KR100522898B1 - Manufacturing method of polyester polyaxial blended yarn - Google Patents

Abstract

The present invention relates to a method for manufacturing a polyester multi-axial blended yarn in which the difference in shrinkage is divided into four grades in a single process. As the regular chip is spun, the twin-shrink yarn is manufactured in the same spinning pack, and the yarns (A) and (B) are cooled, solidified and oiled, respectively, discharged from both spinning packs, and then the yarns (A) are stretched. Shrinkage rate between (A) and (B) by spontaneous stretching and winding of yarns (A) and (B) after acting as spontaneous extension and stretching yarn (B) by 1.1 to 2.5 times to act as potential shrinking yarn. The present invention relates to a method for producing mixed yarns having different grades of shrinkage in a single process by generating a difference. Therefore, the present invention polyester polyaxial blended yarn has a gloss difference without generating a gloss difference on the surface of the fabric and has an excellent touch with the expression of micro loops.

Description

Manufacturing method of polyester polyaxial blended yarn

The present invention relates to a method for manufacturing a polyester polyaxial horn fiber yarn in which the difference in shrinkage is divided into four grades in a single process, and in particular, it is possible to express a faint color without a gloss difference and no color difference due to dyed tea. A micro-loop (MICRO LOOP) is expressed in an effect yarn, and it is related with the manufacturing method of the polyester polyaxial mixed fiber which has the outstanding touch.

Conventionally, in Korean Laid-Open Patent Publication No. 97-62108 as a method of manufacturing a biaxial shrink yarn, cooling oiling of yarns (A) and (B) discharged from two spinning packs, and then yarn (A) is stretched between the rollers. It is known that a method of producing bishrinkage horned yarn is known by acting as a spontaneous extension yarn and stretching yarns between high rollers to act as potential shrinkage yarns and then entanglement and winding. In No. 97-74992, one yarn is heat treated with apostle and then focused on lubrication to make low-shrinkage yarn, and after the other one is stretched, it is focused on lubrication to obtain high-shrinkable yarn, and the winding tension of low-shrink yarn After the adjustment, the blending process is advanced and wound to obtain a biaxially blending blend. Both of these methods are a two-step process consisting of conventional spinning and blending yarns. Although it has the advantage of reducing the manufacturing cost by simplifying to a single process, it is generally a problem in the two-shrink blended yarn, which is caused by the color difference on the fabric due to the dyeing difference between the high and low shrinkers in processing, and the separation of the high and low shrinkers. It does not improve the gloss difference due to.

SUMMARY OF THE INVENTION An object of the present invention is to increase the difference in shrinkage rate of conventional bishrink blended yarns by two or more in manufacturing the blended yarns in a single process, thereby eliminating problems such as color difference and gloss difference in the conventional bishrink blended yarns, Expresses the loop to maximize the soft feeling.

According to the present invention, after cooling and solidifying oil yarns A and B discharged from both spinning packs, respectively, the yarn A is acted as a spontaneous extension without stretching, and yarn B is stretched. After acting as a potential shrinking yarn, the thread thread (A) and thread (B) are fluid-interlaced, but the high shrink yarn is external to the inside of each detention of the thread (A) and thread (B).

Since the regular yarn is to be radiated to have a different rate of shrinkage of four different grades in a single process to produce the multi-axial blended yarn of the present invention.

When described in detail below with reference to the drawings.

Figure 1 shows the yarn composition of the detention, drying and melting the high shrink chip and regular chip, respectively, and distributed in the distributor (DISTRIBUTER) in the same detention finally to the high shrink yarn inside the detention, the regular yarn out of the detention do. At this time, the high shrinkage yarn is a copolymer-modified polyethylene terephthalate fiber, and as copolymerization modifier, isophthalic acid as an acid component, neopentyl glycol as a glycol component, 2-2 'bis [4- (2hydroxyethoxy) phenyl] propane, etc. can be used. Mixed use. The copolymerization ratio is added in the range of 3 to 7 mol% based on the total monomer components, respectively. If it is less than 3.0 mol%, the shrinkage effect of the yarn is not sufficient, and if it is more than 7 mol%, there is a concern that a trouble occurs during spinning, and the physical properties of the yarn are severely deteriorated, which is not preferable.

2 is a schematic view of the process of the present invention, spinning at a spinning speed of 2000 to 4000 and cooling solidified and oiling the yarns (A) and (B) discharged from both spinning packs, respectively. By passing through the second high roller, it is not stretched and acts as spontaneous extension. The yarn (B) is stretched 1.1 to 2.5 times between the first high roller and the second high roller to increase the molecular orientation, thereby increasing the contraction rate to increase the potential shrinkage. It acts as a yarn. At this time, the temperature of the first gourd roller is 50 to 150 ° C. After the yarns (A) and (B) by using a fluid interlocking device having a number of entangled 30 to 100 / m and then wound to prepare a blended yarn in a single process.

3 is a model diagram when the blended yarn manufactured by the above method is subjected to heat treatment, the drawing yarn acts as a screening and the undrawn yarn acts as a super yarn. Each of the screening and the yarn is also composed of high shrink yarn and regular yarn. Due to the difference in the shrinkage rate of the micro-loop is expressed. Therefore, when it is made of fabric, it can show natural and luxurious surface effect on the fabric which was not expressed by the conventional di-shrink blended yarn by the difference in dyeing ratio of each yarn, and improve the gloss difference due to the separation of high and low shrink yarn. It is possible to produce a fabric having an excellent touch due to the appearance of micro loops.

Hereinafter, the present invention will be described in detail with reference to Examples.

Example 1

The high shrinkage yarns spun inside each of A and B prisons are composed mainly of terephthalic acid and ethylene glycol, and isophthalic acid as copolymerization modifier is 5 mol% of the total acid component, 2-2'bis [4- (2hydroxyethoxy ) Phenyl] Propane is copolymerized with 5 mol% of all glycol components. Copolymer polyester chip with 0.65 intrinsic viscosity is used. Regular chip is used outside the cap, and 12 strands are high shrink yarns in the same mold and the other 12 strands are regular polyethylene tere. Allow to be spun by phthalate.

Spinning temperature is 285 ℃ and the first gourd roller temperature is 90 ° C. In case of thread B, it is drawn twice between the first gourd roller and the second gourd roller and the winding speed is 3000M / MIN. Was interwoven with 3 kg / cm 2 compressed air using a fluid interlocking device to obtain a blended yarn with 80 interlocking water / M.

The silk blend fabric was manufactured by a conventional method after sizing the prepared horn fiber.

Comparative Example 1

Except for producing yarns of 50 denier and 24 filaments by spinning regular yarns in each of A and B molds, the same as in Example 1 except that the finished fabric is soft and dyed. , Matteness, bulkiness, etc. were evaluated by sensory test. In the sensory evaluation, 10 subjects were evaluated by fabric, and the subjective evaluation results of each individual were classified into 3 grades of good: 8 or more, normal: 4-7, and poor: 3 or less. When the comparative evaluation of the product of the Example and Comparative Example manufactured under the above conditions are as follows.

division Softness Dyed lines Matte Bulky castle Example 1 Great Great Great Great Comparative Example 1 Great Bad Bad usually

From the above results, it can be seen that the generation of dyed lines, glossiness, and the like, which are a problem in general biaxially horned fiber manufactured in a single process, are improved in the case of the multiaxial horned fiber according to the present invention.

The present invention does not produce a gloss difference on the surface of the fabric due to the separation of the high shrink yarn and low shrink yarn, and because the components of the multiple axis offset the color difference due to the difference in dyeing, it is possible to express a subtle color and even in the effect yarn The micro loops are expressed and have an excellent touch.

1 is a cross-sectional view of the detention used in the present invention,

2 is a manufacturing process schematic diagram of the present invention;

3 is a model diagram when the horn fiber manufactured by the present invention is heat treated.

<Explanation of symbols for main parts of drawing>

1: inside of detention 2: outside of detention

3: spinning pack A 4: spinning pack B

5: oil ring device 6: guide roller

7: 1st goth roller 8: 2nd goth roller

9: fluid communication device 10: regular yarn of unstretched yarn (A)

11: high shrinkage yarn of undrawn yarn (A) 12: regular yarn of undrawn yarn (B)

13. High Shrinkage of Stretched Yarn (B)

Claims (1)

After cooling and solidifying each thread (A) and (B) discharged from both spin packs, the thread (A) acts as a spontaneous extension without stretching and the thread (B) is 1.1 to 2.5 times longer. In the method for producing a biaxial blended yarn in which the thread yarns (A) and (B) are fluidly entangled and wound up so as to act as latent shrinkable yarns, Inside the cages of the yarns (A) and (B), terephthalic acid and ethylene glycol are the main components, and isoprophthalic acid is 3-7 mol% of the total acid component and 2-2'bis [4- (2 hydride) as a copolymerization modifier. Roxy ethoxy) phenyl] propane copolymerized 3-7 mol% of all glycol components is spun into high shrink yarns, the outside is a regular yarn to be spun to have a different shrinkage of 4 grades in a single process Method for producing polyester polyaxial blended yarn.