KR920003133B1 - Manufacturing process of polyamide multi filament yarn - Google Patents
Manufacturing process of polyamide multi filament yarn Download PDFInfo
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- KR920003133B1 KR920003133B1 KR1019890010087A KR890010087A KR920003133B1 KR 920003133 B1 KR920003133 B1 KR 920003133B1 KR 1019890010087 A KR1019890010087 A KR 1019890010087A KR 890010087 A KR890010087 A KR 890010087A KR 920003133 B1 KR920003133 B1 KR 920003133B1
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- yarn
- polyamide
- polymer
- polyamide multifilament
- temperature
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/08—Melt spinning methods
- D01D5/098—Melt spinning methods with simultaneous stretching
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/08—Melt spinning methods
- D01D5/084—Heating filaments, threads or the like, leaving the spinnerettes
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/12—Stretch-spinning methods
- D01D5/16—Stretch-spinning methods using rollers, or like mechanical devices, e.g. snubbing pins
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
- D01F6/60—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyamides
Abstract
Description
본 발명은 고속방사법에 의한 폴리아마이드 멀티필라멘트사의 제조방법에 관한 것으로서, 더욱 구체적으로는 폴리아마이드섬유 특유의 우수한 촉감을 가지며 경시변화에 따르는 염색반과 염색차를 일으키지 않으며 직물용 플렛트 얀으로 사용하기에 적합한 폴리아마이드 멀티필라멘트사의 제조방법에 관한 것이다.The present invention relates to a method for producing polyamide multifilament yarns by a high-speed spinning method, more specifically, to have a unique texture of polyamide fibers, and does not cause dyed spots and dyed teas with changes over time, and is used as a flat yarn for fabrics. It relates to a method for producing a polyamide multifilament yarn suitable for.
본 발명의 폴리아마이드 섬유는 폴리카프로아마이드, 또는 이것을 주성분으로 하는 공중합 폴리아마이드로 이루어진 것이다.The polyamide fibers of the present invention consist of polycaproamide or copolymerized polyamide having the main component thereof.
최근에 폴리아마이드를 고속방사함으로서 방사공정중에 우수한 분자쇄 배향을 갖도록 하는 제조방법이 알려져 있으며, 이러한 방법으로 제조된 멀티필라멘트를 연신가연기로 가공사를 제조하는 방법은 종래의 2,000m/분 전후의 방사속도로 권취한 후 연신하여 직물용 플렛트 얀을 제조하거나 연신사를 가연하여 가공사를 제조하는 방법에 비해 생산성의 극대화를 이룰 수 있다는 장점이 있다.Recently, a method of producing polyamides having high molecular chain orientation during the spinning process by high-speed spinning of polyamide is known, and a method of manufacturing a processed yarn using a drawing combustor using the multifilament prepared in this way is about 2,000 m / min. Winding after stretching at a speed, there is an advantage that the productivity can be maximized as compared to a method for producing a flat yarn for fabric or by twisting the drawn yarn to produce a processed yarn.
또한 결정화 속도가 매우 빠른 폴리아마이드를 사용하여 고속방사법으로 원사를 제조하게 되면 저속방사법으로 제조한 것에 비하여 연신공정을 거친 정도의 결정화 및 결정배향이 이루어진다.In addition, when the yarn is manufactured by a high-speed spinning method using polyamide having a very high crystallization rate, crystallization and crystallization of the degree that have undergone the stretching process are compared with those produced by the low-speed spinning method.
그러나 고속방사법에 의하여 결정화가 이루어진 고분자의 미세구조는 저속방사법에서와는 완전히 다른 특이한 결정구조를 갖게 되는데, 그것은 폴리아마이드 멀티필라멘트사의 미세구조가 폴리에스테르, 폴리에틸렌, 폴리프로필펜 등의 섬유고분자와는 다른 특수한 폴리모피즘(polymorphism)을 갖기 때문이다.However, the microstructure of the polymer crystallized by the high-speed spinning method has a unique crystal structure that is completely different from that of the low-speed spinning method. The microstructure of the polyamide multifilament yarn has a special structure that is different from that of polyester, polyethylene, and polypropylphene. This is because it has polymorphism.
보다 구체적으로 설명한다면, 폴리아마이드 섬유를 충분히 콘디션닝한 후 연신을 하거나 열처리를 해주면, 단사정계의 결정격자를 갖는 α형 결정과 고속방사때와 같이 충분한 레그 타임이 없이 배향이 이루어질 때 형성되는 의사육방정계의 결정격자를 갖는 γ형 결정을 주로 갖게 된다.More specifically, when the polyamide fiber is sufficiently conditioned and stretched or heat treated, the pseudo-form is formed when the alignment is performed without sufficient leg time, such as α-type crystal having monoclinic crystal lattice and high-speed spinning. It mainly has a γ-type crystal having a hexagonal crystal lattice.
그런데 고속방사법으로 제조된 폴리아마이드 멀티필라멘트 미연신사는 결정중에서 40% 이상이 γ형 결정으로 되어 있기 때문에 공기중의 수분을 흡수하게 되면 결정형태의 전이, 후결정화 및 복굴절의 변화등 경시변화가 심하게 된다.However, since polyamide multifilament unstretched yarn manufactured by high-speed spinning method has more than 40% of the crystals as γ-type crystals, when water in the air is absorbed, the change over time such as transition of crystal form, post-crystallization and birefringence change is severe. do.
그러므로 이와 같은 경시변화를 없게 하고 안정된 구조를 폴리아마이드 플렛트 얀을 제조하려면 가열판이 부착되어 있는 연시가연기로 처리하여야 하는 바 고속방사법으로 제조된 폴리아마이드 미연신사는 상술한 바와 같은 폴리머의 미세구조적인 특성때문에 연신성이 불량해진다.Therefore, in order to remove such a change over time and to produce a polyamide flat yarn with a stable structure, a polyamide flat yarn must be treated with a soft combustor attached with a heating plate. Due to its mechanical properties, the elongation is poor.
본 발명은 상술한 바와 같은 문제점을 해결한 것으로서 이하 상세히 설명하면 다음과 같다.The present invention solves the above problems as described in detail below.
본 발명은 방사속도 3,000m/min 이상 4,500m/min 이하의 고속방사법으로 폴리아마이드 멀티필라멘트의 미연신사(γ형 결정이 40% 이상)를 제조한 다음, 상기 미연신사를 연신시킬 때 연신직전에 폴리머의 2차전이온도(Tg℃) 보다 30℃ 이상 50℃이내에 있는 높은 온도의 물을 노즐을 통하여 사조에 0.1g/분 내지 0.2g/분 정도 분사시켜 주고, 이어서 폴리머의 2차 전이온도보다 30℃ 이상 100℃이내의 높은 온도를 갖는 열로울러에 통과시켜서 자연연신배율의 80%이상의 연신배율로 열연신시키는 폴리아마이드 멀티필라멘트사의 제조방법이다.The present invention is to produce a non-stretched yarn (γ-type crystal of 40% or more) of polyamide multifilament by a high-speed spinning method of more than 3,000m / min spinning rate 4,500m / min, and then immediately before stretching A high temperature water of 30 ° C. to 50 ° C. above the polymer's secondary transition temperature (Tg ° C.) is injected into the yarn through the nozzle at about 0.1 g / min to 0.2 g / min. It is a method for producing polyamide multifilament yarn which is passed through a heat roller having a high temperature of 30 ° C or more and 100 ° C and thermally drawn at a draw ratio of 80% or more of the natural draw ratio.
일반적으로 고속방사법으로 제조한 미연신사는 결정화도가 높고 응력신장곡선상에서 상온에서 변형을 가하면 자연연신배율 즉, 네킹(Necking)후 응력이 증가하지 않고 분자쇄배향만 일어나는 구간이 적어지고 분자쇄를 배향시킴에 따라 응력이 점점 크게 걸리는 스트레인하드닝(Strain Hardening)의 경향을 나타내므로 연신성이 불량해진다. 따라서 본 발명에서와 같이 열수처리를 행하면 폴리아마이드 미연신사가 연신될 때 사조에 묻은 폴리머의 2차 전이온도보다 30℃ 내지 50℃ 높은 물이 폴리머에 대하여 가소제역할을 하면서 분자쇄의 유동성을 증대시키므로 연신작업이 용이해지고 최종제품의 촉감을 부드럽게 해준다.In general, unstretched yarns manufactured by high-speed spinning method have high crystallinity and deformation at room temperature on the stress extension curve, thus reducing the natural stretch ratio, that is, the area where molecular chain orientation only occurs without increasing the stress after necking and orienting the molecular chain. As it exhibits a tendency of strain hardening (strain hardening), which is increasingly stressed, the elongation is poor. Therefore, when the hydrothermal treatment is carried out as in the present invention, when the polyamide undrawn yarn is stretched, water 30 ° C. to 50 ° C. higher than the secondary transition temperature of the polymer buried in the yarn increases the fluidity of the molecular chain while acting as a plasticizer for the polymer. Easily stretched and softens the feel of the final product.
아울러 상기한 폴리아마이드 미연신사를 폴리머와 2차 전이온도보다 30℃ 내지 100℃가 높은 열로울러에서 열연신하면 폴리머내의 불안정한 γ형 결정구조가 안정한 α형 결정구조로 바뀌므로 연신제사성이 양호해지고 후가공공정중 결점이 없는 직물용 플렛트 얀을 제조할 수 있게 된다.In addition, when the polyamide non-stretched yarn is thermally drawn in a polymer and a heat roller 30 to 100 ° C. higher than the secondary transition temperature, the unstable γ-type crystal structure in the polymer is changed into a stable α-type crystal structure, resulting in good drawability. It is possible to produce flawless flat yarns during the post-processing process.
아울러 본 발명으로 제조된 사는 열연신한 것이므로 냉연신한 것에 비하여 최종 제품에 부드러운 촉감을 부여한다.In addition, the yarn manufactured according to the present invention is hot drawn, thus imparting a soft touch to the final product as compared to cold drawn.
본 발명으로 제조된 폴리아마이드 멀티필라멘트사의 X선 회절법에 의한 미세구조는 다음과 같았으며 또 본 발명으로 제조된 폴리아마이드 멀티필라멘트사는 폴리아마이드섬유 특유의 우수한 촉감과 염색성을 발휘하였으며 직물용으로 매우 적합하였다.The microstructure of the polyamide multifilament yarn manufactured by the present invention was as follows, and the polyamide multifilament yarn produced by the present invention exhibited excellent touch and dyeing characteristics unique to polyamide fibers and was very useful for fabrics. Suited.
다 음next
· 결정영역(Xc) : 0.35 이상Crystal region (Xc): 0.35 or more
· 회절도형중 적도선상에 나타나는 α형 결정의 미결정의 크기 : 35Å-50ÅSize of microcrystal of α-form crystal appearing on the equator of diffraction diagram: 35Å-50Å
· 전체 결정영역중 α형 결정영역과 γ형 결정영역과의 비(α/γ) : 1.9-3.0Ratio (α / γ) of α-type crystal region and γ-type crystal region among all crystal regions: 1.9-3.0
α형 결정의 배향함수(fc) : 0.90이상Orientation Function (fc) of α-form Crystals: 0.90 or More
[실시예 1~6 및 비교예 1~3][Examples 1-6 and Comparative Examples 1-3]
상대점도 2.42인 나일론 6을 용융방사하고, 방사된 사조를 19℃, 0.45m/분의 냉각풍으로 냉각 고화시키고, 유제 공급장치로 에멀젼 상태의 유제를 공급하면서 3,500m/분, 4,000m/분, 4,200m/분의 속도로 권취하고, 뜨거운 수분(온도=폴리머의 Tg+30℃ ~ Tg+50℃)을 분사시켜 줄 수 있는 노즐제트와 열연신을 수행할 수 있는 뜨거운 로울러(온도=폴리머의 Tg+30℃ ~ Tg+100℃)가 부착된 연신기를 사용하여 자연연신 배율로 Tg+45℃ ~ Tg+65℃의 연신온도에서 연신하여 70데니아/24필라멘트의 연신사를 제조하였다.Melt spun nylon 6 with a relative viscosity of 2.42 and solidify the spun yarn with a cooling wind of 19 ° C. and 0.45 m / min, and supply emulsion in emulsion at 3,500 m / min and 4,000 m / min. , A nozzle jet that can be wound up at a speed of 4,200m / min, and sprays hot water (temperature = polymer Tg + 30 ℃ ~ Tg + 50 ℃) and hot roller that can perform thermal stretching (temperature = polymer Tg + 30 ° C. to Tg + 100 ° C.) was used to draw at a stretching temperature of Tg + 45 ° C. to Tg + 65 ° C. at a natural draw ratio to prepare a stretch yarn of 70 denia / 24 filaments.
그 결과는 표 1과 같다.The results are shown in Table 1.
[표 1]TABLE 1
(x : 불량, ○ : 양호, ◎ : 우수)(x: poor, ○: good, ◎: excellent)
본 발명의 실시예에서는 연신조업성이 양호하여서 제품결점이 적었으나, 비교예에서는 연신조업성이 매우 불량하여 보우 및 사절이 심하였으며 그 결과 원사물성의 불균일로 염반, 염차등 제품의 결함이 심각하였다.In the embodiment of the present invention, the drawability is good, there are few product defects, but in the comparative example, the drawability is very poor, and bowing and trimming are severe. It was.
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