CN106592001B - A kind of aromatic polyester-aliphatic polyester block copolymerization ester fiber and purposes - Google Patents

A kind of aromatic polyester-aliphatic polyester block copolymerization ester fiber and purposes Download PDF

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CN106592001B
CN106592001B CN201611160113.3A CN201611160113A CN106592001B CN 106592001 B CN106592001 B CN 106592001B CN 201611160113 A CN201611160113 A CN 201611160113A CN 106592001 B CN106592001 B CN 106592001B
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aliphatic
polyester
ester
aromatic polyester
acid
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CN106592001A (en
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邱志成
金剑
李志勇
王颖
廉志军
刘玉来
王雪
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CHINA TEXTILE ACADEMY (TIANJIN) TECHNOLOGY DEVELOPMENT Co Ltd
China Textile Research Institute Co Ltd
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CHINA TEXTILE ACADEMY (TIANJIN) TECHNOLOGY DEVELOPMENT Co Ltd
China Textile Research Institute Co Ltd
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    • 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
    • D01F6/78Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products
    • D01F6/84Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products from copolyesters
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G81/00Macromolecular compounds obtained by interreacting polymers in the absence of monomers, e.g. block polymers
    • DTEXTILES; PAPER
    • D02YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02GCRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
    • D02G3/00Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
    • D02G3/02Yarns or threads characterised by the material or by the materials from which they are made
    • DTEXTILES; PAPER
    • D02YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02GCRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
    • D02G3/00Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
    • D02G3/02Yarns or threads characterised by the material or by the materials from which they are made
    • D02G3/04Blended or other yarns or threads containing components made from different materials
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2201/00Cellulose-based fibres, e.g. vegetable fibres
    • D10B2201/01Natural vegetable fibres
    • D10B2201/02Cotton
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2211/00Protein-based fibres, e.g. animal fibres
    • D10B2211/01Natural animal fibres, e.g. keratin fibres
    • D10B2211/02Wool
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2211/00Protein-based fibres, e.g. animal fibres
    • D10B2211/01Natural animal fibres, e.g. keratin fibres
    • D10B2211/04Silk
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2331/00Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products
    • D10B2331/04Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products polyesters, e.g. polyethylene terephthalate [PET]
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2331/00Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products
    • D10B2331/10Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products polyurethanes

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Textile Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Artificial Filaments (AREA)

Abstract

The invention belongs to textile development fields, more particularly to a kind of aromatic polyester-aliphatic polyester block copolymerization ester fiber, the aromatic polyester-aliphatic polyester blocked copolyester is formed by oligoterephthalic acid glycol ester and aliphatic polydiacid diol ester polyhydric alcohol, and has following chemical structure:Wherein, 4 < x <, 100,1 < y < 25, R1For C2~C8 alkylidene, R2For C3~C8 alkylidene;Aromatic polyester-aliphatic polyester blocked copolyester degree of randomness B is 0.05~0.95.The aromatic polyester-aliphatic polyester block copolymerization ester fiber not only has the characteristics that disperse dye dyeable is dark under normal pressure, but also there is good dimensional stability, can be preferably mixed or blended with the elastomers such as natural fibers and spandex such as the cotton of non-refractory, wool, silk, obtain more function admirables and coloury textile material.

Description

A kind of aromatic polyester-aliphatic polyester block copolymerization ester fiber and purposes
Technical field
The invention belongs to textile development fields, and in particular to a kind of aromatic polyester-aliphatic polyester blocked copolyester Fiber and purposes.
Background technique
Polyester fiber has many advantages, such as good breaking strength height, form stable, stiffness, wash and wear, easy to wash easily dry, is one The more satisfactory textile fabric of kind.It is regular that these excellent physical and mechanical properties of polyester fiber depend on its High level of stereoselectivity The condensed state structure of macromolecular chain structure and high-crystallinity and the degree of orientation, but these architectural characteristics also give polyester fiber Achromatic defect.Meanwhile the lesser ester group of polarized in polyester fiber molecular structure, shortage can be bonded with dyestuff The active group of effect can only be dyed using disperse dyes.Disperse dyes belong to nonionic dye, molecular dimension compared with Greatly, water-soluble lower, while the water imbibition of polyester fiber is poor, is not easy to expand in water, so when being dyed with conventional method, dye The dispersion particle of material is difficult to enter fiber from solution, very low the dye-uptake under fluidized state.Polyester in the prior art The dyeing of fiber generallys use high-temperature and high pressure dyeing process and carrier boiling dyeing at normal pressure method.When polyester fiber is dyed using support methods, by Internal plasticization can be played in fibrous inside in carrier, is conducive to dyestuff in the diffusion of fibrous inside, but remaining carrier can make The light resistance of dyestuff is deteriorated, and pollutes.Under the pressure of environmental protection pressure, carrier dyeing process is gradually backed out the arena of history, high temperature and pressure Decoration method has become mainstream.But that there are energy consumptions is high for high-temperature and high pressure dyeing process, is difficult to the shortcomings that serialization industrial production, and be difficult to The elastomers co-bathing dyeing such as the natural fibers such as cotton, wool, the silk of non-refractory and spandex, this strongly limits polyester The application range of fiber.
Therefore, the research and development of the dyeable modified polyester fiber of normal pressure are always by the extensive concern of academia and industry. Currently, the preparation of the dyeable modified polyester fiber of normal pressure mainly changes polyester fiber by the method for physical modification or chemical modification Molecular structure or supramolecular structure, introduce dye molecule receive base or increase accommodate dye molecule space, thus realize change The normal pressure of property polyester fiber can contaminate.
ZL02111210.X discloses a kind of dyed easily by disperse dye functionality copolyester fiber and preparation method, the patent Dyed easily by disperse dye functionality copolyester section using terephthalic acid (TPA), ethylene glycol as raw material, it is (opposite that 2-100mol% is added In terephthalic acid (TPA)) the Third monomer of the binary acid containing isophthalic be copolymerized.Between being added on polyester macromolecule The Third monomer of phenyl group, so that the regularity of polyester macromolecule declines, crystallizing power weakens, and amorphous area increases, short texture, There is disperse dye normal pressure stainability using the fiber that copolyester section spins.But since dyed easily by disperse dye functionality is total Polyester is random copolymer, and molecular structure regularity is poor, crystallizing power is weaker, and fiber size stability is poor, in boiling water condition It is lower easily to occur largely to shrink, it is difficult to be widely used in garment industry.
CN201110366748.X discloses a kind of normal pressure disperse dye dyeable modified copolymer ester fiber, by modified copolyester Spinning forms, in copolyesters containing Third monomer be band side chain and carbon atom number be 6 aliphatic dihydroxy alcohols below.Due to polyester Introducing with side chain dihydric alcohol structural unit in molecular backbone, so that the regularity of macromolecular declines, crystallizing power weakens, amorphous Area increases, short texture, so that the performance that copolyester fiber disperse dye normal pressure can contaminate is imparted, but the fiber of the copolyesters Dimensional stability is also poor, and the shortcomings that largely shrinking easily occurs under the conditions of boiling water.
In order to solve defect in the prior art, the present invention is specifically proposed.
Summary of the invention
The purpose of the present invention, which first consists in, overcomes defect of the existing technology, provides and a kind of has both excellent disperse dyes The aromatic polyester of dyeing at normal pressure performance and dimensional stability-aliphatic polyester block copolymerization ester fiber.
In order to solve the problems, such as that techniques discussed above, the basic ideas of technical solution of the present invention are as follows:
A kind of aromatic polyester-aliphatic polyester block copolymerization ester fiber, wherein aromatic polyester-aliphatic polyester is embedding Section copolyesters is formed by oligoterephthalic acid glycol ester and aliphatic polydiacid diol ester polyhydric alcohol, and With following chemical structure:
Wherein, 4 < x <, 100,1 < y < 25, R1For C2~C8 alkylidene, R2For C3~C8 alkylidene;Aromatic polyester- The degree of randomness B of aliphatic polyester blocked copolyester is 0.05~0.95.
The value of degree of randomness B has 0,1,2, < 1 four kind of situation: B=0 indicates that polymer is the blend or long block of homopolymer Copolymer;B=1 indicates that copolymer is random distribution;B=2 indicates that copolymer is completely alternate sequence distribution, and B < l is indicated altogether Polymers has the tendency that as block copolymer.The present invention provides copolyesters and controls degree of randomness B in the range of 0.05≤B≤0.95, Indicate that the copolymer has the tendency that as block copolymer, but there is no become by aromatic polyester homopolymer and aliphatic poly The long block copolymer that ester homopolymer is formed.
According to above scheme, the accounting of aromatic polyester block is greater than aliphatic polyester block in copolyesters of the invention Accounting, be in order to guaranteeing copolyesters strand regularity and under the premise of dimensional stability, utilize aliphatic polyester block Increase the flexibility of molecule segment, so that it is with stronger crystallizing power and higher hot property, while will not be high because of having The aromatic polyester of the long block of regularity leads to the decline of dyeing function
, and in random copolymer due to structural unit dispersion randomness, cause aromatic polyester can not be formed long-chain from And destroy regularity;And in the block copolymer formed by homopolymer, aromatic polyester section and aliphatic polyester section are strictly divided It opens, is equally unable to reach the requirement to crystallizing power and dyeing function.Therefore, the present invention select degree of randomness for 0.05≤B≤ The aromatic polyester of 0.95 range-aliphatic polyester blocked copolyester.
In the present invention, the long block copolymer is by aromatic polyester homopolymer and aliphatic poly ester homopolymer two The copolymer that segment is polymerized, that is, the such arrangement of BBBBBB ... that forms AAAAAAA ....
The degree of randomness B formula (I) of copolyesters of the present invention calculates:
Wherein: TA is terephthalic acid (TPA), EG is ethylene glycol, SA is straight-chain aliphatic binary acid, BO is pendant aliphatic two First alcohol;FTA-EGMolar fraction, F for ethylene glycol terephthalate repetitive unitTA-BOFor terephthalic acid (TPA) pendant aliphatic two The molar fraction of first alcohol ester repetitive, FSA-BOFor rubbing for straight-chain aliphatic binary acid pendant aliphatic binary alcohol esters repetitive unit That score, FSA-EGFor the molar fraction of straight-chain aliphatic binary acid glycol ester repetitive unit.
The molar fraction of each repetitive unit uses in aromatic polyester-aliphatic polyester blocked copolyester13C-NMR technology is surveyed Amount, by comparing the integral area of signal peak caused by carbonyl carbon in each repetitive unit, to measure repetitive unit terephthalic acid (TPA) Glycol ester, terephthalic acid (TPA) pendant aliphatic binary alcohol esters, straight-chain aliphatic binary acid pendant aliphatic binary alcohol esters and straight The molar fraction of chain fatty race binary acid glycol ester, their carbonyl carbon all have different in the region 160~185ppm Resonance.
The aromatic polyester-aliphatic polyester block copolymerization ester fiber can be realized well lower than 100 DEG C The dyeability of dyestuff, dyeing uniformity and dyefastness are good, and good stability of the dimension, in addition also have preferable dry and wet strong Degree, is a kind of textile fiber material haveing excellent performance.
In particular, aromatic polyester-aliphatic polyester block copolymerization ester fiber and protein fibre, elastomer (such as ammonia Synthetic fibre) between there is very high matching, mixed/intertexture of a step one-bath process can be prepared, under lower mild normal pressure to spin It knits, dress ornament field provides a variety of excellent textile materials.
It is highly preferred that the aromatic polyester-aliphatic polyester blocked copolyester degree of randomness B is 0.1~0.74.
Further scheme of the invention are as follows: the ratio of x and y is x:y=4~54:1.
To achieve the purpose of the present invention, the aromatic polyester section phase in aromatic polyester-aliphatic polyester blocked copolyester Occupy more ingredients than aliphatic polyester block, is the dimensional stability in order to guarantee copolyesters.
Preferably, the aromatic polyester-aliphatic polyester blocked copolyester inherent viscosity is 0.5~1.2dL/g, Fusing point is 160~250 DEG C, and glass transition temperature is 40~77 DEG C.
Aromatic polyester-aliphatic polyester blocked copolyester performance indicator in the range, there is good spinning to add Work performance.And aromatic polyester-aliphatic polyester blocked copolyester glass transition temperature and fusing point only one, table Bright aliphatic poly Straight chain diatomic acid side group binary alcohol esters polyalcohol has been inserted into polyethylene terephthalate in polycondensation process In ester molecule main chain, and aliphatic poly Straight chain diatomic acid side group binary alcohol esters segment and polyethylene terephthalate segment With preferable compatibility, mutually separated there is no apparent.
It is highly preferred that the aromatic polyester-aliphatic polyester blocked copolyester inherent viscosity is 0.8~1.1dL/ G, fusing point are 209~230 DEG C, and glass transition temperature is 55~70 DEG C.
Using the aromatic polyester with above-mentioned preferred or preferred performance-aliphatic polyester blocked copolyester, make altogether The tensile strength of polyester fiber is bigger, tension fracture elongation rate is high, dry and wet fracture value is bigger, and keeps its dyeing more uniform, Color difference should not occur.
Preferably, aromatic polyester-aliphatic polyester blocked copolyester form and aspect b value is 1~8, the content of diethylene glycol (DEG)≤ 1.5%.
It is highly preferred that the aromatic polyester-aliphatic polyester blocked copolyester form and aspect b value is 2~5.
It is highly preferred that the content of the diethylene glycol (DEG) in the aromatic polyester-aliphatic polyester block copolymerization ester fiber≤ 1.0%.
The diethylene glycol (DEG) of the content can make fiber have good flexibility, and can promote the spinning properties of fiber And dyeability, improve the overall quality of fiber further, spins out the clothing feel come and color is good, outside It sees luxurious and comfortable and easy to wear.
In the present invention, the degree of polymerization of the oligoterephthalic acid glycol ester is 1-8.
In the present invention, the test method of the inherent viscosity: referring to GB/T 14190-2008.
Preferably, the binary acid in the aliphatic polydiacid diol ester polyalcohol is straight-chain aliphatic binary acid, Dihydric alcohol is pendant aliphatic dihydric alcohol.
It is highly preferred that the straight-chain aliphatic binary acid is succinic acid, adipic acid or decanedioic acid.
It is highly preferred that the aliphatic dihydroxy alcohol containing side group is 1,2-PD, methyl propanediol, neopentyl glycol, 2- Methyl -2,4-PD, 3- methyl-1,5- pentanediol or trimethylpentanediol.
The crystal property of the above-described preferred or preferred adjustable fiber of technical solution, makes unformed area structure It is more loose, uniformly firm upper dye effect is realized under conditions of normal temperature and pressure, portion are by carrier convenient for dyestuff.
Aromatic polyester of the present invention-aliphatic polyester blocked copolyester is prepared using following method, including such as Lower step:
(1) proper catalyst is added in the terephthalic acid (TPA) and ethylene glycol mixture that molar ratio is 1:1.05~2 to prepare At slurry;
(2) slurry being prepared in step (1) is subjected to esterification, it is oligomeric obtains ethylene glycol terephthalate Object;
(3) after the oligoterephthalic acid glycol ester that step (2) is prepared being adjusted the temperature to 200~250 DEG C It is uniformly mixed with the aliphatic polydiacid diol ester polyalcohol added online, then carries out prepolymerization reaction, be copolymerized Ester prepolymer;
(4) copolyester prepolymer that step (3) is prepared carries out final polycondensation reaction, obtains copolyesters melt;
(5) the copolyesters melt that step (4) is prepared is cooled and solidified after filtering, copolyester section is made.
In the present invention, the catalyst is this field common catalyst when preparing ethylene glycol terephthalate, It is well known in the art.
Aromatic polyester of the present invention-aliphatic polyester blocked copolyester is oligomeric by ethylene glycol terephthalate Object and aliphatic polydiacid diol ester polyalcohol are generated in polycondensation process by ester exchange reaction, anti-by regulation polycondensation The degree of the controllable ester exchange reaction of the condition answered, to reach regulation polyethylene terephthalate segment and aliphatic poly The purpose of binary acid binary alcohol esters polyol segment length.Since copolyesters is blocked copolyester, the regularity of macromolecular chain is good, Crystallizing power is stronger, therefore the fiber spinned has good dimensional stability, and boiling water shrinkage can satisfy subsequent completely The requirement of processing.
Preferably, the number-average molecular weight of the aliphatic poly Straight chain diatomic acid side group binary alcohol esters is 300~10000.
Aliphatic poly Straight chain diatomic acid side group binary alcohol esters polyalcohol in the molecular weight ranges has suitable strand Segment length can meet in subsequent polycondensation process and be embedded in polyethylene terephthalate molecular skeleton by ester exchange reaction The requirement of aliphatic poly Straight chain diatomic acid side group binary alcohol esters segment.
Preferably, the mass ratio of oligoterephthalic acid glycol ester and aliphatic polydiacid diol ester polyalcohol For 100:3~40.
The copolymerization ratios of aliphatic polydiacid diol ester polyalcohol are lower than oligoterephthalic acid glycol ester When 3wt%, disperse dyes, which are not achieved, in the dyeability of copolyester fiber can press the effect that can be contaminated;Aliphatic poly binary acid dihydric alcohol When the copolymerization ratios of ester polyol are higher than the 20wt% of oligoterephthalic acid glycol ester, copolyester fiber is easily because of upper dye speed Rate is too fast and generates specking and dyefastness is lower, and the requirement of rear road application is not achieved.
Preferably, aromatic polyester-aliphatic polyester blocked copolyester is subjected to melt spinning, the spinning temperature used for 180~300 DEG C.
Under the spinning temperature, aromatic polyester-aliphatic polyester blocked copolyester melt has good spinning properties. After aromatic polyester-aliphatic polyester blocked copolyester melt carries out spinning, it is adjusted by counter extensioin, winding process, energy Enough prepare different types of fiber, such as staple fiber, fully drawn yarn FDY or stretch textured yarn DTY.
Preferably, the disperse dyeing dye-uptake under normal pressure is at least 85%;
Dyefastness is at least 4 grades;
Boiling water shrinkage is 1~8%.
Another free-revving engine of the invention is to provide any one above-described aromatic polyester-aliphatic polyester Block copolymerization ester fiber is used to prepare pure spinning textile or the use with cotton, wool, silk, spandex intertexture or blended textile On the way.
Compared to the prior art aromatic polyester of the invention-aliphatic polyester block copolymerization ester fiber, has following The utility model has the advantages that
(1) aromatic polyester-aliphatic polyester block copolymerization ester fiber has both good disperse dye normal pressure stainability And dimensional stability, it can be preferably mixed with the elastomers such as natural fibers and spandex such as the cotton of non-refractory, wool, silk Or blending product is made into the fabric of various styles, pure can also spin and be processed into fabric;
(2) boiling dyeing at normal pressure technique can be used in dyeing, so energy consumption when greatly reducing dyeing;
(3) dye-uptake is high, reduces the discharge of pollutant, has excellent low-carbon environment-friendly performance, can save production cost, Improve production efficiency;
(4) aromatic polyester-aliphatic polyester block copolymerization ester fiber and the property of protein fibre, spandex fibre have Good matching and compatibility may be implemented to be dyed under conditions of 100 DEG C or less and normal pressure, can greatly enrich weaving material Item kind;
(5) mixed/intertexture of aromatic polyester-aliphatic polyester block copolymerization ester fiber and protein fibre, spandex fibre Object can carry out the fabric for mixing/interweaving, and obtain for the single resulting fabric of weaving of the two using arbitrary proportion, Performance more preferably, and can also reduce weaving cost;
(6) staining method has flexibility, can satisfy market to the need of small lot, multicolour polyester fibre containing textile It asks, remarkable in economical benefits.
Specific embodiment
To make the object, technical solutions and advantages of the present invention clearer, preferred real below in conjunction with part of the invention It applies example technical solution of the present invention is clearly and completely described, following embodiment is used merely to explain the present invention, but is not used to limit The scope of the present invention processed.
Embodiment 1
Aromatic polyester-aliphatic polyester blocked copolyester slice is entered after screw extruder melts at 280 DEG C Filament spinning component, winding speed 4200m/min obtain aromatic polyester-aliphatic polyester blocked copolyester fully drawn yarn FDY.Its In, the speed 1500m/min of hot-rolling GR1, temperature are 80 DEG C, and the speed of hot-rolling GR2 is 4250m/min, temperature is 140 DEG C.
The oligoterephthalic acid glycol ester that aromatic polyester-aliphatic polyester blocked copolyester is 6 by the degree of polymerization It is that 2000 polyadipate methyl propanediol ester polyol polycondensations form with number-average molecular weight, wherein ethylene glycol terephthalate is low The mass ratio of polymers and polyadipate methyl propanediol ester polyol is 100:10, and the inherent viscosity of copolyester section is 0.72dL/g, fusing point are 229 DEG C, and glass transition temperature is 71 DEG C, and form and aspect b value is 3, diethylene glycol content 0.9%.Copolyesters Molecular structural formula it is as follows:
Wherein x=38.88, y=4.05, the degree of randomness of copolyesters are 0.27.
Embodiment 2
Aromatic polyester-aliphatic polyester blocked copolyester slice is entered after screw extruder melts at 270 DEG C Filament spinning component, winding speed 3800m/min obtain aromatic polyester-aliphatic polyester blocked copolyester fully drawn yarn FDY.Its In, the speed 1200m/min of hot-rolling GR1, temperature are 72 DEG C, and the speed of hot-rolling GR2 is 3850m/min, temperature is 130 DEG C.
The oligoterephthalic acid glycol ester that aromatic polyester-aliphatic polyester blocked copolyester is 2 by the degree of polymerization Poly-succinic -1,2-PD ester polyol the polycondensation for being 300 with number-average molecular weight forms, wherein ethylene glycol terephthalate Oligomer and poly-succinic -1,2-PD ester polyol mass ratio are 100:10, and the inherent viscosity of copolyester section is 0.75dL/g, fusing point are 226 DEG C, and glass transition temperature is 70 DEG C, and form and aspect b value is 4, diethylene glycol content 1.0%.Copolyesters Molecular structural formula it is as follows:
Wherein x=12.00, y=1.44, the degree of randomness of copolyesters are 0.78.
Embodiment 3
Aromatic polyester-aliphatic polyester blocked copolyester slice is entered after screw extruder melts at 300 DEG C Filament spinning component, winding speed 5200m/min obtain aromatic polyester-aliphatic polyester blocked copolyester fully drawn yarn FDY.Its In, the speed 1800m/min of hot-rolling GR1, temperature are 90 DEG C, and the speed of hot-rolling GR2 is 5250m/min, temperature is 160 DEG C.
The oligoterephthalic acid glycol ester that aromatic polyester-aliphatic polyester blocked copolyester is 1 by the degree of polymerization The poly- decanedioic acid trimethylpentanediol ester polyol polycondensation for being 1000 with number-average molecular weight forms, wherein terephthalate The mass ratio of ester oligomer and poly- decanedioic acid trimethylpentanediol ester polyol is 100:3, and the inherent viscosity of copolyester section is 0.62dL/g, fusing point are 250 DEG C, and glass transition temperature is 77 DEG C, and form and aspect b value is 1, diethylene glycol content 0.8%.Copolyesters Molecular structural formula it is as follows:
Wherein x=65.41, y=1.21, the degree of randomness of copolyesters are 0.84.
Embodiment 4
Aromatic polyester-aliphatic polyester blocked copolyester slice is entered after screw extruder melts at 260 DEG C Filament spinning component, winding speed 3000m/min obtain modified poly ester preoriented yarn POY.Preoriented yarn POY is enterprising in elasticizer The processing of row draw texture, process velocity 600m/min, draft ratio are 1.6 times, deformation temperature is 150 DEG C, D/Y 1.8; It is further formed in shaping box, wherein shaping box temperature is 130 DEG C;Finally with winding speed 960m/min package, virtue is obtained Fragrant adoption ester-aliphatic polyester blocked copolyester stretch textured yarn DTY.
The oligoterephthalic acid glycol ester that aromatic polyester-aliphatic polyester blocked copolyester is 2 by the degree of polymerization The poly-succinic neopentyl glycol ester polyhydric alcohol for being 5000 with number-average molecular weight forms, and wherein ethylene glycol terephthalate is low The mass ratio of polymers and poly-succinic neopentyl glycol ester polyol is 100:15, and the inherent viscosity of copolyester section is 0.82dL/ G, fusing point are 214 DEG C, and glass transition temperature is 63 DEG C, and form and aspect b value is 5, diethylene glycol content 1.1%.The molecule of copolyesters Structural formula is as follows:
Wherein x=68.71, y=10.65, the degree of randomness of copolyesters are 0.11.
Embodiment 5
Aromatic polyester-aliphatic polyester blocked copolyester slice is entered after screw extruder melts at 240 DEG C Filament spinning component, winding speed 2800m/min obtain modified poly ester preoriented yarn POY.Preoriented yarn POY is enterprising in elasticizer The processing of row draw texture, process velocity 520m/min, draft ratio are 1.7 times, deformation temperature is 140 DEG C, D/Y 2.0; It is further formed in shaping box, wherein shaping box temperature is 120 DEG C;Finally with winding speed 880m/min package, virtue is obtained Fragrant adoption ester-aliphatic polyester blocked copolyester stretch textured yarn DTY.
The oligoterephthalic acid glycol ester that aromatic polyester-aliphatic polyester blocked copolyester is 8 by the degree of polymerization The poly-succinic methyl propanediol ester polyol polycondensation for being 10000 with number-average molecular weight forms, wherein terephthalate The mass ratio of ester oligomer and poly-succinic methyl propanediol ester polyol is 100:20, and the inherent viscosity of copolyester section is 1.20dL/g, fusing point are 196 DEG C, and glass transition temperature is 54 DEG C, and form and aspect b value is 5, diethylene glycol content 1.3%.Copolyesters Molecular structural formula it is as follows:
Wherein x=101.27, y=23.36, the degree of randomness of copolyesters are 0.05.
Embodiment 6
Aromatic polyester-aliphatic polyester blocked copolyester slice is entered after screw extruder melts at 240 DEG C Filament spinning component, winding speed 2800m/min obtain modified poly ester preoriented yarn POY.Preoriented yarn POY is enterprising in elasticizer The processing of row draw texture, process velocity 520m/min, draft ratio are 1.7 times, deformation temperature is 140 DEG C, D/Y 2.0; It is further formed in shaping box, wherein shaping box temperature is 120 DEG C;Finally with winding speed 880m/min package, virtue is obtained Fragrant adoption ester-aliphatic polyester blocked copolyester stretch textured yarn DTY.
The oligoterephthalic acid glycol ester that aromatic polyester-aliphatic polyester blocked copolyester is 3 by the degree of polymerization It is 8000 poly- decanedioic acid -3- methyl-1s with number-average molecular weight, 5- pentadiol ester polyhydric alcohol forms, wherein terephthalic acid (TPA) second Glycol ester oligomer and poly- decanedioic acid -3- methyl-1, the mass ratio of 5- pentadiol ester polyalcohol are 100:20, copolyester section Inherent viscosity is 0.98dL/g, and fusing point is 180 DEG C, and glass transition temperature is 50 DEG C, and form and aspect b value is 6, and diethylene glycol content is 1.5%.The molecular structural formula of copolyesters is as follows:
Wherein x=18.81, y=2.54, the degree of randomness of copolyesters are 0.45.
Embodiment 7
Aromatic polyester-aliphatic polyester blocked copolyester slice is entered after screw extruder melts at 240 DEG C Filament spinning component, winding speed 1200m/min obtain aromatic polyester-aliphatic polyester blocked copolyester spun filament UDY.It will be first Raw silk UDY is in 65 DEG C of progress level-one drawing-offs, and 2.8 times of drafting multiple;In 85 DEG C of progress second level drawing-offs, 1.4 times of drafting multiple, later Fiber is crimped at 100 DEG C.Then it is carried out shaping at 130 DEG C, the fiber after sizing obtains after prescinding, being packaged on cutting machine To aromatic polyester-aliphatic polyester blocked copolyester cotton-type short fiber.
The oligoterephthalic acid glycol ester that aromatic polyester-aliphatic polyester blocked copolyester is 5 by the degree of polymerization Poly- decanedioic acid -2- methyl -2, the 4- pentadiol ester polyhydric alcohol for being 3000 with number-average molecular weight forms, wherein terephthalic acid (TPA) The mass ratio of glycol ester oligomer and poly- decanedioic acid -2- methyl -2,4- pentadiol ester polyalcohol is 100:5, copolyester section Inherent viscosity be 0.50dL/g, fusing point is 236 DEG C, and glass transition temperature is 73 DEG C, and form and aspect b value is 3, and diethylene glycol content is 1.0%.The molecular structural formula of copolyesters is as follows:
Wherein x=34.02, y=1.15, the degree of randomness of copolyesters are 0.90.
Embodiment 8
Aromatic polyester-aliphatic polyester blocked copolyester slice is entered after screw extruder melts at 180 DEG C Filament spinning component, winding speed 600m/min obtain aromatic polyester-aliphatic polyester blocked copolyester spun filament UDY.It will come into being Silk UDY is in 50 DEG C of progress level-one drawing-offs, and 3.5 times of drafting multiple;In 60 DEG C of progress second level drawing-offs, 1.2 times of drafting multiple, later will Fiber is crimped at 90 DEG C.Then carried out shaping at 100 DEG C, the fiber after sizing prescinds on cutting machine, be packaged after obtain Aromatic polyester-aliphatic polyester blocked copolyester wool type staple fiber.
The oligoterephthalic acid glycol ester that aromatic polyester-aliphatic polyester blocked copolyester is 3 by the degree of polymerization The poly- decanedioic acid methyl propanediol ester polyol polycondensation for being 5000 with number-average molecular weight forms, wherein ethylene glycol terephthalate The mass ratio of oligomer and poly- decanedioic acid methyl propanediol ester polyol is 100:40, and the inherent viscosity of copolyester section is 0.95dL/g, fusing point are 160 DEG C, and glass transition temperature is 40 DEG C, and form and aspect b value is 8, diethylene glycol content 0.8%.Copolyesters Molecular structural formula it is as follows:
Wherein x=4.05, y=1.42, the degree of randomness of copolyesters are 0.95.
Embodiment 9
Example 8 prepares resulting aromatic polyester-aliphatic polyester block copolymerization ester fiber, wool, according to 40/60 Mass ratio carry out blended, yams 16S, it is made into the knitted fabric of square meter grammes per square metre 200-280g, is then dyed, is contaminated Color technique is disperse dyes and acid dyes normal pressure one bathes step dyeing, and the specific pH that dyes is 5.0, acid dyes and disperse dyes It is added simultaneously, begin 30-40 DEG C of temperature of dye, and 98-100 DEG C of dyeing temperature, dyeing soaking time is 30-60min, and heating rate is 1.0-1.5 DEG C/min, rate of temperature fall is 1.2-2.0 DEG C/min after dye, is cooled to 65 DEG C of drains, then 80 DEG C soap it is primary, 80 DEG C hot water washs 2 times.
Obtained fabric color is vivid, even dyeing, and dyes that firmness is good, and feel is soft, and dimensionally stable Property is good, high-end to improve grade.
Comparative example 1
Copolyester section is entered after screw extruder melts to filament spinning component, winding speed 4200m/ at 280 DEG C Min obtains aromatic polyester-aliphatic polyester blocked copolyester fully drawn yarn FDY.Wherein, the speed 1500m/ of hot-rolling GR1 Min, temperature are 80 DEG C, and the speed of hot-rolling GR2 is 4250m/min, temperature is 140 DEG C.
Copolyesters by terephthalic acid (TPA), ethylene glycol, adipic acid, methyl propanediol is quarternary copolymerized forms, wherein terephthaldehyde The molar ratio of acid and ethylene glycol is 1:1.15, and the molar ratio of terephthalic acid (TPA) and modifying agent adipic acid and methyl propanediol is 10:1.The inherent viscosity of copolyester section is 0.72dL/g, and fusing point is 221 DEG C, and glass transition temperature is 68 DEG C, form and aspect b value It is 9, diethylene glycol content 1.9%.The molecular structural formula of copolyesters is as follows:
Wherein x=9.89, y=1.03, the degree of randomness of copolyesters are 1.07.
Experimental example 1
It will be to fiber prepared by embodiment 1-8 and comparative example 1 below beneficial effect in order to further illustrate the present invention Performance is tested, and test item is as follows: line density (dtex), test method: staple fiber is long referring to GB/T 14335-2008 Silk is referring to GB/T 14343-2008;Breaking strength (cN/dtex) and extension at break (%), test method: staple fiber is referring to GB/T 14337-2008, long filament is referring to GB/T14344-2008;Boiling water shrinkage (%): referring to GB/T 6505-2008;Dye-uptake (%), test method: referring to GB/T 23976.1-2009;Dyefastness (grade), test method: referring to GB/T 3921-2008.
Test result is shown in Table 1.
Table 1
From table 1 it can be seen that, fiber prepared by embodiment 1-8 all have fine dispersion dyestuff dyeing at normal pressure performance and Dimensional stability.
The disperse dye normal pressure dye-uptake basic one of the fiber of the spinning of copolyester section prepared by embodiment 1 and comparative example 1 Cause, but copolyester section prepared by embodiment 1 compared with the fiber that copolyester section prepared by comparative example 1 spin breaking strength with Extension at break is high, and boiling water shrinkage is low.This is because copolyesters prepared by embodiment 1 is compared with copolyesters prepared by comparative example 1 Molecule amylose regularity is high, and fiber is easier that orientation and crystallization, therefore copolyester section prepared by embodiment 1 occurs in spinning process The mechanical property and dimensional stability of the fiber of spinning are above the fiber of the spinning of copolyester section prepared by comparative example 1.
Experimental example 2
Its dimensional stability is investigated in this experiment by the horizontal and vertical washing shrinkage of test fabric.
Test sample:
1. the embodiment of the present invention 9 prepares resulting aromatic polyester-aliphatic polyester block copolymerization ester fiber/wool blended The fabric that yarn is made into;
2. referring to the fabric preparation method of the embodiment of the present invention 9, only by aromatic polyester-aliphatic polyester blocked copolyester Fiber is changed to functionality copolyester fiber described in embodiment 1, other factors in ZL02111210.X and remains unchanged, obtain Fabric;
3. referring to the fabric preparation method of the embodiment of the present invention 9, only by aromatic polyester-aliphatic polyester blocked copolyester Fiber is changed to modified copolymer ester fiber as described in example 2, other factors in CN201110366748.X and remains unchanged, obtain The fabric arrived.
Test method:
5 pieces are sampled first on the fabric of each sample, every piece of specimen size size is transverse direction 40cm, and longitudinal is 35cm, is The influence for preventing edge fabric, in the rectangle of one transverse direction 30cm of each sample central marker, longitudinal direction 25cm, then to examination Sample is dyed, heat setting is handled, and then light base fabric center after treatment does the rectangle of the transverse direction longitudinal direction a 20cm 15cm.
According to international FZ/T 01014-91 by fabric washing 5 times, the transverse direction of 5 pieces of fabrics of each sample sampling is tested respectively With longitudinal washing shrinkage, and average value is calculated separately, test result is referring to following table.
Table 2
It can be seen that test specimen 1. according to above test result, i.e., resulting virtue prepared using the embodiment of the present invention 9 The fabric that fragrant adoption ester-aliphatic polyester block copolymerization ester fiber/wool blended yarn is made into, 2. and 3. relative to test specimen, It is more preferable with lower lateral washing shrinkage and longitudinal washing shrinkage, the dimensional stability of fabric.
And the difference between three kinds of fabrics is only in that the embodiment of the present invention 9 uses fragrant adoption of the present invention Ester-aliphatic polyester block copolymerization ester fiber, the method and other parameters of preparation and the method for test be it is identical, because This, uses aromatic polyester of the present invention-aliphatic polyester block copolymerization ester fiber and protein fibre mixed interweaving can be with It assigns fabric more excellent dimensional stability, is more in line with weaving and apparel industry for the quality requirement of its product, has Broader market prospects can bring better economic benefit.
Experiment content of the invention is not limited only to content listed above, and inventor is in R&D process to it The resulting fabric of his embodiment has also carried out similar test, obtained result with it is above-described same or similar.
The above is only presently preferred embodiments of the present invention, is not intended to limit the present invention in any form.Appoint What is familiar with the technical staff of this patent on the basis of not departing from technical solution of the present invention essence, when the skill using above-mentioned prompt Art content makes a little change or the equivalent embodiment for being modified to equivalent variations, but all without departing from technical solution of the present invention Hold, any simple modification, equivalent change and modification to the above embodiments, still fall within according to the technical essence of the invention In the range of the present invention program.

Claims (8)

1. a kind of aromatic polyester-aliphatic polyester block copolymerization ester fiber, which is characterized in that aromatic polyester-aliphatic poly Ester blocked copolyester is formed by oligoterephthalic acid glycol ester and aliphatic polydiacid diol ester polyhydric alcohol, And there is following chemical structure:
Wherein, the ratio of 4 < x <, 100,1 < y < 25, x and y are x:y=4~54:1, R1For C2~C8 alkylidene, R2For C3~ C8 alkylidene;Aromatic polyester-aliphatic polyester blocked copolyester degree of randomness B is 0.05~0.95, and the degree of randomness B is used Public formula (I) calculates:
Wherein: TA is terephthalic acid (TPA), EG is ethylene glycol, SA is straight-chain aliphatic binary acid, BO is pendant aliphatic dihydric alcohol; FTA-EGMolar fraction, F for ethylene glycol terephthalate repetitive unitTA-BOFor terephthalic acid (TPA) pendant aliphatic dihydric alcohol The molar fraction of ester repetitive, FSA-BOFor straight-chain aliphatic binary acid pendant aliphatic binary alcohol esters repetitive unit mole point Number, FSA-EGFor the molar fraction of straight-chain aliphatic binary acid glycol ester repetitive unit;
Aromatic polyester-aliphatic polyester blocked copolyester inherent viscosity is 0.5~1.2dL/g;
Aromatic polyester-aliphatic polyester blocked copolyester fusing point is 160~250 DEG C;
Aromatic polyester-aliphatic polyester blocked copolyester glass transition temperature is 40~77 DEG C;
The aromatic polyester-aliphatic polyester blocked copolyester is prepared using following method, is included the following steps:
(1) proper catalyst preparation is added in the terephthalic acid (TPA) and ethylene glycol mixture that molar ratio is 1:1.05~2 to be slurried Material;
(2) slurry being prepared in step (1) is subjected to esterification, obtains oligoterephthalic acid glycol ester;
(3) after the oligoterephthalic acid glycol ester that step (2) is prepared being adjusted the temperature to 200~250 DEG C with The aliphatic polydiacid diol ester polyalcohol of line addition is uniformly mixed, and then carries out prepolymerization reaction, it is pre- to obtain copolyesters Polymers;
(4) copolyester prepolymer that step (3) is prepared carries out final polycondensation reaction, obtains copolyesters melt;
(5) by step (4) be prepared copolyesters melt by filtering after cool and solidify, be made copolyester section.
2. aromatic polyester according to claim 1-aliphatic polyester block copolymerization ester fiber, which is characterized in that fragrance Adoption ester-aliphatic polyester blocked copolyester form and aspect b value is 1~8;
Content≤1.5% of aromatic polyester-aliphatic polyester blocked copolyester diethylene glycol (DEG).
3. aromatic polyester according to claim 1-aliphatic polyester block copolymerization ester fiber, which is characterized in that described Aliphatic polydiacid diol ester polyalcohol in binary acid be straight-chain aliphatic binary acid, dihydric alcohol is pendant aliphatic Dihydric alcohol;
The straight-chain aliphatic binary acid is succinic acid, adipic acid or decanedioic acid, and the pendant aliphatic dihydric alcohol is first Base propylene glycol, neopentyl glycol, 2- methyl -2,4-PD, 3- methyl-1,5- pentanediol or trimethylpentanediol.
4. aromatic polyester according to claim 3-aliphatic polyester block copolymerization ester fiber, which is characterized in that described The number-average molecular weight of aliphatic poly Straight chain diatomic acid side group binary alcohol esters is 300~10000.
5. aromatic polyester according to claim 1-4-aliphatic polyester block copolymerization ester fiber, feature exist In the mass ratio of oligoterephthalic acid glycol ester and aliphatic polydiacid diol ester polyalcohol is 100:3~40.
6. aromatic polyester according to claim 1-4-aliphatic polyester block copolymerization ester fiber, feature exist In by aromatic polyester-aliphatic polyester blocked copolyester progress melt spinning, the spinning temperature used is 180~300 DEG C.
7. aromatic polyester according to claim 1-4-aliphatic polyester block copolymerization ester fiber, feature exist In with disperse dyes to the aromatic polyester-aliphatic polyester blocked copolyester stock-dye under normal pressure, dye-uptake is at least It is 85%;
Dyefastness is at least 4 grades;
Boiling water shrinkage is 1~8%.
8. a kind of be used to make by the described in any item aromatic polyesters of claim 1-7-aliphatic polyester block copolymerization ester fiber Purposes for pure spinning textile or with cotton, wool, silk, spandex intertexture or blended textile.
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