THE DIFFERENT SHRINKAGE COMPOSITE YARN AND ITS PREPARATION METHOD

Abstract

A different shrinkage composite yarn and preparation method. The modified polyester is spun with a porous spinneret to produce a different shrinkage composite yarn, and the spinneret holes on the porous spinneret are arranged in an elliptical arrangement. The different shrinkage composite yarn is obtained by winding modified polyester POY yarn and FDY yarn, network recombining, and coiling them. The preparation method of modified polyester is as follows: terephthalic acid reacts with ethylene glycol to produce ethylene terephthalate. The modified polyester is obtained by the reaction of terephthalic acid with branched diol. The fiber of the invention has good properties and the deviation rate of fiber density. The CV value of breaking strength is 4.0%, the CV value of elongation at break is 8.0%, the CV value of coefficient of variation of coiling shrinkage is 8.0%.

Claims

1. A different shrinkage composite yarn, comprising a modified polyester, and the modified polyester is composed of a terephthalic acid chain, an ethylene glycol chain and a diol chain containing a branched chain; a size of the different shrinkage composite yarn is 100-150 dtex; a breaking strength is 1.9 CN/dtex, an elongation at break is 30.05.0; at a temperature of 80 C.-130 C., a space gap between molecular chains in the modified polyester increases by 10-30 v/v %; a deviation rate of fiber density of the different shrinkage composite yarn is 2.0%; a CV value of breaking strength is 4.0%, and a CV value of elongation at break is 8.0%, and a CV value of coiling shrinkage coefficient of variation is 8.0%, and crimp shrinkage is 3.502.0%, and an oil content is 1.00.2%, network degree is 205 units/m; wherein, the increase of the space gap between the molecular chains refers to a comparison of the spatial gaps between molecular chains at a same temperature between the modified polyester and a common polyester; the branched diol is one or more items selected from the group consisting of a 2-pentyl-1,3 propanediol, a 2-hexyl-1,3 propanediol, a 2-heptyl-1,3 propanediol, a 2-octyl-1,3 propanediol, a 2-mercapto-1,3 propanediol, a 2-mercapto group-1,3 propanediol, a 2-pentyl-1,4 butanediol, a 2-hexyl-1,4 butanediol, a 2-heptyl-1,4 butanediol, a 2-octyl-1,4 butanediol, a 2-mercapto-1,4 butanediol, a 2-mercapto-1,4 butanediol, a 2-pentyl-1,5 pentanediol, a 2-hexyl-1,5-pentanediol, a 2-heptyl-1,5-pentanediol, a 2-octyl-1,5-pentanediol, a 2-mercapto group-1.5 pentanediol glycol, a 2-mercapto-1,5 pentanediol, a 2-pentyl-1,6 hexanediol segment, a 2-hexyl-1,6 hexanediol, a 2-heptyl-1,6-hexanediol, a 2-octyl-1,6-hexanediol, a 2-mercapto-1,6-hexanediol and a 2-mercapto-1,6 hexanediol.

2. A method of preparing the different shrinkage composite yarn of claim 1, wherein the modified polyester is spun from a porous spinneret to produce the different shrinkage composite yarn, and an arrangement of spinneret holes in the porous spinneret is an elliptical arrangement; the elliptical arrangement means that the centers of the spinning holes of the spinneret are located on the concentric ellipses, the concentric ellipses are a series of ellipses, the long axes of all the ellipses are collinear, and the short axes of all the ellipses are collinear; the method comprising: preparing a modified polyester POY yarn by metering, squeezing, cooling, oiling and winding the modified polyester, and preparing a modified polyester FDY yarn by metering, extrusion, cooling, oiling, drawing, heat setting and winding the modified polyester chips; combining the modified polyester POY yarn and the modified polyester FDY yarn as a network structure to form the different shrinkage composite yarn; wherein, a method for preparing the modified polyester comprises (1) preparation of terephthalic acid glycol ester: mixing terephthalic acid and the branched hexanediol to a first slurry, and carrying out a first esterification reaction under a catalytic action of concentrated sulfuric acid to obtain the terephthalic acid glycol ester; (2) preparation of ethylene terephthalate: mixing the terephthalic acid and ethylene glycol to a second slurry, carrying out a second esterification reaction to obtain the ethylene terephthalate; (3) preparation of modified polyester: after the second esterification reaction in the step (2) is completed, adding the terephthalic acid glycol ester prepared in the step (1), stirring and mixing, performing a polycondensation reaction under the action of the catalyst and the stabilizer, and under a condition of a negative pressure; first in a low vacuum stage and then in a high vacuum stage to obtain the modified polyester.

3. The method of claim 2, wherein, in the method for preparing the modified polyester the first slurry in the step (1) is added to a first reactor for carrying out the first esterification reaction; the first esterification reaction is carried out under a pressurized nitrogen environment, and the pressure is in a range of a normal pressure to 0.3 MPa, and a temperature is 180-240 C.; the first esterification reaction ends when a water distillation amount in the first esterification reaction reaches at least 90% of a first theoretical value: than that then the terephthalic acid glycol ester is obtained; the second slurry in the stet (2) is added into a second reactor for carrying out the second esterification reaction; the second esterification reaction is carried out under a pressurized nitrogen environment, and the pressure is in a range of normal pressure to 0.3 MPa, and a temperature is 250-260 C.; the second esterification reaction ends when a water distillation amount in the second esterification reaction reaches at least 90% of a second theoretic; then the ethylene terephthalate is obtained; in step (3) the stirring and mixing is performed for 15-20 minutes under the action of the catalyst and the stabilizer, and negative pressure; in the polycondensation reaction under the condition of the low-vacuum stage, the pressure is smoothly pumped from the normal pressure to an absolute pressure under 500 Pa, a temperature is controlled at the temperature of 260-270 C., and a reaction time is 30-50 minutes; then turn to the high vacuum stage, the polycondensation reaction continues and the reaction pressure is reduced to an absolute pressure of less than 100 Pa, and the reaction temperature is controlled at 275 to 280 C., and the reaction time is 50 to 90 minutes in order to obtain the modified polyester; the main spinning process parameters of the different shrinkage composite yarn are as follows: a spinning temperature is 280-300 C.; a wind temperature is 20-22 C.; a network pressure of joint stock is 3.5-4.5 bar. GR1 speed is 800-1000 m/min; SR1 speed is 3000-4200 m/min: GR2 speed is 3000-4000 m/min; HT1 temperature is 90-115 C.; HT2 temperature is 130-140 C.; winding speed is 3000-4000 m/min.

4. The method of claim 2, wherein, in the method for preparing the modified polyester: in step (1), a molar ratio of the terephthalic acid to the branched diol is 1: 1.3-1.5; an amount of concentrated sulfuric acid added is 0.3-0.5% of a weight of terephthalic acid; a concentration of concentrated sulfuric acid is 50-60 wt %; in step (2), a molar ratio of the terephthalic acid to the ethylene glycol is 1: 1.2-2.0; in step (3), a molar percentage value of the diol terephthalate and the ethylene terephthalate is 2-5%; the catalyst is antimony trioxide, antimony glycol or antimony acetate, and an amount of catalyst added ranges from 0.01%-0.05% of a total weight of terephthalic acid; the stabilizer is triphenyl phosphate, trimethyl phosphate or trimethyl phosphite, and an amount of stabilizer added ranges from 0.01%-0.05% of the total weight of terephthalic acid; a number average molecular weight of the modified polyester ranges from 15000-30000.

5. (canceled)

6. The method of claim 2, wherein the spinneret holes are arranged symmetrically along the long axes and/or the short axes of the concentric ellipses.

7. The method of claim 2, wherein a ratio of a length of the long axis of the ellipse to a length of the short axis is 1.3-1.8; a spacing of the adjacent spinneret holes is greater than a diameter of the guide hole of the spinneret hole plus 1.5 mm.

8. The method of claim 2, wherein the spinneret is a circular spinneret or an elliptical spinneret; a difference between a diameter of the circular spinneret and a maximum length of the long axis of the series ellipse is greater than 10 mm, and a difference value between the elliptical spinneret and the maximum length of the long axis of the series ellipse is greater than 10 mm.

9. The method of claim 2, wherein a guide hole diameter of the spinneret is 1.5-2.5 mm; a number of spinneret holes is greater than or equal to 192.

10. The method of claim 2, wherein the cross-section shape of the spinneret spinning hole is a circle, square, diamond, linear shape, triangle, trilobal shape, hollow type or flat type.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0062] FIG. 1 is an elliptical arrangement of 374 spinneret holes with an aperture of 2.0 mm and a length ratio of 1.3 mm between the long axis and the short axis of the ellipse;

[0063] FIG. 2 is a circular arrangement of 370 spinneret holes with an aperture of 2.0 mm;

[0064] FIG. 3 shows the elliptical arrangement of 382 spinneret holes with an aperture of 2.0 mm and a length ratio of 1.6 for the long and short axes of the ellipse.

DETAILED DESCRIPTION OF THE EMBODIMENTS

[0065] Hereinafter, the present invention will be described in more detail by the following examples. It should be noticed that these examples are only for illustrating the present invention and are not intended to limit the scope of the present invention. In addition, it should be noticed that after reading the content of the present invention, those skilled in this field can make various modifications or changes to the present invention, and these equivalent forms also apply to the scope of the appended Claims of this application.

Examples 128

[0066] A preparation method of a modified polyester, including the following steps:

[0067] (1) Preparation of Terephthalic Acid Glycol Esters:

[0068] Add the terephthalic acid and B at a molar ratio of A as a mixture into the reactor at a concentration of Cwt %, and the amount added is D % by weight of terephthalic acid. Under the catalysis of sulfuric acid, the esterification reaction is carried out. The esterification reaction is pressurized to E MPa under a nitrogen environment, the pressure is normal pressure, the temperature is F C. The esterification reaction ends until the water distillation amount in the esterification reaction reaches G % of the theoretical value, and the terephthalic acid glycol ester is obtained.

[0069] (2) Preparation of Ethylene Terephthalate:

[0070] The terephthalic acid and ethylene glycol having a molar ratio of H are mixed into the reactor, and then the esterification reaction is carried out. The esterification reaction is pressurized to I MPa under a nitrogen environment, and a temperature of F C. When the water distillation amount in the esterification reaction reaches K % of the theoretical value, the esterification reaction ends, and ethylene terephthalate is obtained:

[0071] (3) Preparation of Modified Polyester:

[0072] Add the terephthalate diol phthalate ester diol prepared in step (1) after completion of the esterification reaction in step (2). The molar percentage of terephthalate diol phthalate ester diol and ethylene glycol terephthalate is of L %. Stir and mix for M minutes. Add N % of O as catalyst in a total amount of terephthalic acid and P % of Q as stabilizer in a total amount of terephthalic acid. The polycondensation reaction in the low vacuum phase is started under the condition of negative pressure. The pressure is smoothly pumped from atmospheric pressure to an absolute pressure of R Pa, the temperature is controlled at S C., and the reaction time is T minutes, then the vacuum is continued for the high vacuum phase. The polycondensation reaction is carried out to reduce the reaction pressure to an absolute pressure of U Pa, the reaction temperature is controlled at V C., and the reaction time is W minutes. Then we can obtain the modified polyester.

[0073] The modified polyester obtained has a number average molecular weight of X and consists of terephthalic acid segment, ethylene glycol segment and branched B segment. The molar percentage of branched B segment and the ethylene glycol segment is Y %.

[0074] The parameters of the variation in the different examples are shown in the following table. In the table, BA stands for 2-pentyl-1,3 propanediol, BB stands for 2-hexyl-1,3 propanediol, and BC stands for 2-Heptyl-1,3 propanediol, BD stands for 2-octyl-1,3 propanediol, BE stands for 2-mercapto-1,3 propanediol, and BF stands for 2-mercapto-1. 3 propylene glycol, BG stands for 2-pentyl-1,4 butanediol, BH stands for 2-hexyl-1,4 butanediol, and BI stands for 2-heptyl-1,4 The diol, BJ stands for 2-octyl-1,4 butanediol, BK stands for 2-mercapto-1,4 butanediol, and BL stands for 2-mercapto-1,4 Butanediol, BM stands for 2-pentyl-1,5-pentanediol, BN stands for 2-hexyl-1,5-pentanediol, and BO stands for 2-heptyl-1,5 Pentyl glycol, BP stands for 2-octyl-1,5 pentanediol, BQ stands for 2-mercapto-1,5 pentanediol, and BR stands for 2-mercapto-1. 5 pentanediol, BS represents 2-pentyl-1,6 hexanediol, BT represents 2-hexyl-1, 6 hexanediol, and BU represents 2-heptyl-1, 6 hexanediol, BV stands for 2-octyl-1,6 hexanediol, BW stands for 2-mercapto-1, 6-hexanediol, BX represents 2-mercapto-1,6-hexanediol, OA stands for antimony trioxide, OB stands for ethylene glycol, and OC stands for Barium acetate, QA stands for triphenyl phosphate, QB stands for trimethyl phosphate, and QC stands for trimethyl phosphite, and the ratio is molar ratio.

TABLE-US-00001 parameters of the variation in the different examples EXAMPLE A B C D E F G H I J K L M 1 1:1.3 BA 50 0.3 0.1 180 90 1:1.2 0.1 250 90 2 15 2 1:1.38 BB 55 0.32 0.13 181 91 1:1.3 0.12 251 91 2.1 16 3 1:1.33 BC 55 0.33 0.12 183 92 1:1.31 0.31 252 92 2.2 16 4 1:1.34 BD 60 0.34 0.13 184 93 1:1.32 0.33 253 93 2.3 17 5 1:1.35 BE 55 0.36 0.14 185 93.2 1:1.33 0.14 254 93.2 2.4 17 6 1:1.36 BF 50 0.37 0.15 186 93.3 1:1.34 0.15 255 93.3 2.5 18 7 1:1.37 BG 60 0.38 0.16 187 93.4 1:1.36 0.16 256 93.4 2.6 19 8 1:1.38 BH 55 0.39 0.17 188 93.5 1:1.37 0.17 257 93.5 2.7 19 9 1:1.39 BI 50 0.4 0.17 188 93.5 1:1.37 0.17 257 93.5 2.8 16 10 1:1.4 BJ 55 0.4 0.17 188 93.5 1:1.38 0.18 257.8 93.6 3 17 11 1:1.4 BK 55 0.4 0.18 189 93.6 1:1.39 0.19 258.8 94 4 18 12 1:1.4 BL 55 0.4 0.2 200 94 1:1.6 0.2 256 94 4.5 18 13 1:1.5 BM 60 0.5 0.3 240 92 1:2.0 0.3 260 92 5 20 14 1:1.47 BN 60 0.47 0.28 220 92 1:1.8 0.27 258 92 4 18 15 1:1.46 BO 60 0.49 0.28 233 92 1:1.8 0.28 259 92 4.5 19 16 1:1.49 BP 60 0.48 0.28 230 92 1:1.8 0.28 258 92 4.7 19 17 1:1.467 BQ 60 0.47 0.27 236 92 1:1.89 0.28 258 92 4.3 18 18 1:1.48 BR 55 0.46 0.28 230 92 1:1.88 0.28 256 92 4.7 18 19 1:1.46 BS 55 0.47 0.28 238 92 1:1.9 0.28 259 92 4.7 19 20 1:1.46 BT 60 0.46 0.26 221 92 1:1.89 0.25 259 92 4.1 18 21 1:1.43 BU 60 0.47 0.27 235 92 1:1.78 0.26 255 92 4.3 17 22 1:1.43 BV 55 0.45 0.29 235 92 1:1.87 0.27 255 92 4.6 18 23 1:1.457 BW 55 0.46 0.28 239 92 1:1.81 0.27 255 92 4.41 19 24 1:1.47 BX 55 0.48 0.27 245 92 1:1.81 0.27 259 92 4.67 19 25 1:1.45 BW + 55 0.49 0.26 236 92 1:1.8 0.28 258 92 4.4 18 BG (3:1) 26 1:1.45 BO + 60 0.45 0.28 239 92 1:1.84 0.29 255 92 4.6 18 BX (3:2) 27 1:1.45 BW + 55 0.49 0.26 236 96 1:18 0.28 258 92 4.4 18 BG (3:1) 28 1:1.45 BD + 60 0.47 0.29 235 92 1:18 0.27 258 92 4.71 18 BG + BQ (3:2:1) EXAMPLE N O P Q R S T U V W X Y 1 0.01 OA 0.01 QA 500 260 30 100 275 50 15000 2 2 0.011 OA 0.02 QA 490 262 31 99 276 51 16000 2.1 3 0.03 OA 0.02 QA 498 263 32 80 277 57 15900 2.2 4 0.033 OA 0.023 QA 497 264 33 80 278 58 15800 2.3 5 0.034 OA 0.024 QA 496 265 34 70 277 59 15900 2.4 6 0.035 OA 0.025 QA 495 266 35 70 278 60 16000 2.5 7 0.036 OA 0.025 QA 496 267 36 70 278 61 16000 2.6 8 0.036 OA 0.025 QA 496 267 36 60 278 61 17000 2.7 9 0.04 OB 0.026 QB 497 268 38 50 279 62 18000 2.8 10 0.03 OB 0.027 QB 498 269 39 50 278 64 19000 3 11 0.04 OB 0.03 QB 497 260 40 40 277 63 20000 4 12 0.038 OC 0.03 QC 497 265 42 40 277 70 26000 4 13 0.05 OC 0.05 QC 450 270 50 30 280 90 30000 5 14 0.04 OB 0.04 QB 460 263 47 40 278 85 28000 4 15 0.044 OA 0.046 QA 490 269 48 40 279 87 29000 4.5 16 0.048 OB 0.047 QA 460 267 48 40 279 83 27000 4.7 17 0.04 OA 0.041 QC 490 268 48 40 278 85 29000 4.3 18 0.047 OA 0.047 QA 480 265 47 40 279 85 28000 4.7 19 0.046 OC 0.048 QC 446 267 49 40 278 87 29000 4.7 20 0.041 OB 0.042 QB 460 265 47 40 278 85 28000 4.1 21 0.043 OA 0.049 QA 490 268 46 40 275 85 28000 4.3 22 0.047 OB 0.04 QA 470 268 45 40 279 83 29000 4.6 23 0.042 OA 0.048 QC 495 265 45 50 275 85 28000 4.41 24 0.041 OA 0.042 QA 485 268 46 50 275 89 29000 4.67 25 0.042 OA 0.047 QC 495 265 49 50 278 88 29000 4.4 26 0.0423 OA 0.045 QC 495 265 45 50 278 85 28000 4.6 27 0.042 OA 0.047 QC 495 265 49 50 278 88 29000 4.4 28 0.04 OA 0.041 QC 490 268 49 50 277 84 29000 4.71

Example 29

[0075] The invention relates to a preparation method of different shrinkage composite yarn, which is made from a porous spinneret. The arrangement of holes on the spinneret is elliptical, which means that the spinning hole center of the spinneret is located on a concentric ellipse. Concentric ellipse is a series of ellipses, all ellipses of the long axis collinear, and short axis collinear.

[0076] As shown in FIG. 1, the ratio of the length of the long axis to the short axis of the ellipse is 1.3, the spacing of the adjacent spinneret is equal to the diameter of the guide hole of the spinneret plus 1.5 mm, and the spinneret is a circular spinneret. The difference between the diameter of the circular spinneret and the maximum length of the long axis of the series is 11 mm, the diameter of the spinneret is 2.0 mm, the number of spinneret holes is 374, and the cross section shape of the spinneret spinning hole is circle.

[0077] The modified polyester POY yarn is prepared by metering, squeezing, cooling, oiling and winding the modified polyester prepared in EXAMPLE 1, and the modified polyester FDY yarn is prepared by metering, extrusion, cooling, oiling, drawing, heat setting and winding the modified polyester chips. The modified polyester POY yarn and the modified polyester FDY yarn are combined as the network structure to form the different shrinkage composite yarn. The main spinning process parameters are: spinning temperature 280 C., wind temperature 20 C., combined network pressure 3.5 bar, GR1 speed 1000 m/min, SR1 speed 4000 m/min, GR2 speed 3000 m/min, HT1 temperature 100 C., HT2 temperature 130 C., winding speed 3000 m/min.

[0078] The size of the different shrinkage composite yarn is 120 tex, and the breaking strength of the yarn is 2.7 cN/dtex, the elongation at break is 30.7%, and the curling shrinkage rate is 4.53%, and network degree is 25 units/m. At the temperature of 80 C., the space gap between molecular chains of the different shrinkage composite yarn is increased by 15 v/v %. The fiber density deviation rate is 1.7%, the CV value of the breaking strength is 3.2%, the CV value of elongation at break is 6.9%, the CV value of coiling shrinkage variation coefficient is 7.2% and the oil content is 1.0%.

Example 30

[0079] The invention relates to a preparation method of different shrinkage composite yarn, which is made from a porous spinneret. The arrangement of holes on the spinneret is elliptical, which means that the spinning hole center of the spinneret is located on a concentric ellipse. Concentric ellipse is a series of ellipses, all ellipses of the long axis collinear, and short axis collinear.

[0080] As shown in FIG. 3, the ratio of the length of the long axis to the short axis of the ellipse is 1.6, the spacing of the adjacent spinneret is equal to the diameter of the guide hole of the spinneret plus 1.5 mm, and the spinneret is a circular spinneret. The difference between the diameter of the circular spinneret and the maximum length of the long axis of the series is 11 mm, the diameter of the spinneret is 2.0 mm, the number of spinneret holes is 382, and the cross section shape of the spinneret spinning hole is circle.

[0081] The modified polyester POY yarn is prepared by metering, squeezing, cooling, oiling and winding the modified polyester prepared in EXAMPLE 1, and the modified polyester FDY yarn is prepared by metering, extrusion, cooling, oiling, drawing, heat setting and winding the modified polyester chips. The modified polyester POY yarn and the modified polyester FDY yarn are combined as the network structure to form the different shrinkage composite yarn. The main spinning process parameters are: spinning temperature 280 C., wind temperature 20 C., combined network pressure 3.5 bar, GR1 speed 1000 m/min, SR1 speed 4000 m/min, GR2 speed 3000 m/min, HT1 temperature 100 C., HT2 temperature 130 C., winding speed 3000 m/min.

[0082] The size of the different shrinkage composite yarn is 100 tex, and the breaking strength of the yarn is 3.0 cN/dtex, the elongation at break is 35%, and the curling shrinkage rate is 4.77%, and network degree is 25 units/m. At the temperature of 80 C., the space gap between molecular chains of the different shrinkage composite yarn is increased by 15 v/v %. The fiber density deviation rate is 1.5%, the CV value of the breaking strength is 3.1%, the CV value of elongation at break is 5.3%, the CV value of coiling shrinkage variation coefficient is 4.9% and the oil content is 1.2%.

Comparative Example 1

[0083] The invention relates to a preparation method of different shrinkage composite yarn, which is made from a porous spinneret. The arrangement of holes on the spinneret is circular, which means that the spinning hole center of the spinneret is located on a concentric circle. Concentric circle is a series of circles.

[0084] As shown in FIG. 2, the spacing of the adjacent spinneret is equal to the diameter of the guide hole of the spinneret plus 1.5 mm, and the spinneret is a circular spinneret. The difference between the diameter of the circular spinneret and the maximum diameter of the circle in the series is 11 mm, the diameter of the spinneret is 2.0 mm, the number of spinneret holes is 370, and the cross section shape of the spinneret spinning hole is circle.

[0085] The modified polyester POY yarn is prepared by metering, squeezing, cooling, oiling and winding the modified polyester prepared in EXAMPLE 1, and the modified polyester FDY yarn is prepared by metering, extrusion, cooling, oiling, drawing, heat setting and winding the modified polyester chips. The modified polyester POY yarn and the modified polyester FDY yarn are combined as the network structure to form the different shrinkage composite yarn. The main spinning process parameters are: spinning temperature 280 C., wind temperature 20 C., combined network pressure 3.5 bar, GR1 speed 1000 m/min, SR1 speed 4000 m/min, GR2 speed 3000 m/min, HT1 temperature 100 C., HT2 temperature 130 C., winding speed 3000 m/min.

[0086] The size of the different shrinkage composite yarn is 150 tex, and the breaking strength of the yarn is 1.8 cN/dtex, the elongation at break is 25%, and the curling shrinkage rate is 5.6%, and network degree is 17 units/m. At the temperature of 80 C., the space gap between molecular chains of the different shrinkage composite yarn is increased by 15 v/v %. The fiber density deviation rate is 2.6%, the CV value of the breaking strength is 4.5%, the CV value of elongation at break is 8.2%, the CV value of coiling shrinkage variation coefficient is 8.5% and the oil content is 1.2%.

[0087] Comparing with Example 29, it can be seen that when the effective areas of the spinnerets are the same, and the number of spinning holes is similar (the number of spinning holes arranged in a circular array is 370, the number of spinning holes in an elliptical arrangement is 374, the number of layers of the spinning holes in elliptical arrangement is 6, which is smaller than the number (8) of the layers of spinning hole in circular arrangement, making the cooling effect better. Compared with the EXAMPLE 30, it can be seen that when the effective areas of the spinnerets are the same, the spinning holes are arranged in an elliptical shape, and the number of the layers of spinning holes in elliptical arrangement is 5, which is smaller than the circular arrangement of layers 8, making better cooling effect. The number (382) of holes of spinneret spinning hole elliptical arrangement is larger than the number (370) of spinning holes in circular arrangement, making higher cooling efficiency. Compared to the fiber properties in EXAMPLE 29 and EXAMPLE 30, the fiber density variation, the CV value of breaking strength, the CV value of elongation at break, the CV value of yarn unevenness of the fiber in EXAMPLE 29 and EXAMPLE 30 is smaller than Comparative Example 1, proving that under the same condition, the performance of the fiber made by the spinneret having the elliptical arrangement of the spinning holes is superior to that of the spinneret which is arranged in a circular shape.

Example 3133

[0088] The invention relates to a preparation method of different shrinkage composite yarn, which is made from a porous spinneret. The arrangement of holes on the spinneret is elliptical, which means that the spinning hole center of the spinneret is located on a concentric ellipse. Concentric ellipse is a series of ellipses, all ellipses of the long axis collinear, and short axis collinear.

[0089] The arrangement of the orifices is long axis symmetry. The ratio of the length of the long axis to the short axis of the ellipse is 1.4, the spacing of the adjacent spinneret is equal to the diameter of the guide hole of the spinneret plus 1.6 mm, and the spinneret is a circular spinneret. The difference between the diameter of the circular spinneret and the maximum length of the long axis of the series is 12 mm, the diameter of the spinneret is 1.5 mm, the number of spinneret holes is 192, and the cross-section shape of the spinneret spinning hole is square.

[0090] The modified polyester POY yarn is prepared by metering, squeezing, cooling, oiling and winding the modified polyester, and the modified polyester FDY yarn is prepared by metering, extrusion, cooling, oiling, drawing, heat setting and winding the modified polyester chips. The modified polyester POY yarn and the modified polyester FDY yarn are combined as the network structure to form the different shrinkage composite yarn. The main spinning process parameters are: spinning temperature 300 C. wind temperature 21 C., combined network pressure 4.5 bar, GR1 speed 800 m/min, SR1 speed 3000 m/min, GR2 speed 4000 m/min, HT1 temperature 90 C. HT2 temperature 140 C. winding speed 4000 m/min and the oil content of the different shrinkage composite yarn is 0.8%-0.9%. At the temperature of 80 C., the increasing rate of the space gap between the molecular chain inside the fiber and the data of mechanical properties of the fiber is:

TABLE-US-00002 TABLE 2 the different shrinkage composite yarn's mechanical properties when use the polyester from EXAMPLE 2 to EXAMPLE 4 CV value of curl Fiber CV value CV value shrinkage Elonga- density of of coefficient Curl Modified Breaking tion at Increased deviation breaking elongation of Network shrinkage polyester strength break gap rate strength at break variation degree rate Denier EXAMPLE source (cN/dtex) (%) (v/v %) (%) (%) (%) (%) (pieces/m) (%) (dtex) 31 Example 2.0 27.0 15 2.0 4.0 8.0 7.6 20 3.7 110 2 32 Example 2.4 28.0 15 1.7 3.8 7.6 8.0 22 3.9 100 3 33 Example 2.2 27.9 15 1.8 3.7 7.3 7.8 25 4.1 120 4

Example 3436

[0091] The invention relates to a preparation method of different shrinkage composite yarn, which is made from a porous spinneret. The arrangement of holes on the spinneret is elliptical, which means that the spinning hole center of the spinneret is located on a concentric ellipse. Concentric ellipse is a series of ellipses, all ellipses of the long axis collinear, and short axis collinear.

[0092] The arrangement of the orifices is long axis symmetry. The ratio of the length of the long axis to the short axis of the ellipse is 1.4, the spacing of the adjacent spinneret is equal to the diameter of the guide hole of the spinneret plus 1.7 mm, and the spinneret is a circular spinneret. The difference between the diameter of the circular spinneret and the maximum length of the long axis of the series is 12 mm, the diameter of the spinneret is 1.8 mm, the number of spinneret holes is 200, and the cross section shape of the spinneret spinning hole is diamond.

[0093] The modified polyester POY yarn is prepared by metering, squeezing, cooling, oiling and winding the modified polyester, and the modified polyester FDY yarn is prepared by metering, extrusion, cooling, oiling, drawing, heat setting and winding the modified polyester chips. The modified polyester POY yarn and the modified polyester FDY yarn are combined as the network structure to form the different shrinkage composite yarn. The main spinning process parameters are: spinning temperature 300 C., wind temperature 21 C., combined network pressure 4.5 bar, GR1 speed 800 m/min. SR1 speed 3000 m/min, GR2 speed 4000 m/min, HT1 temperature 90 C., HT2 temperature 140 C., winding speed 3500 m/min and the oil content of the different shrinkage composite yarn is 1.1%-1.2%. At the temperature of 90 C., the increasing rate of the space gap between the molecular chain inside the fiber and the data of mechanical properties of the fiber is:

TABLE-US-00003 TABLE 3 the different shrinkage composite yarn's mechanical properties when use the polyester from EXAMPLE 5 to EXAMPLE 7 CV value of curl Fiber CV value CV value shrinkage Elonga- density of of coefficient Curl Modified Breaking tion at Increased deviation breaking elongation of Network shrinkage polyester strength break gap rate strength at break variation degree rate Denier EXAMPLE source (cN/dtex) (%) (v/v %) (%) (%) (%) (%) (pieces/m) (%) (dtex) 34 Example 2.3 30.4 10 1.1 2.8 6.7 6.9 15 3.1 120 5 35 Example 2.1 31.5 10 1.3 2.6 6.3 6.5 18 3.5 129 6 36 Example 2.4 30.9 10 1.4 2.9 6.0 6.2 20 2.7 125 7

Examples 3739

[0094] The invention relates to a preparation method of different shrinkage composite yarn, which is made from a porous spinneret. The arrangement of holes on the spinneret is elliptical, which means that the spinning hole center of the spinneret is located on a concentric ellipse. Concentric ellipse is a series of ellipses, all ellipses of the long axis collinear, and short axis collinear.

[0095] The arrangement of the orifices is long axis symmetry. The ratio of the length of the long axis to the short axis of the ellipse is 1.4, the spacing of the adjacent spinneret is equal to the diameter of the guide hole of the spinneret plus 1.8 mm, and the spinneret is a circular spinneret. The difference between the diameter of the circular spinneret and the maximum length of the long axis of the series is 13 mm, the diameter of the spinneret is 2.5 mm, the number of spinneret holes is 200, and the cross section shape of the spinneret spinning hole is straight line.

[0096] The modified polyester POY yarn is prepared by metering, squeezing, cooling, oiling and winding the modified polyester, and the modified polyester FDY yarn is prepared by metering, extrusion, cooling, oiling, drawing, heat setting and winding the modified polyester chips. The modified polyester POY yarn and the modified polyester FDY yarn are combined as the network structure to form the different shrinkage composite yarn. The main spinning process parameters are: spinning temperature 300 C., wind temperature 22 C., combined network pressure 4 bar, GR1 speed 900 m/min, SR1 speed 4200 m/min. GR2 speed 4000 m/min, HT1 temperature 115 C., HT2 temperature 135 C. winding speed 3500 m/min and the oil content of the different shrinkage composite yarn is 1.0%-1.2%. At the temperature of 100 C., the increasing rate of the space gap between the molecular chain inside the fiber and the data of mechanical properties of the fiber is:

TABLE-US-00004 TABLE 4 the different shrinkage composite yarn's mechanical properties when use the polyester from EXAMPLE 8 to EXAMPLE 10 CV value of curl Fiber CV value CV value shrinkage Elonga- density of of coefficient Curl Modified Breaking tion at Increased deviation breaking elongation of Network shrinkage polyester strength break gap rate strength at break variation degree rate Denier EXAMPLE source (cN/dtex) (%) (v/v %) (%) (%) (%) (%) (pieces/m) (%) (dtex) 37 Example 2.2 30.7 15 1.3 2.6 7.1 6.8 20 5.1 101 8 38 Example 2.4 33.0 15 1.1 2.1 7.2 6.4 17 5.5 105 9 39 Example 1.7 29.9 15 1.5 2.4 6.7 6.7 18 4.7 113 10

Example 4042

[0097] The invention relates to a preparation method of different shrinkage composite yarn, which is made from a porous spinneret. The arrangement of holes on the spinneret is elliptical, which means that the spinning hole center of the spinneret is located on a concentric ellipse. Concentric ellipse is a series of ellipses, all ellipses of the long axis collinear, and short axis collinear.

[0098] The arrangement of the orifices is long axis symmetry. The ratio of the length of the long axis to the short axis of the ellipse is 1.7, the spacing of the adjacent spinneret is equal to the diameter of the guide hole of the spinneret plus 1.9 mm, and the spinneret is a circular spinneret. The difference between the diameter of the circular spinneret and the maximum length of the long axis of the series is 14 mm, the diameter of the spinneret is 1.5 mm, the number of spinneret holes is 210, and the cross section shape of the spinneret spinning hole is triangle.

[0099] The modified polyester POY yarn is prepared by metering, squeezing, cooling, oiling and winding the modified polyester, and the modified polyester FDY yarn is prepared by metering, extrusion, cooling, oiling, drawing, heat setting and winding the modified polyester chips. The modified polyester POY yarn and the modified polyester FDY yarn are combined as the network structure to form the different shrinkage composite yarn. The main spinning process parameters are: spinning temperature 290 C., wind temperature 22 C., combined network pressure 4 bar, GR1 speed 900 m/min, SR1 speed 4200 m/min, GR2 speed 3500 m/min, HT1 temperature 115 C., HT2 temperature 135 C., winding speed 3300 m/min and the oil content of the different shrinkage composite yarn is 0.9%-1.1%. At the temperature of 110 C., the increasing rate of the space gap between the molecular chain inside the fiber and the data of mechanical properties of the fiber is:

TABLE-US-00005 TABLE 5 the different shrinkage composite yarn's mechanical properties when use the polyester from EXAMPLE 11 to EXAMPLE 13 CV value of curl Fiber CV value CV value shrinkage Elonga- density of of coefficient Curl Modified Breaking tion at Increased deviation breaking elongation of Network shrinkage polyester strength break gap rate strength at break variation degree rate Denier EXAMPLE source (cN/dtex) (%) (v/v %) (%) (%) (%) (%) (pieces/m) (%) (dtex) 40 Example 2.7 25.0 18 1.4 3.1 6.8 6.4 22 3.1 145 11 41 Example 2.4 26.1 18 1.2 3.5 6.2 6.6 23 3.5 150 12 42 Example 2.6 27.3 18 1.0 3.6 6.6 6.3 21 3.9 138 13

Example 4345

[0100] The invention relates to a preparation method of different shrinkage composite yarn, which is made from a porous spinneret. The arrangement of holes on the spinneret is elliptical, which means that the spinning hole center of the spinneret is located on a concentric ellipse. Concentric ellipse is a series of ellipses, all ellipses of the long axis collinear, and short axis collinear.

[0101] The arrangement of the orifices is long axis symmetry. The ratio of the length of the long axis to the short axis of the ellipse is 1.8, the spacing of the adjacent spinneret is equal to the diameter of the guide hole of the spinneret plus 1.5 mm, and the spinneret is a circular spinneret. The difference between the diameter of the circular spinneret and the maximum length of the long axis of the series is 15 mm, the diameter of the spinneret is 1.8 mm, the number of spinneret holes is 240, and the cross section shape of the spinneret spinning hole is trilobal.

[0102] The modified polyester POY yarn is prepared by metering, squeezing, cooling, oiling and winding the modified polyester, and the modified polyester FDY yarn is prepared by metering, extrusion, cooling, oiling, drawing, heat setting and winding the modified polyester chips. The modified polyester POY yarn and the modified polyester FDY yarn are combined as the network structure to form the different shrinkage composite yarn. The main spinning process parameters are: spinning temperature 295 C., wind temperature 21 C., combined network pressure 3.8 bar, GR1 speed 850 m/min. SR1 speed 3500 m/min, GR2 speed 3500 m/min, HT1 temperature 115 C., HT2 temperature 135 C., winding speed 3300 m/min and the oil content of the different shrinkage composite yarn is 0.8%-1.00/0%. At the temperature of 120 C., the increasing rate of the space gap between the molecular chain inside the fiber and the data of mechanical properties of the fiber is:

TABLE-US-00006 TABLE 6 the different shrinkage composite yarn's mechanical properties when use the polyester from EXAMPLE 14 to EXAMPLE 16 CV value of curl Fiber CV value CV value shrinkage Elonga- density of of coefficient Curl Modified Breaking tion at Increased deviation breaking elongation of Network shrinkage polyester strength break gap rate strength at break variation degree rate Denier EXAMPLE source (cN/dtex) (%) (v/v %) (%) (%) (%) (%) (pieces/m) (%) (dtex) 43 Example 1.9 32.7 25 1.6 3.3 6.3 6.1 21 1.9 110 14 44 Example 2.4 31.9 25 1.4 3.1 6.7 5.6 23 1.5 112 15 45 Example 2.1 35.0 25 1.7 2.6 6.9 5.7 24 2.6 115 16

Example 4649

[0103] The invention relates to a preparation method of different shrinkage composite yarn, which is made from a porous spinneret. The arrangement of holes on the spinneret is elliptical, which means that the spinning hole center of the spinneret is located on a concentric ellipse. Concentric ellipse is a series of ellipses, all ellipses of the long axis collinear, and short axis collinear.

[0104] The arrangement of the orifices is long axis symmetry. The ratio of the length of the long axis to the short axis of the ellipse is 1.8, the spacing of the adjacent spinneret is equal to the diameter of the guide hole of the spinneret plus 1.6 mm, and the spinneret is a circular spinneret. The difference between the diameter of the circular spinneret and the maximum length of the long axis of the series is 16 mm, the diameter of the spinneret is 2.2 mm, the number of spinneret holes is 250, and the cross section shape of the spinneret spinning hole is hollow.

[0105] The modified polyester POY yarn is prepared by metering, squeezing, cooling, oiling and winding the modified polyester, and the modified polyester FDY yarn is prepared by metering, extrusion, cooling, oiling, drawing, heat setting and winding the modified polyester chips. The modified polyester POY yarn and the modified polyester FDY yarn are combined as the network structure to form the different shrinkage composite yarn. The main spinning process parameters are: spinning temperature 285 C., wind temperature 21 C., combined network pressure 3.8 bar, GR1 speed 850 m/min, SR1 speed 3500 m/min, GR2 speed 3500 m/min, HT1 temperature 95 C., HT2 temperature 138 C. winding speed 3600 m/min and the oil content of the different shrinkage composite yarn is 0.9%-1.00/0%. At the temperature of 130 C., the increasing rate of the space gap between the molecular chain inside the fiber and the data of mechanical properties of the fiber is:

TABLE-US-00007 TABLE 7 the different shrinkage composite yarn's mechanical properties when use the polyester from EXAMPLE 17 to EXAMPLE 20 CV value of curl Fiber CV value CV value shrinkage Elonga- density of of coefficient Curl Modified Breaking tion at Increased deviation breaking elongation of Network shrinkage polyester strength break gap rate strength at break variation degree rate Denier EXAMPLE source (cN/dtex) (%) (v/v %) (%) (%) (%) (%) (pieces/m) (%) (dtex) 46 Example 2.9 32.7 19 1.2 3.1 5.9 6.2 23 4.1 132 17 47 Example 2.7 31.9 19 1.4 3.0 6.1 5.8 24 4.5 138 18 48 Example 2.6 30.6 19 1.5 2.6 6.3 5.7 25 4.6 135 19 49 Example 2.3 32.2 19 1.3 2.9 5.7 6.0 23 4.3 140 20

Example 5053

[0106] The invention relates to a preparation method of different shrinkage composite yarn, which is made from a porous spinneret. The arrangement of holes on the spinneret is elliptical, which means that the spinning hole center of the spinneret is located on a concentric ellipse. Concentric ellipse is a series of ellipses, all ellipses of the long axis collinear, and short axis collinear.

[0107] The arrangement of the orifices is long axis symmetry. The ratio of the length of the long axis to the short axis of the ellipse is 1.8, the spacing of the adjacent spinneret is equal to the diameter of the guide hole of the spinneret plus 1.8 mm, and the spinneret is a circular spinneret. The difference between the diameter of the circular spinneret and the maximum length of the long axis of the series is 15 mm, the diameter of the spinneret is 2.5 mm, the number of spinneret holes is 260, and the cross section shape of the spinneret spinning hole is flat.

[0108] The modified polyester POY yarn is prepared by metering, squeezing, cooling, oiling and winding the modified polyester, and the modified polyester FDY yarn is prepared by metering, extrusion, cooling, oiling, drawing, heat setting and winding the modified polyester chips. The modified polyester POY yarn and the modified polyester FDY yarn are combined as the network structure to form the different shrinkage composite yarn. The main spinning process parameters are: spinning temperature 285 C., wind temperature 21 C., combined network pressure 4.2 bar, GR1 speed 950 m/min, SR1 speed 3800 m/min, GR2 speed 3600 m/min, HT1 temperature 95 C., HT2 temperature 138 C., winding speed 3600 m/min and the oil content of the different shrinkage composite yarn is 0.9%-1.0%. At the temperature of 100 C., the increasing rate of the space gap between the molecular chain inside the fiber and the data of mechanical properties of the fiber is:

TABLE-US-00008 TABLE 8 the different shrinkage composite yarn's mechanical properties when use the polyester from EXAMPLE 21 to EXAMPLE 24 CV value of curl Fiber CV value CV value shrinkage Elonga- density of of coefficient Curl Modified Breaking tion at Increased deviation breaking elongation of Network shrinkage polyester strength break gap rate strength at break variation degree rate Denier EXAMPLE source (cN/dtex) (%) (v/v %) (%) (%) (%) (%) (pieces/m) (%) (dtex) 50 Example 2.1 31.7 15 1.4 3.4 6.2 6.1 20 4.3 121 21 51 Example 2.7 31.9 15 1.1 3.1 6.4 5.9 22 4.5 127 22 52 Example 2.6 31.6 15 1.3 2.9 6.1 5.7 24 4.1 129 23 53 Example 2.3 32.2 15 1.1 3.3 5.9 6.0 22 4.7 119 24

Example 5457

[0109] The invention relates to a preparation method of different shrinkage composite yarn, which is made from a porous spinneret. The arrangement of holes on the spinneret is elliptical, which means that the spinning hole center of the spinneret is located on a concentric ellipse. Concentric ellipse is a series of ellipses, all ellipses of the long axis collinear, and short axis collinear.

[0110] The arrangement of the orifices is long axis symmetry. The ratio of the length of the long axis to the short axis of the ellipse is 1.8, the spacing of the adjacent spinneret is equal to the diameter of the guide hole of the spinneret plus 1.5 mm, and the spinneret is a circular spinneret. The difference between the diameter of the circular spinneret and the maximum length of the long axis of the series is 16 mm, the diameter of the spinneret is 1.8 mm, the number of spinneret holes is 300, and the cross section shape of the spinneret spinning hole is hollow.

[0111] The modified polyester POY yarn is prepared by metering, squeezing, cooling, oiling and winding the modified polyester, and the modified polyester FDY yarn is prepared by metering, extrusion, cooling, oiling, drawing, heat setting and winding the modified polyester chips. The modified polyester POY yarn and the modified polyester FDY yarn are combined as the network structure to form the different shrinkage composite yarn. The main spinning process parameters are: spinning temperature 288 C., wind temperature 21 C., combined network pressure 4.2 bar, GR1 speed 950 m/min, SR1 speed 4200 m/min, GR2 speed 3600 m/min, HT1 temperature 110 C., HT2 temperature 138 C., winding speed 3800 m/min and the oil content of the different shrinkage composite yarn is 0.9%-1.1%. At the temperature of 120 C., the increasing rate of the space gap between the molecular chain inside the fiber and the data of mechanical properties of the fiber is:

TABLE-US-00009 TABLE 9 the different shrinkage composite yarn's mechanical properties when use the polyester from EXAMPLE 25 to EXAMPLE 28 CV value of curl Fiber CV value CV value shrinkage Elonga- density of of coefficient Curl Modified Breaking tion at Increased deviation breaking elongation of Network shrinkage polyester strength break gap rate strength at break variation degree rate Denier EXAMPLE source (cN/dtex) (%) (v/v %) (%) (%) (%) (%) (pieces/m) (%) (dtex) 54 Example 2.3 32.7 30 1.0 3.0 6.0 5.6 15 4.7 138 25 55 Example 1.9 31.9 30 0.9 3.1 5.4 5.9 17 4.9 141 26 56 Example 2.1 33.0 30 1.1 2.7 5.7 5.7 23 4.2 150 27 57 Example 2.5 32.2 30 1.3 3.3 5.9 6.0 20 4.5 147 28

Example 58

[0112] Dyeing Process of Different Shrinkage Composite Yarn:

[0113] The different shrinkage composite yarn prepared in Example 29 is dyed in a high temperature and high pressure machine under the following conditions: before dyeing, the different shrinkage composite yarn is treated with a nonionic surfactant at 60 C. for 30 minutes, and then added to the dyeing solution. In the dyeing solution, the disperse dye content is 2.0% (o.w.f). The dispersant is NNO. The concentration of dispersant NNO is 1.2 g/L and the pH value is 5, the bath ratio is 1:50. Dye the yarn at 60 C., and then raise the temperature to 90 C., 100 C., 110 C., 120 C. and 130 C., dye at each temperature for 1 hour.

[0114] Dye the common fibers under the same dyeing conditions. The percentage of dyeing of the modified polyester fiber after dyeing is obtained by the following method:

[0115] The percentage of dyeing is determined by the residual liquid colorimetric method. Take the appropriate amount of dyeing stock solution and dyeing residue, and add N, N-2 methylformnamide (DMF) and distilled water. The ratio of DMF to water in the dye solution is 70/30 (v/v), the absorbance of the dye solution is measured by an ultraviolet-visible spectrophotometer, and the percentage of dyeing is calculated by the following formula.

[00001]$\mathrm{Percentage}.Math..Math.\mathrm{of}.Math..Math.\mathrm{dyeing}=100.Math.\%\left(1-\frac{A.Math..Math.1}{A.Math..Math.0}\right)$

[0116] In the formula above, A0 and A1 are respectively the absorbances of the dyeing stock solution and the dye residue.

[0117] When the disperse dye is disperse red 3B, disperse blue SE-2R or disperse turquoise S-GL, the dyeing percentage of different shrinkage composite yarn and the common fiber is as follows:

TABLE-US-00010 TABLE 10 the comparison of the percentage of dyeing between different shrinkage composite yarn and ordinary fiber when use modified polyester prepared in EXAMPLE 29 Percentage temperature of dyeing 90 C. 100 C. 110 C. 120 C. 130 C. Disperse Different 50.3 77.3 84.2 88.0 89.4 red 3B shrinkage composite yarn Ordinary 28.2 46.3 78.5 81.7 90.2 fiber Disperse Different 53.6 78.7 84.4 86.4 89.1 blue SE-2R shrinkage composite yarn Ordiniary 12.3 35.2 73.4 88.9 91.3 fiber Scattered Different 44.8 70.4 76.0 83.7 86.7 turquoise shrinkage blue S-GL composite yarn Ordinary 11.8 36.3 70.9 75.6 82.6 fiber

[0118] By comparing the dyeing effect of the different shrinkage composite yarn with the ordinary fiber, it can be seen that the dyeing effect of the different shrinkage composite yarn is obviously superior to that of the ordinary fiber, and it can also be seen that the branched diol segment in the macromolecule of the modified polyester prepared in the invention, making the rate of increase much greater than the free volume unbranched general properties of the polyester of the macromolecular chains. The increase of the free volume helps fine particles go into the interior of the polyester, the free volume of the polyester fiber made from the modified polyester is much larger than that of the unbranched ordinary polyester fiber at the same temperature, which increases the diffusion degree of the dye and improves the dyeing property of the polyester fiber.

Example 59

[0119] Dyeing Process of Different Shrinkage Composite Yarn:

[0120] The different shrinkage composite yarn prepared in Example 31 is dyed in a high temperature and high pressure machine under the following conditions: before dyeing, the different shrinkage composite yarn is treated with a nonionic surfactant at 60 C. for 30 minutes, and then added to the dyeing solution. In the dyeing solution, the disperse dye content is 2.0% (o.w.f). The dispersant is NNO. The concentration of dispersant NNO is 1.2 g/L and the pH value is 5, the bath ratio is 1:50. Dye the yarn at 60 C., and then raise the temperature to 90 C., 100 C., 110 C., 120 C. and 130 C., dye at each temperature for 1 hour.

[0121] Dye the common fibers under the same dyeing conditions. The percentage of dyeing of the modified polyester fiber after dyeing is obtained by the following method:

[0122] The percentage of dyeing is determined by the residual liquid colorimetric method. Take the appropriate amount of dyeing stock solution and dyeing residue, and add N, N-2 methylformamide (DMF) and distilled water. The ratio of DMF to water in the dye solution is 70/30 (v/v), the absorbance of the dye solution is measured by an ultraviolet-visible spectrophotometer, and the percentage of dyeing is calculated by the following formula.

[00002]$\mathrm{Percentage}.Math..Math.\mathrm{of}.Math..Math.\mathrm{dyeing}=100.Math.\%\left(1-\frac{A.Math..Math.1}{A.Math..Math.0}\right)$

[0123] In the formula above, A0 and A1 are respectively the absorbances of the dyeing stock solution and the dye residue.

[0124] When the disperse dye is disperse red 3B, disperse blue SE-2R or disperse turquoise S-GL, the percentage of dyeing percentage of different shrinkage composite yarn and the common fiber is as follows:

TABLE-US-00011 TABLE 11 the comparison of the percentage of dyeing between different shrinkage composite yarn and ordinary fiber when use modified polyester prepared in EXAMPLE 31 temperature dye 90 C. 100 C. 110 C. 120 C. 130 C. Disperse Different 50.3 77.3 84.2 88.0 89.4 red 3B shrinkage composite yarn Common 28.2 46.3 78.5 81.7 90.2 fiber Disperse Different 53.6 78.7 84.4 86.4 89.1 blue SE-2R shrinkage composite yarn Common 12.3 35.2 73.4 88.9 91.3 fiber Scattered Different 44.8 70.4 76.0 83.7 86.7 turquoise shrinkage blue S-GL composite yarn Common 11.8 36.3 70.9 75.6 82.6 fiber

[0125] By comparing the dyeing effect of the different shrinkage composite yarn with the ordinary fiber, it can be seen that the dyeing effect of the different shrinkage composite yarn is obviously superior to that of the ordinary fiber, and it can also be seen that the branched diol segment in the macromolecule of the modified polyester prepared in the invention, making the rate of increase much greater than the free volume unbranched general properties of the polyester of the macromolecular chains. The increase of the free volume helps fine particles go into the interior of the polyester, the free volume of the polyester fiber made from the modified polyester is much larger than that of the unbranched ordinary polyester fiber at the same temperature, which increases the diffusion degree of the dye and improves the dyeing property of the polyester fiber.