KR20060078605A - Process for preparing multilobal fine denier polyester - Google Patents

Process for preparing multilobal fine denier polyester Download PDF

Info

Publication number
KR20060078605A
KR20060078605A KR1020040116903A KR20040116903A KR20060078605A KR 20060078605 A KR20060078605 A KR 20060078605A KR 1020040116903 A KR1020040116903 A KR 1020040116903A KR 20040116903 A KR20040116903 A KR 20040116903A KR 20060078605 A KR20060078605 A KR 20060078605A
Authority
KR
South Korea
Prior art keywords
section
cross
yarn
polyester
spinneret
Prior art date
Application number
KR1020040116903A
Other languages
Korean (ko)
Other versions
KR100630266B1 (en
Inventor
김범석
손양국
Original Assignee
주식회사 효성
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 주식회사 효성 filed Critical 주식회사 효성
Priority to KR1020040116903A priority Critical patent/KR100630266B1/en
Publication of KR20060078605A publication Critical patent/KR20060078605A/en
Application granted granted Critical
Publication of KR100630266B1 publication Critical patent/KR100630266B1/en

Links

Images

Classifications

    • 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
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/62Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters

Abstract

본 발명은 단사 섬도가 0.5 내지 1 데니어이고 단사수가 70 이상인 폴리에스테르 이형단면(三葉 및 四葉단면) 극세 섬유를 제조함에 있어서, 지연냉각부의 길이를 20mm이하, 냉각공기 취출면과 필라멘트간의 거리가 2mm 내지 30mm로 방사함으로써 노즐 하부의 지연냉각부 및 냉각공기 취출면과 사조간 거리를 제어하고 또한 방사노즐 구멍 단면을 높은 이형도에 적합하게 설계하여 이형도가 3 이상이며, 공정성 및 물성이 우수하며 염색성이 양호한 폴리에스테르 극세 섬유 이형단면사를 제조할 수 있다.In the present invention, in the production of polyester release cross-section (three and four-sided cross-section) ultrafine fibers having a single yarn fineness of 0.5 to 1 denier and a single yarn number of 70 or more, the length of the delayed cooling portion is 20 mm or less, and the distance between the cooling air ejection surface and the filament is Spinning from 2mm to 30mm controls the distance between the delayed cooling section and the cooling air ejection surface of the lower part of the nozzle and thread, and also designes the cross section of the spinneret hole for high mold release degree, and the mold release degree is 3 or more. This favorable polyester microfiber release cross section yarn can be manufactured.

이는 이형단면사의 원형단면 환산 지름이 동일 단사섬도를 갖는 원형단면 대비 2배 이상 높아짐에 따라 제품 적용시에 경량 및 보온 특성을 갖는 제품 전개에 유리하며, 이형단면 특성인 난반사 광택에 의한 광택차별화 효과를 나타낸다.This is advantageous for the development of products with light weight and thermal insulation properties when the product is applied, as the circular cross-sectional diameter of the shaped cross section yarn is more than 2 times higher than that of the circular cross section with the same single yarn fineness. Indicates.

이형도, 이형단면, 극세섬유, 지연냉각부, 냉각공기, 삼엽, 사엽Shape diagram, shape section, micro fiber, delayed cooling part, cooling air, three leaf, four leaf

Description

이형단면 폴리에스테르 극세 섬유의 제조방법{Process for preparing multilobal fine denier polyester} Process for preparing multi-section polyester microfiber {Process for preparing multilobal fine denier polyester}             

도 1은 본 발명에서 사용된 방사구금의 삼엽 단면 개략도이다.1 is a schematic diagram of the three-leaf cross section of the spinneret used in the present invention.

도 2은 본 발명에서 사용된 방사구금의 사엽 단면 개략도이다.2 is a cross-sectional schematic diagram of the four-leaf spinneret used in the present invention.

* 도면의 부호 설명* Explanation of symbols in the drawings

A는 각 삼엽 또는 사엽 방사구금에서 엽 중간 부분의 폭A is the width of the middle part of the lobe in each trilobite or 4-lobed spinneret

B는 각 삼엽 또는 사엽 방사구금에서 말단 원형 부분의 직경B is the diameter of the terminal circular portion in each trilobite or tetralobal spinneret

C는 각 삼엽 또는 사엽 방사구금에서 엽 길이C is lobe length at each trilobite or tetralobal spinneret

본 발명은 폴리에스테르 이형단면 극세 섬유 및 그 제조방법에 관한 것으로 상세하게는 단사 섬도가 0.5 데니어 이상, 1.0 데니어 이하이며, 단사수가 70 이상인 폴리에스테르 이형단면 극세 섬유를 용융방사 함에 있어서, 노즐 하부의 지연냉 각부 길이를 조정하고 냉각공기 취출면과 사조간 거리를 제어하고 방사구금을 高 이형도 발현이 가능토록 최적화함으로써 이형도, 공정성 및 물성이 우수하며 염색성이 양호한 폴리에스테르 이형단면 극세 섬유를 제조하는 방법에 관한 것이다.The present invention relates to a polyester release cross-section fine fiber and a method for producing the same, in particular single yarn fineness of 0.5 denier or more, 1.0 denier or less, in the melt spinning the polyester release cross-section fine fibers having a single yarn number of 70 or more, A method for producing a polyester release cross-section microfiber with excellent mold release, fairness and physical properties and good dyeability by adjusting the length of the delayed cooling section, controlling the distance between the ejection surface of the cooling air and the thread, and optimizing the spinneret for high mold release. It is about.

최근 폴리에스테르 섬유업계에서는 고부가가치를 갖는 차별화 소재의 개발이 활발하게 진행되고 있는데, 이러한 목적으로 단사 섬도가 1.0 데니어 이하인 극세 섬유의 생산이 보편화되고 있다. 이에 더 나아가 단사섬도가 0.5 데니어 이하인 폴리에스테르 극세사는 물론 이형단면사 극세사에 대한 관심이 집중되면서 현재는 각사마다 개발에 총력을 기울이고 있다.Recently, in the polyester fiber industry, development of differentiating materials having high value-added is actively progressed, and for this purpose, production of ultrafine fibers having a single yarn fineness of 1.0 denier or less is becoming common. Furthermore, attention has been focused on the development of polyester microfibers with single yarn fineness of 0.5 denier or less as well as hetero-splitting yarn microfibers.

그러나 이형단면 극세사의 경우, 방사 드래프트(Draft)의 급증으로 이형단면 확보가 어렵고, 사조간의 냉각 불균일로 인해 방사 공정상에서 단사절 또는 단면불균일이 다발하는 문제점을 갖는다.However, in the case of a microfiber of a cross section, it is difficult to secure a cross section due to a sudden increase in the spinning draft, and there is a problem in that single yarn section or cross section unevenness occurs in the spinning process due to cooling unevenness between yarns.

일반적으로 폴리에스테르 이형단면 극세 섬유의 제조에 있어 필라멘트들간의 균일 냉각이 원사의 품질을 결정하는 중요한 요인이며 적정한 방사노즐 설계가 이형도 확보에 있어 핵심 기술이다. 통상적인 냉각방식인 전면단방향 냉각방식으로는 충분한 균일 냉각이 이루어지지 않아 사조간의 융착 등에 의해 공정성이 저하되며 불균일한 물성을 얻게 된다. 이러한 단점을 보완하기 위한 대안으로 국내 특허공개 제 92-15834호에는 전방향 원통형송출방식 냉각장치에 의한 냉각방식이 제안되는 등 필라멘트들간의 균일 냉각을 위한 연구가 꾸준히 진행되고 있다.In general, in the manufacture of polyester release cross-section microfibers, uniform cooling between filaments is an important factor in determining yarn quality, and proper spinning nozzle design is a key technology in securing mold release. In the general unidirectional cooling method, the front unidirectional cooling method does not achieve sufficient uniform cooling, resulting in deterioration of fairness due to fusion between yarns and nonuniform physical properties. As an alternative to compensate for these drawbacks, Korean Patent Publication No. 92-15834 proposes a cooling method by an omni-directional cylindrical delivery system cooling device, and the research for uniform cooling among filaments is steadily being conducted.

본 발명은 단사 섬도가 0.5 데니어 이상 1.0 데니어 이하이며, 단사수가 70 이상인 폴리에스테르 이형단면(三葉 및 四葉단면) 극세 섬유를 용융방사하는데 있어서, 지연냉각부의 길이 및 냉각공기 취출면과 필라멘트간의 거리를 제어하여 필라멘트들간의 냉각을 균일하게 유지시키고, 방사구금 최적화를 통해 高이형도, 공정성 및 물성이 우수하며 염색성이 양호한 폴리에스테르 이형단면 극세 섬유를 제조하는 것을 목적으로 한다.
The present invention has a single yarn fineness of 0.5 denier to 1.0 denier and has a single yarn of 70 or more, and melt-spun a polyester release section (three and four leaf sections) of ultrafine fibers, the length of the delay cooling section and the distance between the cooling air ejection surface and the filament. The purpose of the present invention is to maintain a uniform cooling between the filaments, and to optimize the spinneret to produce a polyester release cross-section fine fiber having excellent mold release, fairness and physical properties and good dyeability.

앞서 상술한 본 발명의 목적을 달성하기 위하여, In order to achieve the above object of the present invention,

본 발명은 단사 섬도가 0.5~1.0 데니어이고, 단사수가 70이상인 폴리에스테르 이형단면 극세 섬유에 있어서, 폴리에틸렌테레프탈레이트 중합체를 아래 (1)~(4)를 만족하는 방사구금을 사용하여 용융방사한 후 방사구금 직하에 설치된 20mm이하의 지연 냉각부를 통과시켜 지연 냉각시킨 다음, 냉풍취출면과 필라멘트간의 최대거리를 2 ~ 30mm로 제어된 냉각부를 통과시켜 미연신사를 수득하는 단계; 상기 미연신사를 연신시키는 단계들에 의해 제조되는 폴리에스테르 이형단면 극세 섬유를 제공한다.The present invention is a polyester release cross-section fine fiber having a single yarn fineness of 0.5 to 1.0 denier and a single yarn number of 70 or more, after melt-spun polyethylene terephthalate polymer using spinnerets satisfying the following (1) to (4) Delay cooling by passing a delay cooling unit of 20 mm or less installed directly below the spinneret, and then passing uncooled yarn through a cooling unit controlled to have a maximum distance of 2 to 30 mm between the cold air extraction surface and the filament; It provides a polyester release cross-section fine fibers produced by the step of stretching the non-drawn yarn.

(1) B ≥ 2 × A(1) B ≥ 2 × A

(2) C ≥ 2.5 × B(2) C ≥ 2.5 × B

(3) 방사구금 단면적(mm2) ≤ 날개수(3 혹은 4) × 0.04(3) spinneret cross-sectional area (mm2) ≤ number of wings (3 or 4) × 0.04

(4) 삼엽 또는 사엽 단면형태(4) three- or four-leaf cross-sectional shape

(단, A는 각 삼엽 또는 사엽 방사구금에서 중간 부분의 엽 폭, B는 각 삼엽 또는 사엽 방사구금에서 말단 원형 부분의 직경, C는 각 삼엽 또는 사엽 방사구금에서 엽 길이, 도 1, 2 참조)(Where A is the leaf width of the middle part in each trilobite or four-leaf spinneret, B is the diameter of the terminal circular part in each trilobite or four-leaf spinneret, C is the leaf length in each three- or four-leaf spinneret, see FIGS. 1 and 2). )

또한, 상기 폴리에스테르 이형단면 극세섬유의 이형도가 3.0 이상인 것이 바람직하다.Moreover, it is preferable that the mold release degree of the said polyester mold release cross-section microfiber is 3.0 or more.

또한, 상기 폴리에스테르 이형단면 극세섬유의 물성이 아래 1) 내지 2을 만족하는 것이 바람직하다.In addition, it is preferable that the physical properties of the polyester release cross-section microfiber satisfy the following 1) to 2.

1) 강도 4.0g/den이상1) Strength 4.0g / den or more

2) S = 강도(g/den) × 파단신도(%)1/2 ≥ 252) S = strength (g / den) x elongation at break (%) 1/2 ≥ 25

또한, 상기 극세섬유의 미연신사 물성이 아래 1) 내지 2)를 동시에 만족하는 것이 바람직하다.In addition, it is preferable that the unstretched yarn properties of the ultrafine fibers simultaneously satisfy the following 1) to 2).

1) T(χ) ≥ 1.2 g/den1) T (χ) ≥ 1.2 g / den

T(χ) ; χ% 연신시의 강력(g)÷원사데니어T (χ); χ% strength (g) ÷ yarn denier

χ ; 파단신도(%)÷2χ; Elongation at Break (%) ÷ 2

2) S = 강도(g/den) × 파단신도(%)1/2 ≥ 252) S = strength (g / den) x elongation at break (%) 1/2 ≥ 25

즉, 본 발명은 노즐 하부의 지연 냉각부 및 냉풍 취출면과 사조간 거리를 제어하여 사조간의 냉각균일성을 확보하고 방사구금 설계를 최적화하여 이형도를 올려주는 폴리에스테르 이형단면 극세 섬유의 제조 방법에 관한 것이다.That is, the present invention is a method for producing a polyester release section microfiber which increases the degree of release by securing the cooling uniformity between yarns and optimizing the spinneret design by controlling the distance between the delayed cooling unit and the cold air blowout surface and the yarns at the bottom of the nozzle. It is about.

폴리에스테르 극세 섬유 제조 방법의 핵심 기술은 필라멘트에 동일 위치에서 동일한 냉각효과를 줄 수 있도록 냉각장치를 설계함과 동시에 외란에 대한 사물성의 변동을 최소화하기 위해 방사구금으로부터 압출된 직후에 냉각을 실시하여 사변형을 최소화시키는 것이다. 필라멘트수가 많고 단사 섬도가 낮은 폴리에스테르 극세 섬유의 제조를 위해서는 냉풍이 모든 필라멘트와 균일하게 접촉해야하며, 또한 냉풍간이나 냉풍과 사조간의 충돌에 의한 와류를 제어해야한다.The core technology of the polyester microfiber manufacturing method is to design the cooling device to give the filament the same cooling effect at the same position, and to cool it immediately after being extruded from the spinneret to minimize the variation of the object to disturbance. Minimize quadrilaterals. To produce polyester microfibers with a high number of filaments and low single yarn fineness, cold air must be in uniform contact with all the filaments, and also control of vortices caused by cold winds or collisions between cold winds and yarns.

본 발명에서는 이의 개선방법으로 노즐 직하의 지연냉각부의 길이를 짧게 하고, 냉풍 취출면과 필라멘트간의 거리를 짧게 제어함으로써 필라멘트간의 균일 냉각을 가능케해 폴리에스테르 극세 섬유의 공정성 및 물성을 개선할 수 있었다. 이때 지연 냉각부의 길이는 20mm이하, 냉풍 취출면과 필라멘트간의 거리는 2 ~ 30mm로 제어하였다. 노즐 직하 지연 냉각부의 길이가 20mm를 넘으면 공정성이 저하되며, 냉풍 취출면과 필라멘트간의 거리가 30mm를 초과하면 물성이 불균일해지고 공정성도 저하되는 것을 확인하였다.In the present invention, by shortening the length of the delayed cooling portion directly below the nozzle and controlling the distance between the cold air extraction surface and the filament, the uniform cooling between the filaments is enabled, thereby improving the processability and physical properties of the polyester microfibers. At this time, the length of the delayed cooling unit is 20mm or less, the distance between the cold air extraction surface and the filament was controlled to 2 ~ 30mm. When the length of the delayed cooling part directly under the nozzle exceeds 20 mm, the processability is lowered. When the distance between the cold wind extraction surface and the filament exceeds 30 mm, the physical properties are uneven and the processability is also lowered.

폴리에스테르 이형단면 방사구금은 대개 방사구금단면 이형도(외접원 지름/내접원 지름)가 5 이하인데 반해, 본 발명에 사용된 방사구금은 단면 이형도를 8이상 올리는 동시에 앞에서 언급된 근접 냉각기술을 접목시켜 최종 원사의 이형도를 3.0 이상 올릴 수 있는 것이다. 이때 방사구금단면 이형도가 너무 낮을 경우엔 원하는 원사 이형도를 낼 수 없었으며, 과도하게 높을 경우엔 제사 공정성이 떨어지는 단점이 있었다.Polyester release cross-section spinnerets usually have a spinneret cross-sectional release (circle circle diameter / inscribed circle diameter) of 5 or less, whereas spinnerets used in the present invention increase the cross-sectional release rate of 8 or more and combine the above-mentioned near-cooling techniques to obtain You can raise the degree of release of the yarn to 3.0 or more. At this time, if the spinneret cross-sectional release degree is too low, the desired yarn release degree could not be produced, and if excessively high, the yarn fairness was inferior.

또한, 본 발명의 핵심적인 기술구성은 균일한 냉각에 의해 미연신사가 수득된다. 본 발명에 의해 용융 방사된 미연신사 (POY)의 경우, 일반적인 미연신사가 갖는 물성대비 다음의 특성을 나타낸다. 즉, 본 발명에 의해 방사구금 직하에서 사조를 냉각하고 사조에 균일한 냉각효과를 부여함으로써 단사섬도가 낮아도 물성이 균일하며 원사의 강력이 높아지는 특성을 나타낸다. 또한 이 미연신사를 적정 연신비로 연신하였을 경우에도 높은 강력 특성을 그대로 나타냈으며, 이형도, 물성 및 공정성이 우수하며 염색성이 양호한 폴리에스테르 이형단면 극세사를 제조할 수 있다.In addition, the core technical configuration of the present invention, the undrawn yarn is obtained by uniform cooling. In the case of unstretched yarn (POY) melt-spun according to the present invention, the following properties are compared with those of general unstretched yarn. That is, according to the present invention, by cooling the yarn directly under the spinneret and imparting a uniform cooling effect to the yarn, even when the single yarn fineness is low, the physical properties are uniform and the yarn strength is increased. In addition, even when the unstretched yarn was drawn at an appropriate draw ratio, it exhibited high strength properties as it is, and excellent mold release properties, physical properties and processability, and good dyeing cross-section microfiber yarns with good dyeability can be prepared.

상기의 균일 냉각 효과에 의해 아래와 같은 물성 특성을 갖게 된다.The above uniform cooling effect has the following physical properties.

T(χ) ≥ 1.2 g/den  T (χ) ≥ 1.2 g / den

· T(χ) ; χ% 연신시의 강력(g)÷원사데니어          T (χ); χ% strength (g) ÷ yarn denier

· χ ; 파단신도(%)÷2          · Χ; Elongation at Break (%) ÷ 2

S = 강도(g/den) × 파단신도(%)1/2 ≥ 25 S = strength (g / den) × elongation at break (%) 1/2 ≥ 25

이하, 본 발명의 실시예를 통하여 본 발명을 보다 자세히 설명한다.Hereinafter, the present invention will be described in more detail with reference to the following examples.

< 물성 측정방법 ><Property measurement method>

1) 방사 공정성 평가 내용 : ○ - 매우 양호, △ - 보통, × - 불량, 1) Evaluation of radiological fairness: ○-Very good, △-Normal, ×-Poor,

×× - 불가                                  ××-not available

2) T(χ) ; χ% 연신시의 강력(g) ÷ 원사데니어2) T (χ); χ% strength at drawing (g) ÷ yarn denier

χ ; 파단신도(%) ÷ 2   χ; Elongation at Break (%) ÷ 2

3) 강도(g/den) : 파단신도시의 강력 ÷ 원사데니어3) Strength (g / den): strength of broken new city ÷ yarn denier

4) S : 강도(g/den) × 파단신도(%)1/24) S: Strength (g / den) × Elongation at Break (%)

※ 2) ~ 4) : 사의 강ㆍ신도 물성을 30회 측정하여 평균값을 구해서 측정※ 2) ~ 4): Measure the strength and elongation properties of the yarn 30 times to find the average value

5) 이형도 : 외접원 지름 ÷ 내접원 지름 (원사단면을 SEM설비 활용 측정)5) Deformation degree: circumscribed circle diameter ÷ inscribed circle diameter (measuring yarn cross section using SEM equipment)

6) 염색성 평가방법 : ○ - 매우 양호, △ - 보통, × - 불량6) Dyeing method: ○-Very good, △-Normal, ×-Poor

시료 : 원사를 환편기로 20cm 길이가 되도록 편직하였다.Sample: The yarn was knitted to a length of 20 cm with a circular knitting machine.

염욕 : 분산염료 코우-네이비(S-type)을 염료농도 1% o.w.f.로 만든 후, 분산제 (VGT) 1g/L, pH 5.0(초산), 액비 1대 15로 조제하였다.Salt bath: Disperse dye Ko-navy (S-type) was made with a dye concentration of 1% o.w.f., and then prepared with 1 g / L of a dispersant (VGT), pH 5.0 (acetic acid), and a liquid ratio of 1:15.

염색시험 : 시료를 염욕에 넣고, 염색온도를 30~130℃까지 1℃/분으로 일정하게 승온하여 130℃에서 30분간 유지하면서 염색하였다. 염색이 끝난 시료를 충분히 건조 후, 백색판을 넣어 육안으로 염색성을 판정하였다.Dyeing test: The sample was placed in a salt bath, and the dyeing temperature was raised to 30 to 130 ° C. at a constant temperature of 1 ° C./min, followed by dyeing at 130 ° C. for 30 minutes. After the dyeing sample was sufficiently dried, a white plate was placed to visually determine dyeability.

실시예 1Example 1

고유점도 0.63의 폴리에틸렌테레프탈레이트 중합물을 사용하여 방사온도 297℃, 방사구금 치수는 A, B, C가 각각 0.07/0.16/0.40mm, 방사구금 길이가 0.5mm이며 필라멘트수는 72개로 최종 연신사의 단사섬도가 0.5 데니어가 되도록 토출량을 조절하여 방사속도 2,600m/분에서 용융 방사하였다. 냉풍 온도는 20℃로 조정하였고, 냉각지연부는 방사구금 직하에서 설치하여 그 길이를 5mm로 조정하였다. 또한 냉풍취출면과 필라멘트간의 최대거리가 30mm가 되도록 조정하였다. 제조된 폴리에스테르 극세사의 미연신사를 연신비 1.521로 연신하여 연신사를 제조하였다. 미연신사 및 연신사의 공정성, 염색성 및 아래에 정의된 T(χ), S 등의 값을 표 1에 나타내었다.Using polyethylene terephthalate polymer with an intrinsic viscosity of 0.63, spinning temperature 297 ℃, spinneret dimensions of A, B, C are 0.07 / 0.16 / 0.40mm, spinneret length is 0.5mm, and the number of filaments is 72. The discharge amount was adjusted so that the fineness became 0.5 denier and melt spun at a spinning speed of 2,600 m / min. Cold air temperature was adjusted to 20 ℃, the cooling delay was installed directly under the spinneret, the length was adjusted to 5mm. In addition, the maximum distance between the cold air extraction surface and the filament was adjusted to 30mm. The stretched yarn was manufactured by drawing the undrawn yarn of the polyester microfiber at a draw ratio of 1.521. Table 1 shows the fairness, dyeability, and T (χ), S, and the like of the undrawn and drawn yarns.

실시예 2Example 2

최종 연신사의 단사섬도가 1.0 데니어, 지연냉각부의 길이를 20mm, 냉풍취출면과 필라멘트간의 최대거리를 20mm로 조정한 것외엔 실시예 1과 동일한 조건으로 시험하였으며 그 결과를 표 1에 나타내었다.The single yarn fineness of the final stretched yarn was tested in the same conditions as in Example 1 except that 1.0 denier, the length of the delayed cooling portion was 20 mm, and the maximum distance between the cold air extraction surface and the filament was adjusted to 20 mm.

비교예1Comparative Example 1

최종 연신사의 단사섬도가 1.0 데니어, 지연냉각부의 길이를 30mm, 냉풍취출면과 필라멘트간의 최대거리를 20mm로 조정한 것외엔 실시예 1과 동일하게 실시하여 그 결과를 표 1에 나타내었다.The single yarn fineness of the final stretched yarn was 1.0 denier, the length of the delay cooling part was adjusted to 30 mm, and the maximum distance between the cold air extraction surface and the filament was adjusted to 20 mm, and the results are shown in Table 1 below.

비교예 2Comparative Example 2

최종 연신사의 단사섬도가 1.0 데니어, 지연냉각부의 길이를 60mm, 냉풍취출면과 필라멘트간의 최대거리를 20mm로 조정한 것외엔 실시예 1과 동일하게 실시하여 그 결과를 표 1에 나타내었다.The single yarn fineness of the final stretched yarn was 1.0 denier, the length of the delayed cooling portion was 60 mm, and the maximum distance between the cold wind extraction surface and the filament was adjusted to 20 mm.

비교예 3Comparative Example 3

최종 연신사의 단사섬도가 1.0 데니어, 지연냉각부의 길이를 20mm, 냉풍취출면과 필라멘트간의 최대거리를 40mm로 조정한 것외엔 실시예 1과 동일하게 실시하여 그 결과를 표 1에 나타내었다.The single yarn fineness of the final stretched yarn was 1.0 denier, the length of the delayed cooling portion was 20 mm, and the maximum distance between the cold air extraction surface and the filament was adjusted to 40 mm.

비교예 4Comparative Example 4

최종 연신사의 단사섬도가 1.0 데니어, 지연냉각부의 길이를 20mm, 냉풍취출면과 필라멘트간의 최대거리를 120mm로 조정한 것외엔 실시예 1과 동일하게 실시하여 그 결과를 표 1에 나타내었다.The single yarn fineness of the final stretched yarn was 1.0 denier, the length of the delay cooling part was adjusted to 20 mm, and the maximum distance between the cold wind extraction surface and the filament was adjusted to 120 mm, and the results are shown in Table 1 below.

비교예 5Comparative Example 5

최종 연신사의 단사섬도가 1.0 데니어, 지연냉각부의 길이를 30mm, 냉풍취출면과 필라멘트간의 최대거리를 120mm로 조정한 것외엔 실시예 1과 동일하게 실시하여 그 결과를 표 1에 나타내었다.The single yarn fineness of the final stretched yarn was 1.0 denier, the length of the delay cooling part was adjusted to 30 mm, and the maximum distance between the cold wind extraction surface and the filament was adjusted to 120 mm, and the results are shown in Table 1 below.

비교예 6Comparative Example 6

방사구금 치수는 A, B, C가 각각 0.12/0.16/0.40mm으로 조정한 것외엔 실시예 2과 동일하게 실시하여 그 결과를 표 1에 나타내었다.The spinneret dimensions were carried out in the same manner as in Example 2 except that A, B, and C were each adjusted to 0.12 / 0.16 / 0.40 mm, and the results are shown in Table 1.

비교예 7Comparative Example 7

방사구금 치수는 A, B, C가 각각 0.17/0.16/0.30mm으로 조정한 것외엔 실시예 2과 동일하게 실시하여 그 결과를 표 1에 나타내었다.The spinneret dimensions were carried out in the same manner as in Example 2 except that A, B, and C were each adjusted to 0.17 / 0.16 / 0.30 mm, and the results are shown in Table 1.

비교예 8Comparative Example 8

방사구금 치수는 A, B, C가 각각 0.10/0.22/0.55mm으로 조정한 것 외엔 실시예 2과 동일하게 실시하여 그 결과를 표 1에 나타내었다.The spinneret dimensions were carried out in the same manner as in Example 2 except that A, B, and C were each adjusted to 0.10 / 0.22 / 0.55 mm, and the results are shown in Table 1.

[ 표 1 ]TABLE 1

Figure 112004062917205-PAT00001
Figure 112004062917205-PAT00001

본 발명에 의하면 단사섬도 0.5 데니어 이상, 1.0 데니어 이하이며, 단사수가 70이상인 폴리에스테르 이형단면(三葉 및 四葉단면) 극세 섬유를 제조하는데 있어, 노즐 하부의 지연냉각부 및 냉각공기 취출면과 사조간 거리를 제어하고 방사노즐의 구금설계 최적화를 통해 단사섬도 1.0 데니어 이하에서 이형도, 공정성 및 물 성이 우수한 폴리에스테르 이형단면 극세 섬유를 제조할 수 있다.According to the present invention, the single yarn fineness is 0.5 denier or more and 1.0 denier or less, and in the production of polyester release cross-section (three and four leaf cross-section) ultrafine fibers having a single yarn number of 70 or more, the delayed cooling portion and the cooling air ejection surface and the thread of the lower part of the nozzle By controlling the distance between them and optimizing the spinneret's design, it is possible to produce polyester-shaped cross-section microfibers with excellent mold release, fairness and physical properties at single yarn fineness of 1.0 denier or less.

이는 이형단면사의 원형단면 환산 지름이 동일 단사섬도를 갖는 원형단면 대비 2배 이상 높아짐에 따라 제품 적용시에 경량 및 보온 특성을 갖는 제품전개에 유리하며, 이형단면 특성인 난반사 광택에 의한 광택차별화 효과를 갖는 원사를 제조할 수 있다.














This is advantageous for the development of products with light weight and heat retention characteristics when applied to the product as the circular cross-sectional diameter of the shaped cross section yarn is more than two times higher than the circular cross section having the same single yarn fineness, and the effect of gloss differentiation by the diffuse reflection gloss, A yarn having can be prepared.














Claims (4)

단사 섬도가 0.5~1.0 데니어이고, 단사수가 70이상인 폴리에스테르 이형단면 극세 섬유에 있어서, In polyester release cross-section fine fibers having a single yarn fineness of 0.5 to 1.0 denier and a single yarn number of 70 or more, 폴리에스테르 중합체를 아래 (1)~(4)를 만족하는 방사구금을 사용하여 용융방사한 후, 방사구금 직하에 설치된 20mm이하의 지연 냉각부를 통과시켜 지연 냉각시킨 다음, 냉풍취출면과 필라멘트간의 최대거리를 2 ~ 30mm로 제어된 냉각부를 통과시켜 미연신사를 수득하는 단계;The polyester polymer is melt spun using a spinneret satisfying the following (1) to (4), and then delayedly cooled by passing through a 20 mm or less delay coolant installed directly below the spinneret, and then a maximum between the cold air extraction surface and the filament. Passing uncooled yarn through a cooling section controlled at a distance of 2 to 30 mm; 상기 미연신사를 연신시키는 단계들에 의해 제조되는 것을 특징으로 하는 폴리에스테르 이형단면 극세 섬유.Polyester sectional cross-section ultrafine fiber, characterized in that produced by the step of stretching the undrawn yarn. (1) B ≥ 2 × A(1) B ≥ 2 × A (2) C ≥ 2.5 × B(2) C ≥ 2.5 × B (3) 방사구금 단면적(mm2) ≤ 날개수(3 혹은 4) × 0.04(3) spinneret cross-sectional area (mm2) ≤ number of wings (3 or 4) × 0.04 (4) 삼엽 또는 사엽 단면형태(4) three- or four-leaf cross-sectional shape (단, A는 각 삼엽 또는 사엽 방사구금에서 중간 부분의 엽 폭, B는 각 삼엽 또는 사엽 방사구금에서 말단 원형 부분의 직경, C는 각 삼엽 또는 사엽 방사구금에서 엽 길이)(Where A is the leaf width of the middle part in each trilobite or four-leaf spinneret, B is the diameter of the terminal circular part in each three- or four-leaf spinneret, and C is the leaf length in each three- or four-leaf spinneret) 제 1 항에 있어서,The method of claim 1, 상기 폴리에스테르 이형단면 극세섬유의 이형도가 3.0 이상인 것을 특징으로 하는 폴리에스테르 이형단면 극세 섬유. The polyester release cross-section fine fiber, characterized in that the degree of release of the polyester release cross-section fine fiber 3.0 or more. 제 1 항에 있어서,The method of claim 1, 상기 폴리에스테르 이형단면 극세섬유의 물성이 아래 1) 내지 2을 만족하는 것을 특징으로 하는 폴리에스테르 이형단면 극세 섬유.The polyester release cross-section microfiber, characterized in that the physical properties of the polyester cross-section microfiber satisfies 1) to 2 below. 1) 강도 4.0g/den이상1) Strength 4.0g / den or more 2) S = 강도(g/den) × 파단신도(%)1/2 ≥ 252) S = strength (g / den) x elongation at break (%) 1/2 ≥ 25 제 1 항에 있어서,The method of claim 1, 상기 극세섬유의 미연신사 물성이 아래 1) 내지 2)를 동시에 만족하는 것을 특징으로 하는 폴리에스테르 이형단면 극세 섬유.The polyester release cross-section microfine fiber, characterized in that the unstretched yarn properties of the microfine fiber at the same time satisfy the following 1) to 2). 1) T(χ) ≥ 1.2 g/den1) T (χ) ≥ 1.2 g / den T(χ) ; χ% 연신시의 강력(g)÷원사데니어          T (χ); χ% strength (g) ÷ yarn denier χ ; 파단신도(%)÷2          χ; Elongation at Break (%) ÷ 2 2) S = 강도(g/den) × 파단신도(%)1/2 ≥ 252) S = strength (g / den) x elongation at break (%) 1/2 ≥ 25
KR1020040116903A 2004-12-30 2004-12-30 Process for preparing multilobal fine denier polyester KR100630266B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020040116903A KR100630266B1 (en) 2004-12-30 2004-12-30 Process for preparing multilobal fine denier polyester

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020040116903A KR100630266B1 (en) 2004-12-30 2004-12-30 Process for preparing multilobal fine denier polyester

Publications (2)

Publication Number Publication Date
KR20060078605A true KR20060078605A (en) 2006-07-05
KR100630266B1 KR100630266B1 (en) 2006-09-29

Family

ID=37170478

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020040116903A KR100630266B1 (en) 2004-12-30 2004-12-30 Process for preparing multilobal fine denier polyester

Country Status (1)

Country Link
KR (1) KR100630266B1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110983575A (en) * 2019-12-29 2020-04-10 江苏恒力化纤股份有限公司 Preparation method of oxford fabric

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101894724B1 (en) * 2016-06-08 2018-09-05 주식회사 휴비스 Thermally Adhesive Shaped Conjugate yarn

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3953417B2 (en) 2002-12-18 2007-08-08 帝人ファイバー株式会社 Melt spinning method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110983575A (en) * 2019-12-29 2020-04-10 江苏恒力化纤股份有限公司 Preparation method of oxford fabric

Also Published As

Publication number Publication date
KR100630266B1 (en) 2006-09-29

Similar Documents

Publication Publication Date Title
CN101139735A (en) Method for preparing ultra-fine denier polyester filament yarn
CN103437018A (en) Production technology of super simulation silk kam ammonia air-coated wire
CN102828266A (en) Terylene superfine flat yarn production method and product
JP2009133025A (en) Spinneret of thermoplastic modified cross-section fiber and method for producing thermoplastic modified cross-section fiber
CN104480555A (en) Production process of high-elasticity-feature terylene pre-oriented fibers
KR100630266B1 (en) Process for preparing multilobal fine denier polyester
CN1333119C (en) Fine-denier polyester hollow filament spinning method and its produced pilament
JP2004124338A (en) Method for producing hollow pre-oriented yarn of thin denier polyester and hollow pre-oriented yarn of thin denier polyester produced by the method
KR100523809B1 (en) Preparation of Polyester Fiber
CN116716670A (en) Polyester pre-oriented yarn for direct weaving and preparation method thereof
US6926854B2 (en) Process of making polyester fine denier multifilament
KR100682706B1 (en) Device and process for spinning flat polyester and flat polyester produced by same
KR101222201B1 (en) Process for preparing non-round cross-sectional polyester yarn
KR100404545B1 (en) Method for producing polyester superfine fiber
CN106245121B (en) A kind of porous spinneret of melting spinning filament
KR100649538B1 (en) Process for preparing non-round type cross-sectional polyester
CN106245122B (en) A kind of preparation method of porous polyester long filament
KR100468086B1 (en) Method for manufacturing fine denier polyester hollow pre-oriented yarn and the yarn manufactured from the same
KR101389737B1 (en) High-speed spinneret for high-hallow fiber having thick fineness and preparing method for the same
KR100412177B1 (en) The method of manufacturing a polyester microfiber
CN116732623B (en) Moisture-absorbing sweat-releasing polyester fiber and preparation method thereof
KR100231195B1 (en) Spinning spinneret device for fineness mono filament
TWI221487B (en) Method for manufacturing polyester fine denier multifilaments
CN117026400A (en) Preparation method of three-blade high-profile polyester drawn yarn
JP2004124339A (en) Method for producing two or more pre-oriented yarn of thin denier polyester and two or more pre-oriented yarn of thin denier polyester produced by the method

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20120619

Year of fee payment: 7

FPAY Annual fee payment

Payment date: 20130807

Year of fee payment: 8

FPAY Annual fee payment

Payment date: 20140805

Year of fee payment: 9

FPAY Annual fee payment

Payment date: 20150812

Year of fee payment: 10

FPAY Annual fee payment

Payment date: 20160817

Year of fee payment: 11

FPAY Annual fee payment

Payment date: 20180814

Year of fee payment: 13

FPAY Annual fee payment

Payment date: 20190813

Year of fee payment: 14