Example 4C Denier (dtex) 25 (27.5 dtex) 24 (26 dtex) 27 (30 dtex) Wing polymer 4G- T 4G-T 3G-T core polymer HYTREL ™ 2MeP04G: 4G-T 2MeP04G: 4G-T 3078 Ri / R2 1.6 1.6 1.6 After boiling water treatment 60 100 76 Recovery elongation% Shrinkage after desizing% 10 12 12 Back Recovery after pulping 85 94 89 No load @ 20% effective stretch 15 18 17 No load @ 35% 3 5 1 Effective stretch

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線 O:\74\74152-911018.DOa 4 -45 本纸張尺度適用中國國家標準(CNS) A4規格(210X297公釐) 580527 A7 B7 五、發明説明( 43 實施例4B之纖維的脫層評比為〇 · 〇。由實施例4 A、4B及 4C之纖維針織得之純粹針織品胚料於蒸氣捲板、染色、及 處理之後具有均勻的外觀及良好的伸展及回復。 實施例5 . A 使用圖7之裝置及實施例3 A之噴絲板封裝及抽絲條件,利 用實施例1D之聚合物及處理劑,將根據本發明之雙組成纖 維抽絲,除了使用以纖維之重量計為13重量百分比的處理 劑。翼及芯聚合物先於抽絲成為纖維之前的約〇.〇76公分彼 此接觸。 心牙透翼,以致翼/芯/突出芯重量比為39/51/10 (r〗/r2 為約1·5)。纖維具有20丹尼值(22分德士)之線性密度, 1〇〇%之退漿後伸展百分比,23%之退漿後收縮率,及94% 之退漿後回復。 實施例5 . Β 將實施例5.Α之纖維的四個經紗噴氣摻和,而形成雙組成 紗。在SULZER RUTI 5100(噴氣織機)上,使用每公分3 8紗 (96緯數/英吋)之噴氣摻和雙組成紗作為緯,及每公分48經 紗(12 1每英吋)之44丹尼值“容分德士”“長絲丁^巧!^ (杜邦公司之註冊商標)6342型耐綸作為經,以3/1構造編織 織物。經由在115°C下蒸氣鬆弛,在7(TCtM(:f噴射煮煉, 使用耐論之標準的酸性染料在⑺代下MCF噴射染色6〇分鐘 ,及在190 C下熱定型30秒,而將編織織物處理。此等織物 不蓬鬆且光滑,當風乾時無皺褶,且其顯現良好的伸展及 回復及優異的硬纖維手感及視覺美觀性。經鬆弛的完成編 O:\74\74152-911018.DOO 4 -46· ^纸張尺度適用中國國家標準(CNS) Α4^^1〇 χ 2的公釐)-----Line O: \ 74 \ 74152-911018.DOa 4 -45 This paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) 580527 A7 B7 V. Description of the invention (43 Delamination evaluation of fiber of Example 4B 〇. 〇. Pure knitted fabric blanks knitted from the fibers of Examples 4 A, 4B and 4C have uniform appearance and good stretch and recovery after steam coiling, dyeing, and treatment. Example 5. A Using the device of FIG. 7 and the spinneret packaging and spinning conditions of Example 3 A, the polymer and processing agent of Example 1D were used to spin the bicomponent fiber according to the present invention, except that the fiber weight was used as 13% by weight of the treatment agent. The wings and the core polymer contact each other about 0.076 cm before spinning into fibers. The teeth penetrate the wings so that the weight ratio of wings / cores / protruding cores is 39/51/10 ( r〗 / r2 is about 1.5). The fiber has a linear density of 20 denier (22 cents taxi), 100% elongation after desizing, 23% shrinking after desizing, and 94% Example 5. Β The four warp yarns of the fiber of Example 5.A were air-blended and shaped. Double-component yarn. On SULZER RUTI 5100 (air-jet loom), air-jet blended double-component yarn with 38 yarns per cm (96 wefts / inch) is used as weft, and 48 warp yarns per cm (12 1 per inch) 44 Denny value "Rong Fen Tex" "Filament ^ Qiao! ^ (Registered trademark of DuPont) 6342 nylon as a warp, woven fabric with 3/1 structure. After steam relaxation at 115 ° C, Woven fabrics were treated by spraying at 7 ° C tM (: f, using a standard acid dye of MCF for 60 minutes under generation, and heat setting at 190 C for 30 seconds. These fabrics were not treated with Fluffy and smooth, no wrinkles when air-dried, and it shows good stretch and recovery, excellent hard fiber feel and visual aesthetics. Finished by relaxation O: \ 74 \ 74152-911018.DOO 4 -46 · ^ Paper size applies Chinese National Standard (CNS) (A4 ^^ 1〇χ 2 mm) -----

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580527 A7 B7 五、發明説明(44 ) 織織物具有以下之性質: 基重量=3.29盎司/平方碼(112克/平方米) 厚度= 0.079英吋(2毫米) 緯數= 160 /英忖(63 /公分) 經數= 208/每英吋(82/公分) 5公分寬度X 10公分長度之織物可由手伸展40%,之後其 回復多於9 5 %。 實施例6 此實施例說明使用全厚度的喷絲板於製造本發明之纖維 。使用與實施例1 C相同之前凝結喷絲板封裝,除了以具有 與噴絲板A (圖8 A)中之孔口相同形態、尺寸、軸向對齊、 及徑向方向之噴絲板毛細孔(0.015英吋(〇·〇3 8公分)長度)及 0.1406英叶(0.357公分)直徑圓柱坑之0.3125英忖(0.794公分 )厚度之噴絲板(圖11A)取代支承板E。翼及芯聚合物先於形 成纖維之前的約0.87公分(0.794公分噴絲板+ 0.038公分板 A+0.03 8公分板B)彼此接觸。使用圖7之裝置,利用4X牵伸 比,將具有六個聚(六亞曱基-共-2-甲基五亞甲己二醯胺) 之翼(其中六亞甲基基團係以二胺衍生基團之8〇莫耳百分比 存在)(以名知方式製備得’相對黏度90)及PEB AX 3 5 3 3 SN 聚醚酯醯胺之芯之2 5丹尼值(2 8分德士)雙組成纖維抽絲, 並將其在每分鐘1400米下捲起。翼/芯/突出芯重量比為 4 5 /4 8 / 7 ’及/R2為約1 · 4。在如此抽絲得之纖維中,芯 穿透至翼中,但其無通常為較佳之降低頸段,如圖3所示。 實施例7 O:\74\74152-9UOl8.DOa 4 _ 47 本紙張尺度適用中國國家標準(CNS) A4規格(21〇 χ跗7公釐) 580527 A7 B7 五、發明説明(45 ) 此實施例說明具有三個翼,其中翼穿透至芯中之雙組成 纖維,且亦說明使用薄噴絲板封裝於製造纖維。翼聚合物 為聚(六亞甲基十二酿胺)(固有黏度1.18,Zy tel® 158,杜 邦公司之柱冊商標),及芯聚合物為PEBAX® 3533SA聚醚 酯醯胺。在2651之喷絲板溫度下利用40/60之翼對芯體積 比將70丹尼值(7 8分德士)之10長絲紗抽絲。使用大致示於 圖1 0之蓟凝結嘴絲板封裝’但個別的板與先前的實施例不 同。圖10A所示之不銹鋼噴絲板A為0.015英吋(0.038公分) 厚,且其具有利用實施例1A之方法切割出之呈各具有兩寬 度,且繞對稱中心隔開120。對稱設置之三直翼1之形態的孔 口;在毛細孔口之上方沒有柱坑。各翼140自其之尖端至中 心與對稱中心一致之0.012英吋(0.030公分)直徑之中心圓形 噴絲板孔142之圓周為0.040英吋(0.102公分)長。接下來參 照圖10B,0.010英吋(0.025公分)厚度之分佈板b係同軸對齊 於噴絲板A上,以致分佈板B之各別的翼孔口 15 〇係與噴絲 板A之翼140對齊;分佈板B之各翼孔口 150自其之尖端至對 稱中心為0.1375英吋(0.349公分)長。計量板c (圖10C)為 0.010英吋(0.025公分)厚,且其具有0.025英吋(0.064公分) 直徑之孔160、0.015英吋(〇·〇3公分)直徑之孔162、及0.010 英吋(0.025公分)直徑之中心孔164。板C係與分佈板B對齊 ,以致在使用時,由熔體池板D (簡要地見圖1 〇)供給至孔 160之翼聚合物及供給至分佈板C之孔162及164之芯聚合物 經板B分佈至板A而形成長絲,其中翼穿透芯。在喷絲板a 中並無柱坑,且板A、B、及C之結合厚度僅為約0.035英吋 O:\74\74l52-9HOI8.DOa 4 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公釐) -48-580527 A7 B7 V. Description of the invention (44) The woven fabric has the following properties: Basis weight = 3.29 ounces per square yard (112 grams per square meter) Thickness = 0.079 inches (2 mm) Weft number = 160 / inch (63 / Cm) Warp = 208 / inch (82 / cm) 5cm width X 10cm length fabric can be stretched by hand by 40%, after which its recovery is more than 95%. Example 6 This example illustrates the use of a full thickness spinneret in the manufacture of the fibers of the present invention. The same spinneret package as before Example 1C was used, except that the spinneret capillaries had the same shape, size, axial alignment, and radial direction as the orifices in spinneret A (Figure 8A). A spinneret (Fig. 11A) having a thickness of 0.3125 inches (0.794 cm) in a cylindrical pit having a diameter of (0.115 inches (0.03 cm) and a diameter of 0.1406 inches (0.357 cm) replaced the support plate E. The wing and core polymer came into contact with each other about 0.87 cm (0.794 cm spinneret + 0.038 cm board A + 0.03 8 cm board B) before forming the fibers. Using the apparatus of FIG. 7, using a 4X draft ratio, a wing with six poly (hexamethylene-co-2-methylpentamethylenehexamethylene diamine) (in which the hexamethylene group is divided into two 80 mol% of amine-derived groups are present) (prepared in a well-known manner with a relative viscosity of 90) and PEB AX 3 5 3 3 SN Polyetheresteramide core 2 5 denier value (2 8 de Taxi) The bicomponent fiber is drawn and rolled up at 1400 meters per minute. The wing / core / protruding core weight ratio is 4 5/4 8/7 ′ and / R2 is about 1.4. In the fiber thus drawn, the core penetrates into the wings, but it is generally not preferable to lower the neck section, as shown in FIG. 3. Example 7 O: \ 74 \ 74152-9UOl8.DOa 4 _ 47 This paper size applies Chinese National Standard (CNS) A4 specifications (21 × 7 mm) 580527 A7 B7 V. Description of the invention (45) This example Describes a bi-component fiber with three wings, of which the wings penetrate into the core, and also illustrates the use of a thin spinneret to encapsulate the manufacturing fibers. The wing polymer is poly (hexamethylene dodecylamine) (inherent viscosity 1.18, Zy tel® 158, a trademark of DuPont) and the core polymer is PEBAX® 3533SA polyetheresteramide. At a spinneret temperature of 2651, 10 filament yarns with a value of 70 denier (78 cents taxi) were drawn using a wing-to-core volume ratio of 40/60. A thistle condensing mouth wireboard package 'shown roughly in Fig. 10 was used, but the individual boards were different from the previous embodiments. The stainless steel spinneret A shown in FIG. 10A is 0.015 inches (0.038 cm) thick and has two widths each cut by the method of Example 1A and spaced 120 apart around the center of symmetry. Symmetrically arranged orifices in the form of three straight wings 1; there are no pillar pits above the capillary orifice. Each wing 140 has a diameter of 0.012 inch (0.030 cm) from the center of the circular center spinneret hole 142 having a circumference of 0.040 inch (0.102 cm). Next, referring to FIG. 10B, the distribution plate b having a thickness of 0.010 inches (0.025 cm) is coaxially aligned with the spinneret A, so that the respective wing apertures 15 of the distribution plate B and the wing 140 of the spinneret A are 140 Align; each wing aperture 150 of distribution plate B is 0.1375 inches (0.349 cm) long from its tip to the center of symmetry. Metering plate c (Figure 10C) is 0.010 inches (0.025 cm) thick and has 0.025 inches (0.064 cm) diameter holes 160, 0.015 inches (0.03 cm) diameter holes 162, and 0.010 inches Center hole 164 in. (0.025 cm) diameter. Plate C is aligned with distribution plate B so that, in use, the wing polymer supplied to hole 160 and the core supplied to holes 162 and 164 of distribution plate C are polymerized by melt pool plate D (shown briefly in Figure 10). The objects are distributed through plate B to plate A to form filaments, with wings penetrating the core. There are no pillar pits in the spinneret a, and the combined thickness of the boards A, B, and C is only about 0.035 inches O: \ 74 \ 74l52-9HOI8.DOa 4 This paper size applies to the Chinese National Standard (CNS) A4 Specifications (210 X 297 mm) -48-

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線 580527 A7 B7 五、發明説明(46 ) (0.089公分)。在1225米/分鐘之牽引輥速度下將紗拉伸3·5χ ’及於大氣壓力蒸氣噴射中鬆弛至1〇45米/分鐘之收捲速度 。當於鬆弛狀態中蒸氣加熱時,紗產生螺旋拈,且具有高 伸展及回復。根據此實施例所製造之纖維之橫剖面的顯微 照片示於圖1 3。 實施例8 此實施例說明使用習知厚度之喷絲板於製造本發明之纖 維。 重複實施例1.Α,但有以下之差異。未使用噴絲板支承板 Ε(見圖8)。喷絲板Α為0.3125英吋(0.794公分)厚,且各抽 絲孔口具有〇·1〇〇英吋(〇·254公分)直徑柱坑及在柱坑底部之 0.015英吋(0.038公分)長的毛細孔。如圖11Α所示,噴絲板 Α中之各喷絲板孔口具有六個直的翼孔口丨7〇,其各具有通 過對稱中心之長軸中心線,且具有〇〇35英吋(0.089公分)之 自其尖端至中心圓孔172之圓周的長度。自各翼之尖端至 0.015英吋(0.038公分)之長度174為〇·〇〇4英吋(0.0 10公分)寬 ,長度176為0.020英叶(0.051公分)長及〇·〇〇2 8英忖(0.007公 分)寬。將各翼之尖端於尖端之一半寬度處圓弧切割。分佈 板Β(見圖11Β)為0.015英吋(0.038公分)厚,且具有六翼孔口 1 50,此孔口各係正中位於噴絲板a中之相對柱坑之上,且 經定向成使板B中之各翼孔口 150與板A之翼孔口 170對齊。 板B中之各翼孔口 150為0.060英吋(0.152公分)長及0.020英 吋(0.051公分)寬,且將其尖端弄圓至〇〇1〇英忖(〇〇25公分) 之半徑。板B中之中心孔152的直徑為o.ioo英吋(0.254公分) -49-Line 580527 A7 B7 V. Description of the invention (46) (0.089 cm). The yarn was stretched at 3 · 5χ ′ at a traction roller speed of 1225 m / min and relaxed to a winding speed of 1045 m / min in an atmospheric pressure steam jet. When steam is heated in a relaxed state, the yarn generates a helix, and has high stretch and recovery. A photomicrograph of a cross section of a fiber manufactured according to this example is shown in FIG. Example 8 This example illustrates the use of spinnerets of known thickness in the manufacture of the fibers of the present invention. Example 1.A was repeated with the following differences. The spinneret support plate E is not used (see Figure 8). The spinneret A is 0.3125 inches (0.794 cm) thick, and each spinning orifice has a diameter of 0.100 inches (0.254 cm) and a pit at the bottom of the pit of 0.015 inches (0.038 cm). Long pores. As shown in FIG. 11A, each spinneret orifice in spinneret A has six straight wing orifices, each of which has a long axis centerline passing through a center of symmetry, and 0.089 cm) from its tip to the circumference of the center circular hole 172. The length 174 from the tip of each wing to 0.015 inches (0.038 cm) is 0.004 inches (0.0 10 cm) wide, the length 176 is 0.020 inches (0.051 cm) long and 0.02 8 inches (0.007 cm) wide. Cut the tip of each wing in an arc at half the width of the tip. Distribution plate B (see Figure 11B) is 0.015 inches (0.038 cm) thick and has six wing orifices 150. Each of these orifices is centered on the opposite column pit in the spinneret a, and is oriented to Align each wing aperture 150 in plate B with wing aperture 170 in plate A. Each of the wing apertures 150 in the plate B is 0.060 inches (0.152 cm) long and 0.020 inches (0.051 cm) wide, and its tip is rounded to a radius of 001 inches (0.025 cm). The diameter of the center hole 152 in the plate B is o.ioo inches (0.254 cm) -49-

O:\74\74152-9H018.DOQ 本纸張尺度適用中國國家標準(CNS) A4規格(210X297公釐) 580527 A7 B7 五、發明説明(47 ) 。計量板C(見圖11C)亦為0.015英吋(0.038公分)厚。在板C ,孔160具有0.008英忖(0.020公分)之直徑,且其距直徑為 0.080英吋(0.203公分)之中心孔162之中心0.1 〇〇英忖(0.254 公分)。板C係與板B對齊,以致板C之六個孔160係在板B 之翼孔口 1 5 0之中心線的上方。將板排列成使供給至板c之 孔162的彈性芯聚合物通過板B及A之中心,且形成纖維之 芯。將非彈性翼聚合物供給至板C中之孔16 0,並通過板b 及A之翼孔口,而形成纖維之翼。翼及芯聚合物先於在噴絲 板A面上方0.328英吋(0.833公分)之分佈板B之上方接觸, 由噴絲板A擠製得纖維。 噴絲板溫度為247°C。將14長絲之紗抽絲,塗布5重量百 分比之聚醚酯基處理劑取代先前所使用之處理劑,及使紗 在捲起之前鬆弛1 5 %(以拉伸紗之長度計)。經拉伸及部分 鬆弛之紗具有75丹尼值(83分德士)之線性密度,及Ri/r 為1 ·20。纖維之橫剖面的顯微照片示於圖6。 雖然本發明已結合其之詳述作說明,但應明瞭前述之詳 述的性質係為舉例及說明用,其係要說明本發明及其之較 佳具體實施例。透過例行的實驗,熟悉技藝人士當知曉可 不脫離本發明之精神而作明顯的修改及變化。O: \ 74 \ 74152-9H018.DOQ This paper size is applicable to China National Standard (CNS) A4 specification (210X297 mm) 580527 A7 B7 V. Description of invention (47). Gauge plate C (see Figure 11C) is also 0.015 inches (0.038 cm) thick. In plate C, the hole 160 has a diameter of 0.008 inches (0.020 cm) and a distance of 0.100 inches (0.254 cm) from the center of the central hole 162 having a diameter of 0.080 inches (0.203 cm). The plate C is aligned with the plate B so that the six holes 160 of the plate C are above the center line of the wing aperture 150 of the plate B. The plate is arranged such that the elastic core polymer supplied to the holes 162 of the plate c passes through the centers of the plates B and A, and forms a core of the fiber. The non-elastic wing polymer is supplied to the holes 160 in the plate C and passes through the wing orifices of the plates b and A to form a fiber wing. The wing and core polymer contacted above the distribution plate B 0.328 inches (0.833 cm) above the surface of the spinneret A, and fibers were extruded from the spinneret A. The spinneret temperature was 247 ° C. The 14-filament yarn was drawn, coated with a 5 weight percent polyetherester-based treatment agent to replace the previously used treatment agent, and the yarn was relaxed by 15% (based on the length of the drawn yarn) before being rolled up. The stretched and partially slackened yarn had a linear density of 75 denier (83 cents taxi), and Ri / r was 1.20. A photomicrograph of a cross section of the fiber is shown in FIG. Although the present invention has been described in conjunction with its detailed description, it should be understood that the foregoing detailed nature is illustrative and illustrative in nature, and is intended to illustrate the present invention and its preferred embodiments. Through routine experimentation, those skilled in the art should know that obvious modifications and changes can be made without departing from the spirit of the invention.

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Claims (1)

27g ^ i • / . --'j ... ^ A B c D 號專利申請案 甲又帽專利範圍替換本(92年8月) 、申請專利範圍 1 · 種可伸展合成聚合物纖維,包括含熱塑性彈性聚合物 又軸芯,及複數個附著至芯且包含熱塑性、非彈性聚合 物之翼,其中該翼聚合物或芯聚合物之至少一者突出至 另一聚合物内。 2· 根據申請專利範圍第1項之纖維,其中該芯包含一外部 半徑R i、一内邵半徑R 2,及R丨/ R 2係大於J . 2。 3·根據申請專利範圍第2項之纖維,其中Ri/R2係在κ3至 2.0之範圍内’.非彈性翼聚合物對彈性芯聚合物之重量 比係在10/90至70/3 0之範圍内,及退漿後伸展(after boil-〇ff stretch)係至少 20% 0 4·根據申請專利範圍第1項之纖維,其中該突出聚合物包 括遠端擴大的末端部分,及將末端部分結合至其餘之突 出聚合物,而於其中形成至少一頸縮部分的降低頸段。 5·根據申請專利範圍第1項之纖維,其中該翼實質上為相 同尺寸,且實質上係對軸芯對稱設置。 6. 根據申請專利範圍第1項之纖維,其中該非彈性聚合物 係選自聚醯胺、非彈性聚烯烴、及聚酯所組成之群,及 咸彈性聚合物係選自熱塑性聚胺甲酸酯、熱塑性聚酯彈 性體、熱塑性聚烯烴、熱塑性聚酯醯胺彈性體及熱塑性 聚醚酯醯胺彈性體所組成之群。 7. 根據申請專利範圍第1項之纖維,其更包括加至翼聚合 物,以改良翼對芯之黏著的添加劑,其中該纖維具有低 於2 · 5之脫層評比。 8·根據申請專利範圍第7項之纖維,其中該非彈性聚合物 O:\74\74152-920807.DOa 5 ^ 本紙張尺度適财S國家鮮(CNS) Α4規格(210 X 297公*y 580527 A8 B8 C8 、申請專利-- 係選自(a)聚(六亞甲基己二醯胺)及其與2_甲基五亞甲二 胺之共聚物及(b)聚己内醯胺所組成之群,及該彈性聚 合物係為聚醚醯胺。 9. 一種包括根據申請專利範圍第丨項之纖維之衣物。 10.種可伸展合成聚合物纖維,包括含熱塑性彈性聚合物 之轴心,及複數個附著至芯之含至少一熱塑性非彈性聚 e物之翼,其中該纖維具有低於i之脫層評比及至少 2 0 %之退漿後伸展。 Π· 一種將連續聚合纖維抽絲之熔融抽絲方法,包括: 使包含非彈性聚合物之嫁體及包含彈性聚合物之熔體 通過噴絲板,而形成具有複數個附著至芯之翼之可伸展 合成聚合物纖維,其中該翼聚合物或芯聚合物之至少一 者突出至另一聚合物内;於纖維離開噴絲板之後使其驟 冷,以使纖維冷卻;及收集纖維。 12.根據申請專利範圍第1 1項之方法,其包括於驟冷之後使 纖維熱鬆弛,以致其展現至少2 0 %之退漿後伸展的額外 步驟。 13·根據申請專利範圍第1 2項之方法,其中該熱鬆弛步驟係 利用乾燥空氣、熱水或超過大氣壓力之蒸氣的加熱介質 ,當加熱介質為該乾燥空氣時在80°C至120°C之範圍内 之溫度下,當加熱介質為該熱水時在75 °C至100 °C下, 及當加熱介質為該超過大氣壓力之蒸氣時在1〇1。〇至115 °(:下進行。 14.根據申請專利範圍第1 1項之方法,其包括於驟冷之後使 -2 - O:\74\74152^920807. DOQ 5 本紙張尺度適用中國國家標準(CNS) A4規格(210 χ 297公釐) 580527 ABCD 申請專利範圍 纖維鬆弛以在鬆弛之前之纖維長度計1 %至3 5 %之範圍 内之額外步騾。 15. —種用以熔融擠製第一及第二合成聚合物以製造纖維之 噴絲板封裝,包括: 包含可接受第一聚合物熔體之第一組孔及可接受第二 水合物溶體之第二組孔的計量板; 與刀佈板對齊及接觸之噴絲板,此噴絲板具有貫穿的 毛細孔及具有低於噴絲板毛細孔長度之6〇%之柱坑長度 ;及 與噴絲板對齊及接觸,具有較毛細孔大之孔之噴絲板 支承板; 其中孩板經對齊,以致經供給至計量板之第一及第二 聚合物通過分佈板、噴絲板、及噴絲板支承板,而形成 纖維。 16·根據申請專利範圍第15項之噴絲板封裝,其中該喷絲板 柱坑長度係低於噴絲板毛細孔長度之4〇%。 17·根據中請專利範圍第15項之噴絲板封裝,其中該喷絲板 支承板孔為張開。 18·根據申請專利範圍第丨5項之噴絲板封裝,其中該孔及毛 細孔係利用雷射切割。 19·根據申請專利範圍第丨5項之噴絲板封裝,其更包括一分 佈板。 20.根據申請專利範圍第19項之噴絲板封裝,其中該分佈板 及嘴絲板之最大結合厚度係低於〇 · 3公分。 O:\74\74152-920807. DOC\ 527g ^ i • /.-'J ... ^ AB c D Patent Application A and Cap Patent Scope Replacement (August 1992), Patent Application Scope 1 · Extensible synthetic polymer fibers, including The thermoplastic elastomeric polymer has a shaft core and a plurality of wings attached to the core and comprising a thermoplastic, non-elastic polymer, wherein at least one of the wing polymer or the core polymer protrudes into the other polymer. 2. The fiber according to item 1 of the scope of the patent application, wherein the core includes an outer radius Ri, an inner radius R2, and R 丨 / R2 are larger than J.2. 3. The fiber according to item 2 of the patent application scope, in which Ri / R2 is in the range of κ3 to 2.0 '. The weight ratio of the non-elastic wing polymer to the elastic core polymer is in the range of 10/90 to 70/3 0 Within the range, and after boil-〇ff stretch is at least 20% 0 4 according to the scope of the patent application of the first fiber, wherein the protruding polymer includes the distal end of the enlarged end portion, and the end portion A lower neck segment that is bonded to the remaining protruding polymer, forming at least one necked portion therein. 5. The fiber according to item 1 of the scope of patent application, wherein the wings are substantially the same size and are arranged symmetrically to the axial core. 6. The fiber according to item 1 of the patent application scope, wherein the non-elastic polymer is selected from the group consisting of polyamide, non-elastic polyolefin, and polyester, and the salty elastic polymer is selected from thermoplastic polyurethane. Ester, thermoplastic polyester elastomer, thermoplastic polyolefin, thermoplastic polyester ammonium elastomer and thermoplastic polyetherester ammonium elastomer. 7. The fiber according to item 1 of the patent application scope, further comprising an additive added to the wing polymer to improve wing-to-core adhesion, wherein the fiber has a delamination ratio lower than 2.5. 8. The fiber according to item 7 of the scope of the patent application, in which the non-elastic polymer O: \ 74 \ 74152-920807.DOa 5 ^ This paper is suitable for the country S (CNS) A4 size (210 X 297 public * y 580527 A8, B8, C8, patent application-are selected from (a) poly (hexamethylenehexamethylenediamine) and its copolymer with 2-methylpentamethylenediamine and (b) polycaprolactam The group and the elastic polymer is polyetheramide. 9. A garment comprising fibers according to item 丨 of the patent application scope. 10. An extensible synthetic polymer fiber including a shaft containing a thermoplastic elastic polymer Heart, and a plurality of wings containing at least one thermoplastic non-elastic polymer e attached to the core, wherein the fiber has a delamination ratio lower than i and at least 20% stretch after desizing. Π · A continuous polymer fiber A spinning method for spinning, including: passing a graft containing a non-elastic polymer and a melt containing an elastic polymer through a spinneret to form a stretchable synthetic polymer fiber having a plurality of wings attached to a core, Wherein at least one of the wing polymer or the core polymer protrudes to the other In a polymer; quenching the fibers after they exit the spinneret to cool the fibers; and collecting the fibers. 12. A method according to item 11 of the patent application scope comprising thermally relaxing the fibers after quenching, So that it exhibits an additional step of at least 20% stretching after desizing. 13. The method according to item 12 of the scope of the patent application, wherein the thermal relaxation step uses a heating medium of dry air, hot water or steam exceeding atmospheric pressure , When the heating medium is the dry air at a temperature in the range of 80 ° C to 120 ° C, when the heating medium is the hot water, at 75 ° C to 100 ° C, and when the heating medium is the above atmospheric pressure The steam of force is performed at 101.0 to 115 ° (:). 14. The method according to item 11 of the scope of patent application, which comprises -2: O: \ 74 \ 74152 ^ 920807 after quenching. DOQ 5 This paper size is applicable to Chinese National Standard (CNS) A4 (210 x 297 mm) 580527 ABCD patent scope Fiber relaxation is an additional step within the range of 1% to 35% based on the fiber length before relaxation. 15. — a kind of melt extrusion No. 1 and No. A spinneret package for synthesizing polymers to manufacture fibers, comprising: a metering plate including a first set of holes that can accept a first polymer melt and a second set of holes that can accept a second hydrate solution; and a knife cloth plate Aligned and contacted spinneret, the spinneret has a capillary hole that penetrates and a column pit length that is less than 60% of the length of the capillary hole of the spinneret; The spinneret support plate of the hole; wherein the child plates are aligned so that the first and second polymers supplied to the metering plate pass through the distribution plate, the spinneret, and the spinneret support plate to form fibers. 16. The spinneret package according to item 15 of the scope of the patent application, wherein the length of the pits of the spinneret is less than 40% of the capillary hole length of the spinneret. 17. The spinneret package according to item 15 of the patent claim, wherein the spinneret support plate hole is open. 18. The spinneret package according to item 5 of the patent application, wherein the hole and the capillary hole are cut by laser. 19. The spinneret package according to item 5 of the patent application scope, which further includes a distribution board. 20. The spinneret package according to item 19 of the scope of patent application, wherein the maximum combined thickness of the distribution plate and the nozzle wire plate is less than 0.3 cm. O: \ 74 \ 74152-920807. DOC \ 5
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