KR100464457B1 - Manufacturing method of polyester low shrinkage water repellent - Google Patents

Manufacturing method of polyester low shrinkage water repellent Download PDF

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Publication number
KR100464457B1
KR100464457B1 KR1019980000976A KR19980000976A KR100464457B1 KR 100464457 B1 KR100464457 B1 KR 100464457B1 KR 1019980000976 A KR1019980000976 A KR 1019980000976A KR 19980000976 A KR19980000976 A KR 19980000976A KR 100464457 B1 KR100464457 B1 KR 100464457B1
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South Korea
Prior art keywords
water repellent
yarn
water
oven
high temperature
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KR1019980000976A
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Korean (ko)
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KR19990065606A (en
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김윤조
김효대
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주식회사 코오롱
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    • DTEXTILES; PAPER
    • D02YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02JFINISHING OR DRESSING OF FILAMENTS, YARNS, THREADS, CORDS, ROPES OR THE LIKE
    • D02J13/00Heating or cooling the yarn, thread, cord, rope, or the like, not specific to any one of the processes provided for in this subclass
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/62Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters
    • DTEXTILES; PAPER
    • D02YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02JFINISHING OR DRESSING OF FILAMENTS, YARNS, THREADS, CORDS, ROPES OR THE LIKE
    • D02J1/00Modifying the structure or properties resulting from a particular structure; Modifying, retaining, or restoring the physical form or cross-sectional shape, e.g. by use of dies or squeeze rollers
    • D02J1/22Stretching or tensioning, shrinking or relaxing, e.g. by use of overfeed and underfeed apparatus, or preventing stretch
    • D02J1/221Preliminary treatments
    • DTEXTILES; PAPER
    • D02YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02JFINISHING OR DRESSING OF FILAMENTS, YARNS, THREADS, CORDS, ROPES OR THE LIKE
    • D02J1/00Modifying the structure or properties resulting from a particular structure; Modifying, retaining, or restoring the physical form or cross-sectional shape, e.g. by use of dies or squeeze rollers
    • D02J1/22Stretching or tensioning, shrinking or relaxing, e.g. by use of overfeed and underfeed apparatus, or preventing stretch
    • D02J1/224Selection or control of the temperature during stretching
    • DTEXTILES; PAPER
    • D02YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02JFINISHING OR DRESSING OF FILAMENTS, YARNS, THREADS, CORDS, ROPES OR THE LIKE
    • D02J1/00Modifying the structure or properties resulting from a particular structure; Modifying, retaining, or restoring the physical form or cross-sectional shape, e.g. by use of dies or squeeze rollers
    • D02J1/22Stretching or tensioning, shrinking or relaxing, e.g. by use of overfeed and underfeed apparatus, or preventing stretch
    • D02J1/228Stretching in two or more steps, with or without intermediate steps
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2200/00Functionality of the treatment composition and/or properties imparted to the textile material
    • D06M2200/10Repellency against liquids
    • D06M2200/12Hydrophobic properties
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2401/00Physical properties
    • D10B2401/02Moisture-responsive characteristics
    • D10B2401/021Moisture-responsive characteristics hydrophobic

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

Abstract

본 발명은 폴리에스터 저수축 발수사의 제조방법에 관한 것으로, 본 발명의 제조방법은 미연신사를 횡연신법에 의해 연신중에 발수액을 도포하여 폴리에스터 발수사를 제조함에 있어서, 롤코터(RC)와 오일제트(OJ)를 사용하여 2단 연속적으로 발수액을 도포하는 것을 특징으로 하며 더불어 발수액이 도포된 사를 순간고온열처리수단(HA)으로 열처리하는 것을 또 다른 특징으로 하며, 이러한 특징의 본 방법을 이용하면 발수액이 균일하게 도포되고, 발수제의 고착이 강화되어 발수성능이 우수할 뿐만 아니라 그 편차도 거의 없으며 원사물성에 있어서도 수축율이 상당히 낮은 저수축 발수사의 제조가 가능하게 된다.The present invention relates to a method for producing a polyester low shrink water-repellent yarn, the manufacturing method of the present invention by applying a water-repellent liquid during the stretching of the unstretched yarn by the lateral stretch method, to produce a polyester water repellent yarn, roll coater (RC ) And the oil jet (OJ) is used to apply water repellent liquid in two stages in succession, and the heat-treated yarn is coated with instantaneous high temperature heat treatment means (HA). By using this method, the water repellent solution is uniformly applied and the adhesion of the water repellent agent is enhanced, so that the water repellent performance is excellent and there is almost no variation and the shrinkage rate in the raw material properties is very low. .

Description

폴리에스테르 저수축 발수사의 제조방법Manufacturing method of polyester low shrinkage water repellent

본 발명은 폴리에스터 사를 제조하기 위한 방법에 관한 것으로서, 보다 구체적으로는 내구성이 우수하고 발수성이 우수한 폴리에스테르 저수축 발수사를 제조하기 위한 방법에 관한 것이다.The present invention relates to a method for producing a polyester yarn, and more particularly to a method for producing a polyester low shrink water-repellent yarn excellent in durability and excellent water repellency.

기존의 발수사를 제조하는 방법에는 직접방사연신방식(Direct Spinning and Drawing: 이하 "DSD방식"이라 한다.) 및 미연신사를 횡연신시키는 횡연신 방식(Warp Drawing: 이하 "W/D방식" 이라 한다.) 등 크게 2가지로 분류할 수 있다.Conventional methods for producing water repellent yarns include direct spinning and drawing (hereinafter referred to as "DSD method") and lateral stretches to laterally stretch undrawn yarn (War drawing: "W / D method"). Can be classified into two types.

대체적으로 많이 사용되는 방법은 W/D방식이며, DSD 방식도 일부에서 적용하고 있다. W/D방식은 방사공정과 연신공정이 분리되어 있는데, 우선 미연신사를 제조후 이를 횡연신기에서 일정배율의 연신비 및 이완(relax)을 주어 원사를 제조하는 방식이다. The most commonly used method is the W / D method, and some of the DSD methods are also applied. In the W / D method, the spinning process and the stretching process are separated. First, undrawn yarn is manufactured, and then a yarn is manufactured by giving a draw ratio and relaxation of a certain ratio in a transverse stretching machine.

W/D 방식에서 발수제를 처리하는 방법으로는 1)미연신사 제조 공정에서 유제와 발수액을 도포시킨 후, 연신공정에서 열처리를 행하여 발수사를 제조하는 방법, 2)미연신사를 횡연신하는 공정에서 어느 특정 부위에서 롤러를 이용하여 발수액을 도포한 직후 열처리 장치를 거치면서 발수사를 제조하는 방법 등이 있다. Methods of treating the water repellent agent in the W / D method include 1) applying an emulsion and a water repellent liquid in the undrawn yarn manufacturing process, and then performing heat treatment in the stretching step to produce a water repellent yarn; 2) a process of transversely stretching the undrawn yarn. In the specific part, there is a method for producing a water repellent while passing through the heat treatment apparatus immediately after applying the water repellent using a roller.

종래의 DSD 방식으로 발수사를 제조하는 경우에는 유제와 발수사를 혼용하여 원사에 처리한 후, 연신공정 중에 고뎃롤러(G/R)에서 직접 열처리방식에 의하여 발수제를 원사에 고착시키기 때문에 G/R의 오염이 심하여 모우 발생, 잦은 절사등으로 작업성이 떨어진다. 또한 G/R과 직접적인 접촉이 이루어지지 않는 원사의 어느 특정 부위에서는 발수제의 고착이 불안정하여 후공정에서 발수제의 탈락, 발수성 부족 및 원사물성 불균일 등의 문제점이 발생하여 균일한 물성 획득이 어렵다. In the case of manufacturing a water repellent yarn by the conventional DSD method, the oil and water repellent yarn are mixed and treated to the yarn, and then the water repellent is fixed to the yarn by the direct heat treatment method in the stretching roller (G / R) during the stretching process. Due to the high pollution of R, workability is reduced due to the occurrence of cattle and frequent cutting. In addition, in certain parts of the yarn that are not in direct contact with the G / R, the seizure of the water repellent is unstable, resulting in problems such as dropping of the water repellent, lack of water repellency and non-uniformity of the yarn in the post-process, making it difficult to obtain uniform physical properties.

W/D 방식으로 발수사를 제조하는 방법에서 상기 방법 1)의 경우에는 미연신사를 G/R에서 연신하는 과정에서 DSD방식과 마찬가지로 G/R의 오염으로 인하여 모우발생등 원사의 외관을 손상시킬 수 있고, 상기 방법 2)의 경우에는 발수제의 부여가 불균일하며, 열고착이 불완전하여 발수제의 탈락 등을 유발시키므로 발수성능이 떨어진다.In the method of manufacturing a water-repellent yarn by the W / D method, in the case of the method 1), like the DSD method, in the process of stretching the unstretched yarn in the G / R, the appearance of the yarn may be damaged due to the contamination of G / R In the case of the method 2), the provision of the water repellent is non-uniform, and the heat repellent is incomplete and causes dropping of the water repellent, resulting in poor water repellency.

이와 같이 종래의 기술인 발수제와 유제를 혼용하여 발수사를 제조하는 DSD방식, 미연신사 제조과정 및 연신공정 중에 발수제를 부여한 후 비정촉열처리 방식에 의하여 발수사를 제조하는 W/D 방식에서는 조업성, 발수성 불균일 등의 문제점이 많아, 발수성능이 우수하며 균일한 발수성능을 발현하는 발수사의 제조방법에 대한 요구가 날로 증가하고 있다. As described above, the DSD method for manufacturing a water repellent by mixing a water repellent agent and an oil agent in the prior art, and the W / D method for manufacturing a water repellent agent by a non-tactile heat treatment method after imparting a water repellent agent during the non-stretched yarn manufacturing process and the stretching process, There are many problems such as non-uniformity of water repellency, and there is an increasing demand for a method for producing a water repellent which is excellent in water repellency and expresses uniform water repellency.

따라서 본 발명은 상기한 선행기술의 제반문제점을 감안하여 발수성이 우수하면서도 균일하고 수축성이 낮은 폴리에스테르 저수축 발수사를 제공하는 것을 과제로 한다.Accordingly, an object of the present invention is to provide a polyester low shrinkage water repellent yarn having excellent water repellency and low uniformity and shrinkage property in view of the above-mentioned problems of the prior art.

상기한 과제를 해결한 본 발명에 의하면 미연신사를 횡연신법에 의해 연신중에 발수액을 도포하여 폴리에스터 발수사를 제조하는 방법에 있어서, 롤코터와 오일제트를 사용하여 발수액을 도포하는 2단 연속적인 발수액 도포공정을 거친 후에 발수액이 도포된 사를 순간고온열처리수단으로 열처리하는 것을 특징으로 하는 폴리에스터 저수축 발수사의 제조방법이 제공된다.According to the present invention that solved the above problems, in the method of producing a polyester water repellent by applying a water repellent during stretching the undrawn yarn by the lateral stretching method, 2 to apply a water repellent using a roll coater and an oil jet However, there is provided a method for producing a polyester low shrinkage water repellent yarn, characterized in that the yarn to which the water repellent solution is applied is heat-treated with an instantaneous high temperature heat treatment means after a continuous water repellent solution application process.

이하, 본 발명을 도면을 참조하여 보다 상세하게 설명하기로 한다.Hereinafter, the present invention will be described in more detail with reference to the drawings.

본 발명의 개량된 구성은 연신사에 발수액을 균일하게 도포하기 위해 발수액 도포수단인 오일 제트와 롤코터로 2단 연속 도포한다는 것과, 내구성 향상으로 위해 이와 같이 발수제가 도포된 사를 순간적으로 고온열처리하는 것에 있다. The improved configuration of the present invention is to apply the water jet to the stretched yarn uniformly in two stages with the oil jet and the roll coater, which is a water repellent liquid application means, and to apply the water repellent agent instantaneously to improve the durability High temperature heat treatment.

본 발명의 바람직한 구현의 일예를 예시한 도 1에는 제3고뎃롤러(23)와 제3오븐(33) 사이에서 사에 발수제가 도포되며, 그 도포 순서가 오일제트(OJ) 다음에 롤코터(RC)의 순서로 도시된다. 그러나, 본발명은 이에 제한되지 않는 것으로서, 상기 발수액 도포는 역순으로 수행하여도 무방하고, 또한 상기 2단 연속적인 발수액 도포는 예를 들어 제2고뎃롤러(22)와 제1고온오븐(31) 사이에서 수행하여도 무방하다. In Figure 1 illustrating an example of a preferred embodiment of the present invention, a water repellent is applied between yarns between the third gourd roller 23 and the third oven 33, and the order of application is followed by the oil coat OJ followed by the roll coater ( RC is shown in the order. However, the present invention is not limited thereto, and the water repellent liquid application may be performed in the reverse order, and the two-stage continuous water repellent liquid application may be, for example, the second gourd roller 22 and the first high temperature oven ( 31) may be performed.

이와 같이 2단 연속적으로 발수제가 도포된 사는 고온의 오븐을 통과하여 비접촉식으로 열처리가 이루어져서 발수제의 고착이 이루어지나, 보다 바람직하게는 순간적으로 열처리를 거친 후 오븐을 통과시키는 것이 좋다. 이렇게 하면 발수제의 내구성이 증대된다. 순간적인 고온열처리수단(HA)의 바람직한 예로는 비활성기체 분사식 고온열처리수단이 있다. As described above, the yarn coated with the water repellent in two stages is passed through a high-temperature oven and heat-treated in a non-contact manner, so that the water-repellent is fixed. More preferably, after passing through the oven, it is preferable to pass through the oven. This increases the durability of the water repellent. A preferred example of the instantaneous high temperature heat treatment means HA is an inert gas injection type high temperature heat treatment means.

이러한 고온열처리수단(HA)의 온도는 150-350℃로 설정하는 것이 적당하다. 그 설치위치 및 설치대수는 발수액 도포수단과 고온오븐 사이에 1대 이상 설치하는 것이 적당하다. 이와 같이 순간적인 고온열처리를 상기 발수액 도포수단(OJ)(RC)과 고온오븐 사이에서 1회 이상 수행하여 열처리 효과를 강화시켜 주면 발수성과 수축성을 일층 향상시킬 수 있게 된다.The temperature of the high temperature heat treatment means HA is suitably set to 150-350 ° C. It is appropriate to install at least one of the installation position and the number of installations between the water repellent liquid applying means and the high temperature oven. As such, the instantaneous high temperature heat treatment may be performed at least once between the water repellent solution applying unit (OJ) RC and the high temperature oven to enhance the heat treatment effect, thereby further improving water repellency and shrinkage.

이와 같이 본 발명에 따라 2단연속으로 발수액을 도포하고 순간적인 고온열처리를 수행하게 되면 저수축성이 뛰어나고 물성의 편차가 없으며 발수성이 균일화고 발수성능이 우수한 폴리에스테르 저수축 발수사를 제조할 수 있게 된다.As described above, when the water-repellent solution is applied in two stages and the instantaneous high temperature heat treatment is performed, excellent low shrinkage property, no variation in physical properties, uniform water repellency, and excellent polyester water-repellent water repellency can be produced. Will be.

상술한 바와 같은 본 발명의 특징 및 기타의 장점은 후술되는 실시에로부터 보다 명백하게 될 것이다. 단 본발명은 하기 실시예에 한정되지 않는다.Features and other advantages of the present invention as described above will become more apparent from the following embodiments. However, the present invention is not limited to the following examples.

[실시예 1 내지 4, 6 및 비교예 1][Examples 1 to 4 and 6 and Comparative Example 1]

하기 표 1의 조건으로 방사하여 제조한 폴리에스테르 5400D/192fil의 미연신사를 크릴(10)에 공급한 후, 제1 G/R(21), 제2 G/R(22), 제1 고온오븐(31), 제2 고온오븐(32), 제3 G/R(23), 제3 고온오븐(33), 제4 고온오븐(34), 제4 G/R(24), 권취기(40)를 순차적으로 구비하되, 하기 표4에 나타낸 바와 같이 각 예에서 서로 다른 위치에 오일제트(OJ), 롤코터(RC), 순간 고온열처리수단(HA)가 설치된 횡연신 장치를 통해 연신하여 1000D/192fil의 발수사를 제조하였다. After the unstretched yarn of polyester 5400D / 192fil prepared by spinning under the conditions of Table 1 to the krill (10), the first G / R (21), the second G / R (22), the first high temperature oven (31), second high temperature oven (32), third G / R (23), third high temperature oven (33), fourth high temperature oven (34), fourth G / R (24), winder (40) ) Are sequentially provided, but as shown in Table 4 below, the oil jet (OJ), the roll coater (RC), and the instantaneous high temperature heat treatment means (HA) are drawn at different positions in each of the examples to draw 1000D. A water repellent yarn of / 192 fil was prepared.

각 예에서 발수액으로는 하기 표 2와 같이 조성된 동일한 수성 에멀젼을 사용하였고, 제1, 제2, 제3 및 제4 고뎃롤러의 속도 및 온도 그리고 제1, 제2, 제3 및 제4 고온오븐의 온도 및 통과속도를 또한 동일하게 하였다. 제조된 발수사의 특성은 하기 표 5에 제시된다.In each example, the same aqueous emulsion as shown in Table 2 was used as the water repellent liquid, and the speed and temperature of the first, second, third and fourth rollers and the first, second, third and fourth The temperature and passage speed of the hot oven were also the same. The properties of the prepared water repellent are shown in Table 5 below.

[실시예 5]Example 5

제4 G/R의 속도를 215 mpm으로 변경하고 제2HA를 설치하지 않은 것을 제외하고는 실시예 2와 동일한 절차를 반복하여 954D/192fil의 발수사를 제조하였다. 제조된 발수사의 특성은 하기 표5에 제시된다.A water repellent yarn of 954D / 192fil was prepared by repeating the same procedure as in Example 2 except changing the speed of the fourth G / R to 215 mpm and not installing 2HA. The properties of the prepared water repellent are shown in Table 5 below.

방 사 조 건Condition 폴리머칩의 고유점도(I.V.) Intrinsic Viscosity of Polymer Chip (I.V.) 1.01.0 DEG(에틸렌글리콜) DEG (ethylene glycol) 1.01.0 제 1 존히터(Zone-Heater #1) 온도 Zone-heater # 1 temperature 284℃284 ℃ 제 2 존히터(Zone-Heater #2) 온도 Zone-Heater # 2 Temperature 286℃286 ℃ 제 3 존히터(Zone-Heater #3) 온도 Zone-Heater # 3 Temperature 288℃288 ℃ 제 4 존히터(Zone-Heater #4) 온도 Zone-Heater # 4 Temperature 290℃290 ℃ 기어펌프(Gear Pump) 온도 Gear Pump Temperature 292℃292 ℃ 방사블럭(Spin Block) 온도 Spin Block Temperature 292℃292 ℃ ETR's 헤드(head) 압력 ETR's head pressure 2200 psi2200 psi

발 수 액 의 조 성Composition of Water Repellent 조 성 성 분Composition 함량 (중량%)Content (% by weight) 발수제 Water repellent 1212 아세트산 Acetic acid 0.20.2 이소프로필알코올 Isopropyl Alcohol 2.02.0  water 85.885.8

고뎃롤러(G/R)Gauze Roller (G / R) 조건(mpm/℃)Condition (mpm / ℃) 고온오븐High temperature oven 열풍온도 및 풍속(℃×m/sec)Hot air temperature and wind speed (℃ × m / sec) 제 1 G/R 1st G / R 38/11038/110 제 1 고온오븐1st high temperature oven 240×23240 × 23 제 2 G/R2nd G / R 155/120155/120 제 2 고온오븐2nd high temperature oven 250×23250 × 23 제 3 G/R3rd G / R 230/30230/30 제 3 고온오븐3rd high temperature oven 260×10260 × 10 제 4 G/R4th G / R 205/cold205 / cold 제 4 고온오븐4th high temperature oven 260×10260 × 10

구 분division 오일제트Oil jet 롤코터Roll coater 제1 HA1st HA 제2 HASecond HA 실시예 1Example 1 조건Condition 10 ℓ/hr10 ℓ / hr 20 mpm20 mpm 350℃350 ℃ -- 위치location 제 3G/R과 제3오븐 사이 Between 3G / R and 3rd oven 오일제트와 제3오븐 사이 Between oil jet and third oven 롤코터와 제3오븐 사이 Between the roll coater and the third oven 미설치Not installed 실시예 2Example 2 조건Condition 10 ℓ/hr10 ℓ / hr 20 mpm20 mpm 350℃350 ℃ 350℃350 ℃ 위치location 제3 G/R과 제3오븐 사이 Between 3rd G / R and 3rd oven 오일제트와 제3오븐 사이 Between oil jet and third oven 롤코터와 제3오븐 사이 Between the roll coater and the third oven 제3오븐과제4 G/R 사이Between 3rd oven and 4th G / R 실시예 3Example 3 조건Condition 10 ℓ/hr10 ℓ / hr 20 mpm20 mpm 350℃350 ℃ -- 위치location 제2 G/R과 제1오븐 사이 Between 2nd G / R and 1st oven 오일제트와 제1오븐 사이 Between oil jet and first oven 롤코터와 제1오븐 사이 Between the roll coater and the first oven 미설치Not installed 실시예 4Example 4 조건Condition 10 ℓ/hr10 ℓ / hr 20 mpm20 mpm 350℃350 ℃ 350℃350 ℃ 위치location 제2 G/R과 제1오븐 사이 Between 2nd G / R and 1st oven 오일제트와 제1오븐 사이 Between oil jet and first oven 롤코터와 제1오븐 사이 Between the roll coater and the first oven 제2 오븐과제3 G/R 사이Between 2nd oven and 3G / R 실시예 5Example 5 조건Condition 10 ℓ/hr10 ℓ / hr 20 mpm20 mpm 350℃350 ℃ -- 위치location 제3G/R과 제3오븐 사이 Between 3G / R and 3rd oven 오일제트와 제3오븐 사이 Between oil jet and third oven 롤코터와 제3오븐 사이 Between the roll coater and the third oven 미설치Not installed 실시예 6Example 6 조건Condition 10 ℓ/hr10 ℓ / hr 20 mpm20 mpm -- -- 위치location 제3 G/R과 제3오븐 사이 Between 3rd G / R and 3rd oven 오일제트와 제3오븐 사이 Between oil jet and third oven 미설치Not installed 미설치Not installed 비교예 1Comparative Example 1 조건Condition -- 20 mpm20 mpm -- -- 위치location 미설치Not installed 제3 G/R과 제3오븐 사이 Between 3rd G / R and 3rd oven 미설치Not installed 미설치Not installed

구 분division 강 도 (g/de)Strength (g / de) 파단신도(%)Elongation at Break (%) 발 수 성Water repellent 수축율*2(%)Shrinkage * 2 (%) 발수도*1(mm)Water repellency * 1 (mm) 표준편차Standard Deviation 실시예 1Example 1 7.737.73 25.125.1 1313 2.02.0 1.81.8 실시예 2Example 2 7.757.75 24.824.8 77 1.51.5 1.51.5 실시예 3Example 3 7.827.82 23.723.7 1717 2.52.5 1.91.9 실시예 4Example 4 7.737.73 24.224.2 99 1.91.9 1.61.6 실시예 5Example 5 7.817.81 22.522.5 77 2.12.1 2.32.3 실시예 6Example 6 7.707.70 25.025.0 4040 17 17 2.62.6 비교예 1Comparative Example 1 7.807.80 24.524.5 5252 14.314.3 2.62.6

*1) 발수도 측정 : 염료액에 원사를 침지시켜 수면에서 원사를 통하여 원사에 타고 올라온 염료의 높이로 측정. 염료액으로 0.5 중량% Miketon Blue FBL 수용액 사용.* 1) Water repellency: Measured by the height of the dye on the surface of the dye is immersed in the dye solution to the yarn through the yarn at the water surface. 0.5 wt% Miketon Blue FBL aqueous solution as dye solution.

*2) 수축률 측정 : 190℃ × 15 min, 무장력하에서 측정* 2) Shrinkage rate measurement: 190 ℃ × 15 min, measured under no tension

상기 표 5로부터 알 수 있는 바와 같이 본 발명에 따라 오일제트 및 롤코터를 거치면서 균일하게 발수액을 도포하고 순간적인 고온열처리를 수행하게 되면 발수제의 고착이 강화되어 발수성능이 우수할 뿐만 아니라 그 편차도 거의 없으며 원사물성에 있어서도 수축율이 상당히 낮은 저수축 발수사의 제조가 가능하게 된다.As can be seen from Table 5, when the oil jet and the roll coater are uniformly coated with the water repellent solution and the instantaneous high temperature heat treatment is carried out, the fixing of the water repellent is enhanced and the water repellent performance is not only excellent. There is little variation and it is possible to manufacture a low shrinkage water repellent yarn with a considerably low shrinkage in yarn properties.

도1은 본 발명의 바람직한 구현에 따라 발수사를 제조하는 공정을 개략적으로 나타낸 도면이다.1 is a view schematically showing a process for manufacturing a water repellent yarn according to a preferred embodiment of the present invention.

※ 도면중 주요부분의 부호 설명 ※※ Explanation of main parts in the drawing ※

10 … 미연신사 크릴(creel) 21 … 제 1 고뎃롤러군10... Unstretched creel 21. 1st roller roller group

22 … 제 2 고뎃롤러군 23 … 제 3 고뎃롤러군22. 2nd roller roller group 23. 3rd roller roller group

24 … 제 4 고뎃롤러군 31 … 제 1 고온오븐(hot oven)24. 4th roller roller group 31. First hot oven

32 … 제 2 고온오븐 33 … 제 3 고온오븐32. Second high temperature oven 33. 3rd high temperature oven

34 … 제 4 고온오븐 40 … 권취기34. Fourth high temperature oven 40. Winder

OJ … 오일제트 RC …롤코터OJ… Oil Jet RC. Roll coater

HA … 순간고온열처리수단HA… Instant high temperature heat treatment means

Claims (3)

미연신사를 횡연신법에 의해 연신중에 발수제를 부여하여 폴리에스터 발수사를 제조하는 방법에 있어서, 롤코터(RC)와 오일제트(OJ)를 사용하여 2단 연속적인 발수액을 도포하는 것을 특징으로 하는 폴리에스터 저수축 발수사의 제조방법.A method of producing a polyester water repellent yarn by applying a water repellent agent during stretching of an undrawn yarn by the lateral stretching method, wherein a two-stage continuous water repellent liquid is applied using a roll coater (RC) and an oil jet (OJ). Method for producing a polyester low shrinkage water repellent yarn. 제 1 항에 있어서, 발수액 도포후 순간고온열처리수단(HA)으로 열처리하는 것을 특징으로 하는 폴리에스터 저수축 발수사의 제조방법.The method for producing a polyester low shrinkage water repellent yarn according to claim 1, wherein the instantaneous high temperature heat treatment means (HA) is heat-treated after applying the water repellent solution. 제 2 항에 있어서, 상기 순간고온열처리수단(HA)의 온도가 150-350℃인 것을 특징으로 하는 폴리에스터 저수축 발수사의 제조방법.The method of claim 2, wherein the instantaneous high temperature heat treatment means (HA) has a temperature of 150-350 ° C.
KR1019980000976A 1998-01-15 1998-01-15 Manufacturing method of polyester low shrinkage water repellent KR100464457B1 (en)

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